Re: FW: VERY DANGEROUS PC VIRUS

2008-11-13 Thread Todd Williams - FPDC
Read this before everybody freaks. 
http://urbanlegends.about.com/library/bl_postcard_virus.htm




Todd G. Williams, PE
Fire Protection Design/Consulting
Stonington, Connecticut
www.fpdc.com
860.535.2080  
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Re: Fire line FDC and Inside controls

2008-11-13 Thread Todd Williams - FPDC

The FDC has to be installed downstream of the backflow



At 03:48 PM 11/13/2008, you wrote:

Forum,
I have a situation where the fire department is requiring a post 
indicator valve and free standing FDC outside the building.  We will 
also need a backflow preventer installed inside in the sprinkler 
control room.  Is it permissible to install the FDC so it ties into 
the fire line prior to the backflow control valves, or would we need 
to install a separate FDC line into the building?
I know 8.16.1.1.1.3 does not allow a shutoff valve in the line, but 
it seems contradictory with Figure A.8.16.1.1 2007 NFPA 13.

Thanks,
Jamie Seidl
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Todd G. Williams, PE
Fire Protection Design/Consulting
Stonington, Connecticut
www.fpdc.com
860.535.2080  
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RE: design and coordination roles and responsibilities.

2008-11-12 Thread Todd Williams - FPDC
One of the consistent problems we have up here is the electrician. 
They don't take part in the coordination process, they often don't 
even have CAD drawings and they just run everything where they want. 
And the GC's tend to let them get away with a lot of it. I find that 
more problems with the architect's concepts surface in the sprinkler 
design that any of the other trades.



At 11:54 AM 11/12/2008, you wrote:
Well if you want to be innovative then by all means be so.  On 
projects such as this if the contractor has a better idea, I'm all 
for it and then we will sit down and see how it will integrate into 
the overall picture.  But if there was no direction given on 
projects like this where there's 20lbs stuffed in the 10lb bag, 
guess who will be the loser every time, you guessed it boys and 
girls, the sprinkler contractor.


So if you get innovative and there's extremely limited space and you 
venture off on your own, get ready to install it and reinstall it 
more than once, at your expense.  Did you coordinate like the specs 
directed you?


The problem with a lot of AE firms is even IF they do have competent 
design/3D modeling persons, they can't coordinate with something 
that isn't there.  If it's not in the model, it doesn't exist is 
pretty much the normal viewpoint.  So if you're not part of that 
effort, you're on your own.  Hope you bid high enough.


Fire protection is always treated as the red-head step child in 
the engineering world.  To most people fire protection is a waste of 
money, it makes no profit, is expensive and takes up valuable space, 
then it becomes a life-long maintenance headache.  So any time we 
can get it recognized as being a vital discipline and building 
system and included in any level of detail in the overall project 
design, I'll take it.


We're just trying to put a better product on the streets than the 
typical big X on the drawing whenever possible to make the more 
complex projects flow better.  Hopefully at the end of it all 
everybody goes home with a few more bucks in their pocket and a 
positive experience, instead of saying OH $%^* I wish we had never 
taken that job!


Oh and I know that ALL disciplines have been engineering in 3D since 
the beginning of time.


Craig L. Prahl, CET
Fire Protection Specialist
Mechanical Department
CH2MHILL
1500 International Drive
PO Box 491, Spartanburg, SC  29304-0491
Direct - 864.599.4102
Fax - 864.599.8439
[EMAIL PROTECTED]
http://www.ch2m.com


-Original Message-
From: [EMAIL PROTECTED] 
[mailto:[EMAIL PROTECTED] On Behalf Of Fletcher, Ron

Sent: Tuesday, November 11, 2008 1:14 PM
To: sprinklerforum@firesprinkler.org
Subject: RE: White papers and definition of roles

Right on George. With all the special systems I would expect more 
than $2k difference in the specialty equipment quotes and the prices 
should be closer if you take away the opportunity for innovation of 
design by the bidders.


Our prices are higher on jobs requiring 3D or BIM. We find there is 
very little coordination and more here is where we are so now you
(sprinkler) can go around us. It's like a 3D retrofit. The only 
thing that changes is we spend more design time to come up with the 
same product. Besides we FP contractors have been doing 3D since the 
beginning of time, it's just that the presentation has been 2D.


Ron Fletcher
Aero Automatic
Phoenix, AZ

-Original Message-
From: [EMAIL PROTECTED]
[mailto:[EMAIL PROTECTED] On Behalf Of George Church
Sent: Tuesday, November 11, 2008 7:00 AM
To: sprinklerforum@firesprinkler.org
Subject: RE: White papers and definition of roles

Ummm, maybe the two bidders had breakfast together on bid morning?
Don't throw your elbow out patting yourself on the back.

Coincidence or a comp price is far more likely to produce bids 
within .001% of each other than quality of the bid documents.


Seriously, if you'd given em a stocklist, a finished, coordinated 
dwg, and a rational schedule, there'd be more difference in the 
price than this just on how different companies allocate OH, backlog 
needs, lift pricing renting vrs owning, mileage from office to site 
variance, mix of each contractor's design talent pool $ cost, 
workman's comp experience reflected in what could be drastically 
different rates, skill of the two estimators, whether someone got 
something last night- There are so many variables, I'd suspect a 
comp number before a headless piping layout as the root cause for 
the close resemblance.


glc

-Original Message-
From: [EMAIL PROTECTED]
[mailto:[EMAIL PROTECTED] On Behalf Of 
[EMAIL PROTECTED]

Sent: Tuesday, November 11, 2008 8:46 AM
To: sprinklerforum@firesprinkler.org
Subject: RE: White papers and definition of roles

Speaking of bid prices.  We performed our first AutoCAD based 3D 
integration of fire protection on a recent project.  Our typical 
corporate deliverable is the design criteria and a floor plan with 
equipment on it.  (I have had a couple 

Re: Viking concealed sprinkler

2008-11-11 Thread Todd Williams - FPDC

It needs to be replaced?



At 08:38 PM 11/10/2008, you wrote:

Hi
What does purple paint on a Viking concealed sprinkler indicate?
Thanks
Forest Wilson
Cherokee Fire
Sent from my Verizon Wireless BlackBerry

-Original Message-
From: Terri Leyton [EMAIL PROTECTED]

Date: Mon, 10 Nov 2008 08:51:17
To: sprinklerforum@firesprinkler.org
Subject: RB-64, Home Builders Assn. Letter


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Todd G. Williams, PE
Fire Protection Design/Consulting
Stonington, Connecticut
www.fpdc.com
860.535.2080  
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RE: White papers and definition of roles - segue #4

2008-11-11 Thread Todd Williams - FPDC

Welcome to the world of 3D. The only way to go

Todd Williams
Autosprink and former Fireacad user



At 08:45 AM 11/11/2008, you wrote:
Speaking of bid prices.  We performed our first AutoCAD based 3D 
integration of fire protection on a recent project.  Our typical 
corporate deliverable  is the design criteria and a floor plan with 
equipment on it.  (I have had a couple complete installation level 
design requests but they are rare in this industry)  Typical 
criteria based design, no piping, or heads or anything 
else.  (because the contractor will do it for free).  Anyway,  as 
we've progressed into the 3D realm I've pushed to get fire 
protection included in the 3D modeling.  Convincing the powers that 
be that by at least including mains and branch lines into the model 
and coordinating their locations and elevations will aid the 
contractor during installation, reduce his design time and reduce 
change orders and bring us tighter bids as there is less for the 
imagination and more solid information to work with.


So they let us do the piping layout but no heads, so we did the 
layout in the model dealing with equipment, steel and other modeled 
obstructions.


Two weeks ago the project went out for bids.  We had 3 bidders.  One 
dropped out due to various personal reasons but the bids came back 
yesterday from the other two.


The fire protection bids on the project were within $2,000 of each 
other.  Now that may not sound like a big deal but understand the 
total above ground fire protection is valued at almost $1.5 million dollars.


For two bidders to be that close is pretty unusual.  But it 
validated the need for better design other than the old floor plan 
with the note follow NFPA 13 and similar stuff.


Hopefully we can continue this trend within our company.  I know 
this would be difficult for many companies because there is a lack 
of qualified people who can actually layout a fire protection system 
and this project ran the gamut of system types from wet, dry, 
pre-action, foam-water deluge, low expansion foam, dry chemical, CO2 
and a proprietary, IR triggered, high speed, deluge curtain system 
(that is really cool by the way).


Now I'm hoping that our management sees the value in this effort and 
will continue down this path.  Convincing some to allow us to 
provide more than the bare minimum of fire protection information is 
a tough fight.  For whatever reason is has been for years.  Maybe it 
has to do with the lack of qualified people, some of it is based on 
economics, some of it is perceived value, like I said, most AE firms 
feel the contractor provides the engineering effort for free so why 
do anything other than a spec and some fancy notes.


I actually had one PM complain that the sprinkler contractors ALWAYS 
put their pipe in the wrong place and it has to be torn down and 
removed.  He caught me on a good day so I graciously (stop 
snickering)  reminded him of the directive we typically give 
sprinkler contractors:  1. coordinate with everyone and 
everything.  But at the same time all we give them is a floor plan 
of the building, no process piping layouts (because there is no such 
animal), no steel plans, no duct layouts, etc.  So how can he 
coordinate with things that don't exist or haven't been designed 
yet?  Hence my sales pitch for getting it in the model and then 
giving that info to the contractor.


But this is one I will put in the WIN column.  They come far and few 
between so forgive me while I savor the moment





Craig L. Prahl, CET
Fire Protection Specialist
Mechanical Department
CH2MHILL
Lockwood Greene
1500 International Drive
PO Box 491, Spartanburg, SC  29304-0491
Direct - 864.599.4102
Fax - 864.599.8439
[EMAIL PROTECTED]
http://www.ch2m.com


-Original Message-
From: [EMAIL PROTECTED] 
[mailto:[EMAIL PROTECTED] On Behalf Of Mark Sornsin

Sent: Monday, November 10, 2008 6:16 PM
To: 'sprinklerforum@firesprinkler.org'
Subject: RE: White papers and definition of roles

Then there are those jurisdictions such as ND where you not only 
don't get registered in a specific discipline, but complaints will 
not be investigated unless there is a problem with the design. E.g., 
simply being trained in structural engineering and signing someone's 
sprinkler system design is not a problem that will be 
investigated.  It may violate the engineers' code of ethics, but it 
won't see action from the State Board unless there arises some issue 
with the design. So if you're a PE not trained in sprinkler design, 
just get some non-PE designer to complete the work and then you can 
seal it. Effectively there is no problem.  If the building burns as 
a result of improper design, then you've got a problem.


Of course, how many MEs even attempt to design a system?  It's 
pretty difficult to hold an engineer to the fire when his design 
boils down to do it per code. I have had MEs ask me why I would 
ever attempt to provide a complete 

Re: White papers and definition of roles

2008-11-11 Thread Todd Williams - FPDC
I had another phrase in mind other than shut up, but the gist is 
the same. Thank you for the pro bono professional consultation.




At 04:59 PM 11/10/2008, you wrote:

Todd,

I can provide some assistance with all six of your concerns.
1) Tell him to shut up
2) Tell him to shut up
3) Tell him to shut up
4) Tell him to shut up
5) Tell him to shut up
6) Tell him to shut up or identify himself [gotta throw a little 
diversity in there]


As you are a fellow professional, there will be no charge for this assistance.
PARSLEY CONSULTING
Ken Wagoner, SET
760.745.6181 voice
760.745.0537 fax
[EMAIL PROTECTED] mailto:[EMAIL PROTECTED] e-mail
www.ParsleyConsulting.com http://www.ParsleyConsulting.com website



Todd Williams - FPDC wrote:
Personally, I don't think any one profession has a lock on either 
ignorance or stupidity. Right now I have to deal with the 
following: 1) an architect who can't figure out how to provide 
separate areas for a wet and dry system; 2) an AHJ who rejected a 
plan because it didn't show the riser nipples per NFPA 13 (there 
aren't any); 3) a contractor who filed a grievance against my 
license because I drew a plan for a job he was thrown off of; 4) an 
engineer who can't grasp why 4 pipe can't go through a 2-1/2 
space; 5), a building owner who can't understand why he can't feed 
three standpipes from a 250 gpm pump; and 6) a mystery designer 
whose calculations he used for the hydraulic placard were off by 
250 psi. Talk about multi-cultural.



Todd G. Williams, PE
Fire Protection Design/Consulting
Stonington, Connecticut
www.fpdc.com
860.535.2080 ___
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No virus found in this incoming message.
Checked by AVG - http://www.avg.com Version: 8.0.138 / Virus 
Database: 270.9.0/1778 - Release Date: 11/9/2008 2:14 PM





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Todd G. Williams, PE
Fire Protection Design/Consulting
Stonington, Connecticut
www.fpdc.com
860.535.2080  
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RE: Viking concealed sprinkler

2008-11-11 Thread Todd Williams - FPDC

Barney was there?

Seriously, folks A purple glass bulb would be for 300 degree 
sprinklers, but the paint would be red. Is the paint all over the 
sprinkler or just in certain areas? Could it be a custom finish for a 
specific area?




At 07:03 AM 11/11/2008, you wrote:

Really bad taste?

-Original Message-
From: [EMAIL PROTECTED]
[mailto:[EMAIL PROTECTED] On Behalf Of Todd Williams
- FPDC
Sent: Tuesday, November 11, 2008 5:22 AM
To: sprinklerforum@firesprinkler.org
Subject: Re: Viking concealed sprinkler

It needs to be replaced?



At 08:38 PM 11/10/2008, you wrote:
Hi
What does purple paint on a Viking concealed sprinkler indicate?
Thanks
Forest Wilson
Cherokee Fire
Sent from my Verizon Wireless BlackBerry

-Original Message-
From: Terri Leyton [EMAIL PROTECTED]

Date: Mon, 10 Nov 2008 08:51:17
To: sprinklerforum@firesprinkler.org
Subject: RB-64, Home Builders Assn. Letter


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Todd G. Williams, PE
Fire Protection Design/Consulting
Stonington, Connecticut
www.fpdc.com
860.535.2080
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Todd G. Williams, PE
Fire Protection Design/Consulting
Stonington, Connecticut
www.fpdc.com
860.535.2080  
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Re: Russian sub fire

2008-11-10 Thread Todd Williams - FPDC

If I recall my history, wasn't phosgene used quite a bit during WWI?



At 09:28 AM 11/10/2008, you wrote:

Freon! If they used freon (R-12
) it's no wonder that fatalities occured. When freon and flame combine the
product is a deadly gas called phosgene.

Ergo
On Sun, Nov 9, 2008 at 9:45 AM, Stewart Kidd 
[EMAIL PROTECTED]wrote:


 According to the BBC the fire fighting gas was 'freon'

 Stewart

 On 9 Nov 2008, at 16:52, Todd Williams - FPDC wrote:

 It will be interesting to see how this plays out in the next few weeks.
 http://www.cnn.com./2008/WORLD/europe/11/09/russia.submarine/index.html

 Todd G. Williams, PE
 Fire Protection Design/Consulting
 Stonington, Connecticut
 www.fpdc.com
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Todd G. Williams, PE
Fire Protection Design/Consulting
Stonington, Connecticut
www.fpdc.com
860.535.2080  
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RE: Interesting letter from the WABO

2008-11-10 Thread Todd Williams - FPDC
Ok, I'll start this off. If organizations send people to meetings, so 
what? How many companies or other groups send people to attend 
conventions, meetings or other functions? A lot. This is pretty much 
a non-issue, in my book. Although, I can't understand how I was 
overlooked amongst the hundreds of people the sprinkler industry 
sent to Minneapolis. Who in this business has that kind of money? Are 
they hiring?


The rest of it seems to be clerical and procedural issues that the 
ICC should look into if there is probable cause. A letter from a 
disgruntled organization who lost the vote may not meet the probable 
cause criteria, but that is for the ICC to sort out.


As long as our industry is clean and ethical, we have nothing to 
worry about from things like this.



Todd G. Williams, PE
Fire Protection Design/Consulting
Stonington, Connecticut
www.fpdc.com
860.535.2080  
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RE: White papers and definition of roles

2008-11-10 Thread Todd Williams - FPDC
Personally, I don't think any one profession has a lock on either 
ignorance or stupidity. Right now I have to deal with the following: 
1) an architect who can't figure out how to provide separate areas 
for a wet and dry system; 2) an AHJ who rejected a plan because it 
didn't show the riser nipples per NFPA 13 (there aren't any); 3) a 
contractor who filed a grievance against my license because I drew a 
plan for a job he was thrown off of; 4) an engineer who can't grasp 
why 4 pipe can't go through a 2-1/2 space; 5), a building owner who 
can't understand why he can't feed three standpipes from a 250 gpm 
pump; and 6) a mystery designer whose calculations he used for the 
hydraulic placard were off by 250 psi. Talk about multi-cultural.



Todd G. Williams, PE
Fire Protection Design/Consulting
Stonington, Connecticut
www.fpdc.com
860.535.2080 
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Russian sub fire

2008-11-09 Thread Todd Williams - FPDC
It will be interesting to see how this plays out in the next few 
weeks. http://www.cnn.com./2008/WORLD/europe/11/09/russia.submarine/index.html


Todd G. Williams, PE
Fire Protection Design/Consulting
Stonington, Connecticut
www.fpdc.com
860.535.2080  
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RE: Fire Pump Suction

2008-11-07 Thread Todd Williams - FPDC





Sadly I hang my head when I hear where was the EoR.

John Drucker
Fire Protection Subcode Official (AHJ)
New Jersey


I wonder how may projects there are out there with no EoR?

Todd G. Williams, PE
Fire Protection Design/Consulting
Stonington, Connecticut
www.fpdc.com
860.535.2080  
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RE: Fire Pump Suction

2008-11-07 Thread Todd Williams - FPDC
It's nice to see that I don't get all of this stuff to figure out. I 
wonder where the EoR was on this project? I also love the term had 
access. Is this a pump he mis-ordered for another job and got stuck with?


If this were my crisis, I would run a test increasing the flow in 100 
gpm increments until I got to the -3 suction. That would give me what 
I can run the pump to flow wise. Assuming you hit the -3 before the 
600 gpm, you essentially have three choices: install the correct 
pump, change out the suction line or come up with a way to live with 
the existing situation. This would probably include discussions with 
the owner, pump rep and the AHJ. Best of luck.


I am working on a hospital with a 250 gpm pump that is trying to feed 
3 standpipes. I'll let you know when this pump becomes available (just kidding)






At 11:58 PM 11/6/2008, you wrote:

The concern is the size of the suction pipe. The pump selected was 250 gpm,
to match the 222 gpm, 40 psi demand. But the contractor had access to a 400
gpm, 70 psi pump which got installed instead. An overkill, but that is what
happened. The suction piping from the tank to the pump is 4. The engineer
is pointing to NFPA 20, 2003 section 5.14.3.2 which requires gauge pressure
at pump suction flange to be no less than -3 psi. Although the flow is not
mentioned in this particular section, from section 5.14.3.1 it can be
deduced that it is 150% of the rated flow. Now flowing 600 gpm through the
4 suction piping and avoiding cavitation is the problem.

Tony

-Original Message-
From: [EMAIL PROTECTED]
[mailto:[EMAIL PROTECTED] On Behalf Of Chris Cahill
Sent: November 6, 2008 1:59 PM
To: sprinklerforum@firesprinkler.org
Subject: RE: Fire Pump Suction

If I understand your concern you are worried the tank will run out before 30
minutes because of overflow due to a supply calc vs. a demand calc.  You are
worried about calc'ed world vs. real world.  Fine but in what real world
will the actual design area operate.  Odds are you won't be in the remote
area which increases overflow meaning less than 33 minutes.  Odd are less
than the calc'ed number of heads will flow decreasing the demand meaning
more than 33 minutes.  Odds are 2 heads (or less) will flow and you won't
have anywhere near 222 gpm coming out.  This probability is the driving
force showing in reality the tank will last more than 33 minutes.

Overflow is good from a fire suppression standpoint anyway.  More water per
time equals higher probability of suppression and quicker time.  It's also
not linear, you get more bang for the buck with increase in density.  I
don't know of specific figures, just going from experience.  If you put the
fire out in 10 minutes and the tank runs dry in 20 is there a problem?

IMHO the system failed if the full remote area operates in the first place.
Or at least a serious investigation is warranted to determine why.  If you
still need the sprinklers after about 10-15 minutes there is a problem.  The
extra heads and 30 minutes already have a deal of safety in them.

The actual produced is always a balance between flow and available pressure.
So yes if the entire remote area opens you will in reality drain the tank
faster than 33 minutes.  Could be much quicker depending on the shape of the
pump curve and the overflow.  But assuming you are light hazard based on the
very little information provided I don't see a problem.  If you are really
curios start running system supply calc's for different areas and you should
see the tank will never last 33 minutes with a full sized calc'ed area and
much longer when less than the full area.

Now maybe you are 45 minutes from the closest FD and this becomes an
engineering question to consider. Some day the code may differentiate
between available levels of fire service but not yet.

But hey maybe I missed the point of your question.

Chris Cahill, P.E.
Fire Protection Engineer
Sentry Fire Protection, Inc.

763-658-4483
763-658-4921 fax

Email: [EMAIL PROTECTED]

Mail: P.O. Box 69
Waverly, MN 55390

Location: 4439 Hwy 12 SW
  Waverly, MN 55390
-Original Message-
From: [EMAIL PROTECTED]
[mailto:[EMAIL PROTECTED] On Behalf Of A.P.Silva
Sent: Thursday, November 06, 2008 2:11 PM
To: sprinklerforum@firesprinkler.org
Subject: RE: Fire Pump Suction

The maximum sprinkler demand as per hydraulic calcs. is 222 gpm. The water
supply is by means of storage tanks having a total volume of 7448 gallons.
Just barely enough for approx. 33 minimute at maximum demand. The contractor
has installed a 400 gpm fire pump. NFPA 20 requires gauge pressure at the
fire pump suction flange to be 0 psi or higher when pump is operating at
150% of rated flow, which in this case is 600 gpm. Is this realistic? I
know, if the suction pressure is 0 psi or higher for 600 gpm flow, it will
work for all cases. However, I would expect a flow between the supply and
demand with all design sprinklers flowing. Anyone with experience with

RE: -- Fire on exterior wall of a building

2008-11-07 Thread Todd Williams - FPDC

Valve or FDC
sleep with one eye open
or oft up to p

Haiku


At 03:10 PM 11/7/2008, you wrote:

Manual valve or FDC,
sleep with one eye open,
or often get up to p

Longfellow

-Original Message-
From: [EMAIL PROTECTED]
[mailto:[EMAIL PROTECTED] On Behalf Of å... 
Sent: Friday, November 07, 2008 1:39 PM
To: sprinklerforum@firesprinkler.org
Subject: -- Fire on exterior wall of a building

 sprinklerforum@firesprinkler.org


To take the fire on an exterior balcony and give it a slight twist,
consider this...

I have someone in a cold town, with many 4 story wooden buildings.
Owner of one of these buildings wants
protection of their 4 story structure (wood cornices,
wooden exterior paneling and windows) from fire in their neighbor's
structure.  Some buildings were lost as fire extended from
original structure onto exposures.

Freezing is a problem.

Neighbor's structure is 15 feet away.
Both structures have windows at each level,
and my building has ornate 3 ft wooden cornice.


I am considering a compliment of
   old-school open cornice sprinklers for the cornices
   and open window sprinklers (same manuf. makes both)
   for the windows and exterior paneling
   Using 15 psig I can use get a 20 ft wide coverage.

These are open sprinklers,
so we will provide a unique FDC to this exterior system.
but connecting to the city main would be a good back up plan,
using a simple control valve to hold back the deluge on the
one exterior wall facing the neighbor.


I can see the need to provide sprinklers underneath each window,
as the water coming from above, will not flow down over a broken
window, and i can see a sprinkler over each window, for reasons
that windows break... but where on the exterior wall there is
a continuous vertical path from cornice to ground, what vertical
interval is suggested for prevention of radiative or brand/piloted ignition?


I am not trying to meet a code. I have read NFPA 80A.  Here,
I am trying to meet a clients performance objective.
Save my wooden building, if and when my neighbor's building
is burning.


scot deal
excelsior fire
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www.fpdc.com
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Re: Fire resistant barriers between transformers

2008-11-06 Thread Todd Williams - FPDC
There is a pre-fab fire barrier system that is used on off-shore oil 
rigs. That might be a place to look




At 10:04 AM 11/6/2008, you wrote:

Fellow forumites,

I realize this is not a sprinkler related topic, but it is fire protection
related.

Does anyone know of prefab or easy site built fire barrier walls?

Our client is wanting to know if there are cheaper alternatives to
building cast in place concrete barriers to separate oil filled
transformers.

Thanks in advance.

James L.(Jim) Roberts, PE/SET
Fluor Corporation
100 Fluor Daniel Drive - C104F
Greenville, SC 29607
864.281.5149
864.281.4916(Fax)

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Any views expressed in this message are those of the individual
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Re: Plastic rack storage question

2008-11-06 Thread Todd Williams - FPDC
Craig is on target with his observation. I had posted something else 
regarding mixed commodities a while back and I believe Joe Hankins 
chimed in with some good explanation as to why it would have to be 
designed based on the most hazardous product.




At 11:19 AM 11/6/2008, you wrote:

We have a building that has some rack storage of plastic products.  We
are following FM data sheet 8-9 for the design criteria.
The maxim storage for this product is 25ft in a 45ft building for the
design criteria chosen.  The owner would like to store a lesser
class commodity above the plastics.  IE: Build the racks to 35ft. store
plastics for 25ft and fill the remainder with a different commodity.
If the overhead design is capable of supporting this, can it be done?  I
have done some oil storage racks where this was allowed.
Thanks,
Dewayne
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RE: water test standards

2008-11-04 Thread Todd Williams - FPDC

Thank you

TAt 08:50 AM 11/4/2008, you wrote:

NFPA 291

-Original Message-
From: [EMAIL PROTECTED]
[mailto:[EMAIL PROTECTED] On Behalf Of Todd
Williams - FPDC
Sent: Tuesday, November 04, 2008 6:47 AM
To: sprinklerforum@firesprinkler.org
Subject: water test standards

I think I am going through a cerebral meltdown. Where is the NFPA
reference for hydrant flow testing?

Todd G. Williams, PE
Fire Protection Design/Consulting
Stonington, Connecticut
www.fpdc.com
860.535.2080
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Re: Attic Rule

2008-11-04 Thread Todd Williams - FPDC

Jimmy,

I would assume that there is no engineer to throw this question back 
on. I have looked at some similar situations and have used a couple 
of approaches:


First, I try to get them to fill the space with insulation, thus 
eliminating the need for sprinklers.


Next I try to take a practical approach and see what it would take to 
flood the space and get coverage. The typical spacing rules are 
probably out the window, because you physically can't meet all on 
them. I don't know how long this space is, but it sounds similar to 
the canopies on strip malls. I tend to keep the deflector distance 
and distance from the peak within code, make sure the single 
sprinkler can get water to the entire cross-section of the space and 
shrink the sprinkler spacing (8-10 ft instead of 12-14). If a single 
sprinkler goes off in this space, it is probably going to flood it in 
a matter of seconds.


The previous being said, each situation has to be looked at 
individually and what works in one might not in another. You'll have 
to spend some time trying to figure out what is going to happen. 
(yes, that is a disclaimer) It would be also good to talk with the 
AHJ about it. You want to make sure he is on board.


Todd



At 11:38 AM 11/4/2008, you wrote:

Dear Forum Members,  We are working on a retrofit for a church.  The
building is entirely wood construction, built with large glu-lams and 14
composite trusses (parallel to the glu-lams).  We are protecting a small
cold space above a balcony.  The roof pitch is 12 in 12, and the cold space
dies into a full height wall.  So the space is a right triangle (with the
slope being the hypotenuse), instead of a typical attic and a typical peak.
8.6.4.1.4.2 (07) says I have to have a head within 12 of the bottom of the
top chord (TJI).  First, does this rule still apply when I don't have a two
slopes to protect?  Secondly, if this rules does apply, I'd have to add a
second line (in a very small space) and I couldn't maintain 6 feet between
heads, while still being more than 5 feet from the eave?  Please help.


Thanks

Jimmy Waite
Burtell Fire Protection
406-652-7697
[EMAIL PROTECTED]


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Re: Fire Pump Suction

2008-10-31 Thread Todd Williams - FPDC
That is a very legitimate concern. My guess is that you could very 
easily have a problem, especially if your static head is less that 
4.6 psi. In my experience, there are very few good uses for 4 pipe 
prior to the system riser. With 6 pipe, your friction loss would be 
about 2 psi.




At 01:32 PM 10/31/2008, you wrote:


400 gpm fire pump supplied from tanks with suction flanges higher than pump
suction flange. Approximately 100 feet of 4 piping (including fittings)
from tanks to pump. NFPA 20 permits the gauge pressure at the pump suction
flange to drop to -3 psi, with the pump flowing at 150% (600 gpm in this
case). The friction loss in the piping for 600 gpm flow is about 7.6 psi. Is
there a concern for the pressure available at the pump suction, when the
water level drops in the tanks? I have been told that it will, so checking
the opinion of the forum.

Tony

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RE: Mezz design area

2008-10-30 Thread Todd Williams - FPDC

Russell,

If you do the calc, why not submit it with the package?



At 07:55 AM 10/30/2008, you wrote:

I always calc. beneath a mezzanine and may or may not include them with my
submittal package for AHJ approval, but rather to have them just in case
they are requested and as not to find out that the piping I've already had
fabricated and in most cases installed just to find that it doesn't meet the
demand. Besides, how else could you come up the pipe sizes if you don't?
With experience one can usually get it right by guessing but I find that I'm
fooled sometimes too. Don't like to have egg on my face. That's just the way
I usually approach the situation. This may not even be connected to what you
are asking. If not, please except my apologies.

Russell Rewis
Brown Automatic Sprinklers, Inc.
107C Hemlock Street
Valdosta, Georgia 31601
229-244-8130
[EMAIL PROTECTED]



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flow test conundrum

2008-10-29 Thread Todd Williams - FPDC
I did a couple of flow tests last night and the results, to me, don't 
make sense. There is a looped 6 main in Liberty St and a dead end 6 
that branches off to Chase St. There is a hydrant at the intersection 
where we read pressures (P), a hydrant on Liberty that we flowed (F1) 
and one on Chase St that we also flowed (F2). For the first test, we 
flowed F1 and read the pressures at P. We got a static of 90 psi, and 
a residual of 72 psi at a flow of 470 gpm. On the second test, we 
flowed F2 and read the pressures again at P. Those results were a 
static of 90 psi and a residual of 26 psi at a flow of 380 gpm. The 
tests were done about 15 minutes apart. I am having a hard time 
reconciling these two tests. The water department foreman said that 
the 6 main in Chase St could be severely tuberculated, but offered 
no other options.  If that were the case, I would have thought that 
both the flow and pressure would have been dramatically different. 
Any thoughts? Of course the project in question is at the end of 
Chase St, but fortunately, there is brand new 6 PVC main from the 
hydrant to where the building is.


The other irony is that this 6 is connected to a 12 main about 0.1 
miles away. A test on the 12 in 2006 had a static of 82 and a 
residual of 80 at a flow of 1400 gpm.


I am going to the water department today to look at the system amps. 
Perhaps there is a weird piping configuration that creates this 
disparity. SSDP (P stands for project)


Todd G. Williams, PE
Fire Protection Design/Consulting
Stonington, Connecticut
www.fpdc.com
860.535.2080 
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RE: flow test conundrum

2008-10-29 Thread Todd Williams - FPDC
Ed, that is exactly what I was thinking. The residual pressure should 
be much higher on the second test. I read the gauges personally and 
verified the flows. Hydrant P ties into the 6 on Liberty St about 10 
ft from the connection to Chase. Given the difference between the 
2006 flow test abut 1/4 mile away on Liberty (12 main that connects 
to 6) and the Liberty St test last night, it seems to me that there 
may be a systemic problem, not just this connection.




At 09:00 AM 10/29/2008, you wrote:

Todd, it makes sense that F2 would flow something less than F1, but the huge
difference in residuals blows me away.  The 2nd flow test should have given
a residual closer to 78, not 26.  Something is definitely amiss.

Did you personally read the static/residual gauge of both tests?
Does hydrant P tie into the looped main on Liberty, or does it tie into the
dead-end main on Chase?  If it ties into the dead-end main, there could be a
major restriction somewhere between the point the 2 mains connect and the
point where hydrant P connects.

Ed Kramer
Littleton, CO

 -Original Message-
 From: [EMAIL PROTECTED] [mailto:sprinklerforum-
 [EMAIL PROTECTED] On Behalf Of Todd Williams - FPDC
 Sent: Wednesday, October 29, 2008 4:20 AM
 To: sprinklerforum@firesprinkler.org
 Subject: flow test conundrum

 I did a couple of flow tests last night and the results, to me, don't
 make sense. There is a looped 6 main in Liberty St and a dead end 6
 that branches off to Chase St. There is a hydrant at the intersection
 where we read pressures (P), a hydrant on Liberty that we flowed (F1)
 and one on Chase St that we also flowed (F2). For the first test, we
 flowed F1 and read the pressures at P. We got a static of 90 psi, and
 a residual of 72 psi at a flow of 470 gpm. On the second test, we
 flowed F2 and read the pressures again at P. Those results were a
 static of 90 psi and a residual of 26 psi at a flow of 380 gpm. The
 tests were done about 15 minutes apart. I am having a hard time
 reconciling these two tests. The water department foreman said that
 the 6 main in Chase St could be severely tuberculated, but offered
 no other options.  If that were the case, I would have thought that
 both the flow and pressure would have been dramatically different.
 Any thoughts? Of course the project in question is at the end of
 Chase St, but fortunately, there is brand new 6 PVC main from the
 hydrant to where the building is.

 The other irony is that this 6 is connected to a 12 main about 0.1
 miles away. A test on the 12 in 2006 had a static of 82 and a
 residual of 80 at a flow of 1400 gpm.

 I am going to the water department today to look at the system amps.
 Perhaps there is a weird piping configuration that creates this
 disparity. SSDP (P stands for project)

 Todd G. Williams, PE
 Fire Protection Design/Consulting
 Stonington, Connecticut
 www.fpdc.com
 860.535.2080
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RE: flow test conundrum

2008-10-29 Thread Todd Williams - FPDC
This discombobulates everyone, including the water department. The 
municipal water maps show nothing enlightening. The only way I can 
think these results could be obtained is if there is a problem with 
the gate valve where the Chase St main is tapped and hydrant P is 
actually tapped off the main in Chase St, after the valve. This 
hydrant is decades old and was probably installed before wet taps 
were available. They might have cut into the branch main because they 
would only have to shut down a small dead-end line instead of the one 
in Liberty St, which is a main feed. Only speculation at this point. 
They are installing a new hydrant at the end of the Chase St main on 
Saturday and when they get to flushing it, I am going to do a 
gradient, plus a couple of other checks. Right now, it is still in 
the idea and pondering phase.



At 01:14 PM 10/29/2008, you wrote:

Totally discombobulates me.  It'll be interesting to see what the city water
maps reveal.  Please keep us posted.

Ed Kramer
Littleton, CO

 -Original Message-
 From: [EMAIL PROTECTED] [mailto:sprinklerforum-
 [EMAIL PROTECTED] On Behalf Of Todd Williams - FPDC
 Sent: Wednesday, October 29, 2008 7:31 AM
 To: sprinklerforum@firesprinkler.org
 Subject: RE: flow test conundrum

 Ed, that is exactly what I was thinking. The residual pressure should
 be much higher on the second test. I read the gauges personally and
 verified the flows. Hydrant P ties into the 6 on Liberty St about 10
 ft from the connection to Chase. Given the difference between the
 2006 flow test abut 1/4 mile away on Liberty (12 main that connects
 to 6) and the Liberty St test last night, it seems to me that there
 may be a systemic problem, not just this connection.



 At 09:00 AM 10/29/2008, you wrote:
 Todd, it makes sense that F2 would flow something less than F1, but the
 huge
 difference in residuals blows me away.  The 2nd flow test should have
 given
 a residual closer to 78, not 26.  Something is definitely amiss.
 
 Did you personally read the static/residual gauge of both tests?
 Does hydrant P tie into the looped main on Liberty, or does it tie into
 the
 dead-end main on Chase?  If it ties into the dead-end main, there could
 be a
 major restriction somewhere between the point the 2 mains connect and
 the
 point where hydrant P connects.
 
 Ed Kramer
 Littleton, CO
 
   -Original Message-
   From: [EMAIL PROTECTED]
 [mailto:sprinklerforum-
   [EMAIL PROTECTED] On Behalf Of Todd Williams - FPDC
   Sent: Wednesday, October 29, 2008 4:20 AM
   To: sprinklerforum@firesprinkler.org
   Subject: flow test conundrum
  
   I did a couple of flow tests last night and the results, to me,
 don't
   make sense. There is a looped 6 main in Liberty St and a dead end
 6
   that branches off to Chase St. There is a hydrant at the
 intersection
   where we read pressures (P), a hydrant on Liberty that we flowed
 (F1)
   and one on Chase St that we also flowed (F2). For the first test, we
   flowed F1 and read the pressures at P. We got a static of 90 psi,
 and
   a residual of 72 psi at a flow of 470 gpm. On the second test, we
   flowed F2 and read the pressures again at P. Those results were a
   static of 90 psi and a residual of 26 psi at a flow of 380 gpm. The
   tests were done about 15 minutes apart. I am having a hard time
   reconciling these two tests. The water department foreman said that
   the 6 main in Chase St could be severely tuberculated, but offered
   no other options.  If that were the case, I would have thought that
   both the flow and pressure would have been dramatically different.
   Any thoughts? Of course the project in question is at the end of
   Chase St, but fortunately, there is brand new 6 PVC main from the
   hydrant to where the building is.
  
   The other irony is that this 6 is connected to a 12 main about 0.1
   miles away. A test on the 12 in 2006 had a static of 82 and a
   residual of 80 at a flow of 1400 gpm.
  
   I am going to the water department today to look at the system amps.
   Perhaps there is a weird piping configuration that creates this
   disparity. SSDP (P stands for project)
  
   Todd G. Williams, PE
   Fire Protection Design/Consulting
   Stonington, Connecticut
   www.fpdc.com
   860.535.2080
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 Todd G. Williams, PE
 Fire Protection

RE: flow test conundrum

2008-10-29 Thread Todd Williams - FPDC
I doubt if it is a leak. I would think the same thing would show up 
for both, but I will consider it. As I said in my last post, I am 
going to do a gradient when the new hydrant goes in and hopefully be 
able to isolate the problem. I did not gauge F2, but plan to as part 
of the next phase.



At 03:45 PM 10/29/2008, you wrote:

Still sounds like an obstruction.

I had two identical buildings, side by side within 100ft of each 
other, both on dry systems, govt jobs, had to do a trip test and 
flow at the inspector's test within 60 seconds of the valve 
tripping. One building was less than 40 seconds and the other over a 
minute and a half.  We went over everything from the installation to 
water flow tests on the mains, you name it.  Long story short we 
finally had to break the line at the flange at the floor and ran a 
line directly to the outside to see what the flow looked 
like.  Opened the PIV to the building and while expecting a torrent, 
we got a trickle.  The state guy brought one of those fiber optic 
scopes and fed it down the riser and found a conglomeration of 
debris at the base of the elbow.  My UG sub swore up and down he had 
flushed it and the GC signed off as witness.  Taught me not to take 
their word for it next time, if there was a next time.  Anyway, 
flushed the system, put it all back together and everything worked as planned.


Depending on how old the dead end leg is, there may be other issues 
that are causing the problem.  Did you put a gauge on the hydrant 
(F2) and see what the static was there?  If the static is less than 
at hydrant(P) then there could be leak in that line.  If the static 
is the same then obstruction comes up as first choice.





Craig L. Prahl, CET
Fire Protection Group
Mechanical Department
CH2MHILL
Lockwood Greene
1500 International Drive
PO Box 491, Spartanburg, SC  29304-0491
Direct - 864.599.4102
Fax - 864.599.8439
[EMAIL PROTECTED]
http://www.ch2m.com

-Original Message-
From: [EMAIL PROTECTED] 
[mailto:[EMAIL PROTECTED] On Behalf Of Todd 
Williams - FPDC

Sent: Wednesday, October 29, 2008 2:53 PM
To: sprinklerforum@firesprinkler.org
Subject: RE: flow test conundrum

This discombobulates everyone, including the water department. The 
municipal water maps show nothing enlightening. The only way I can 
think these results could be obtained is if there is a problem with 
the gate valve where the Chase St main is tapped and hydrant P is 
actually tapped off the main in Chase St, after the valve. This 
hydrant is decades old and was probably installed before wet taps 
were available. They might have cut into the branch main because 
they would only have to shut down a small dead-end line instead of 
the one in Liberty St, which is a main feed. Only speculation at this point.
They are installing a new hydrant at the end of the Chase St main on 
Saturday and when they get to flushing it, I am going to do a 
gradient, plus a couple of other checks. Right now, it is still in 
the idea and pondering phase.



At 01:14 PM 10/29/2008, you wrote:
Totally discombobulates me.  It'll be interesting to see what the city
water maps reveal.  Please keep us posted.

Ed Kramer
Littleton, CO

  -Original Message-
  From: [EMAIL PROTECTED]
  [mailto:sprinklerforum- [EMAIL PROTECTED] On Behalf Of Todd
  Williams - FPDC
  Sent: Wednesday, October 29, 2008 7:31 AM
  To: sprinklerforum@firesprinkler.org
  Subject: RE: flow test conundrum
 
  Ed, that is exactly what I was thinking. The residual pressure
  should be much higher on the second test. I read the gauges
  personally and verified the flows. Hydrant P ties into the 6 on
  Liberty St about 10 ft from the connection to Chase. Given the
  difference between the
  2006 flow test abut 1/4 mile away on Liberty (12 main that connects
  to 6) and the Liberty St test last night, it seems to me that there
  may be a systemic problem, not just this connection.
 
 
 
  At 09:00 AM 10/29/2008, you wrote:
  Todd, it makes sense that F2 would flow something less than F1, but
  the
  huge
  difference in residuals blows me away.  The 2nd flow test should
  have
  given
  a residual closer to 78, not 26.  Something is definitely amiss.
  
  Did you personally read the static/residual gauge of both tests?
  Does hydrant P tie into the looped main on Liberty, or does it tie
  into
  the
  dead-end main on Chase?  If it ties into the dead-end main, there
  could
  be a
  major restriction somewhere between the point the 2 mains connect
  and
  the
  point where hydrant P connects.
  
  Ed Kramer
  Littleton, CO
  
-Original Message-
From: [EMAIL PROTECTED]
  [mailto:sprinklerforum-
[EMAIL PROTECTED] On Behalf Of Todd Williams - FPDC
Sent: Wednesday, October 29, 2008 4:20 AM
To: sprinklerforum@firesprinkler.org
Subject: flow test conundrum
   
I did a couple of flow tests last night and the results, to me,
  don't
make sense. There is a looped 6 main in Liberty St and a dead

Re: Mezz design area

2008-10-29 Thread Todd Williams - FPDC
I would tend to go with the 1500 sqft, unless there is a draft stop 
around the opening. The hole in the first floor issue is sort of 
dealt with the escalator and water curtain section. Now what about a 
room with ceiling clouds. The deck or the bottom of the clouds? How 
much area has to be covered for one to take precedent over the other?




At 04:34 PM 10/29/2008, you wrote:

I think we've talked about this before but couldn't come up with anything in
the archives.



Roof elv. just over 20'.  All quick response heads.



50' x 50' mezzanine in a corner so that one 50' side is open to above.  This
situation also comes when you have a hole in a first floor open to the
second.



At the roof the design area is 1500 but what about under the mezz?



I tend to lean to a full 1500 sq.ft. under the mezz. but that's just
conservatism and I don't think it's really supported in code either way.
Even if the wall is around all 4 sides you might have a stair opening
wrecking the reduced remote area if that's otherwise allowed.



What about a two story 1,000,000 sq.ft. building with a 33.34' x 30' stair
opening in the middle?  I can see doing by the opening 1500 sq.ft. but what
is by the opening mean.  How far away until you are no longer near.



Chris Cahill, P.E.

Fire Protection Engineer

Sentry Fire Protection, Inc.



763-658-4483

763-658-4921 fax



Email: [EMAIL PROTECTED]



Mail: P.O. Box 69

Waverly, MN 55390



Location: 4439 Hwy 12 SW

  Waverly, MN 55390



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RE: Pitot Chart

2008-10-26 Thread Todd Williams - FPDC

...And teach you the ways of NFPA, I shall.


At 07:05 PM 10/26/2008, you wrote:

Remember the second Star Wars movie, when Luke tells Yoda that he's not
afraid?  And Yoda says, You will be.  You WILL be.

Same thing, but the green midget doesn't come out until 1:36 in the AM.

Steve Leyton
Protection Design  Consulting
San Diego, CA


-Original Message-
From: [EMAIL PROTECTED]
[mailto:[EMAIL PROTECTED] On Behalf Of Todd
Williams - FPDC
Sent: Friday, October 24, 2008 2:17 PM
To: sprinklerforum@firesprinkler.org
Subject: Re: Pitot Chart

This George's Room thing is starting to scare me.


At 04:25 PM 10/24/2008, you wrote:
Thank You, one and all! Got what I needed. Sure
do enjoy monitoring  this site and I pick up
goodies all the time. I will make an effort to
do San Diego next year, mainly to find out what happens at George's
Room.




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Re: Occupancy hazard for labour accomodation

2008-10-25 Thread Todd Williams - FPDC

Sam,

Welcome aboard. By 'labour accommodations', I assume you mean living 
quarters for workers. If so, then the occupancy would be Residential 
and would need to be protected by either NFPA 13R or NFPA 13 Light 
Hazard, depending on the arrangement of the building, local codes, 
etc. This, of course, is under the assumption that Dubai is using the 
NFPA standards.



At 03:34 AM 10/25/2008, you wrote:

Hi everyone.

am a new kid on the block.

a beginner to Fire protection Engineering and am working in Dubai.
Found this forum as a very informative one

I have a doubt regarding the occupancy hazard classification needed for
labour accomodation.
Labour accomodation is in portable cabins and is a G+1 Construction.



Please give your valuable advice.

sam
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Re: Pitot Chart

2008-10-24 Thread Todd Williams - FPDC

This George's Room thing is starting to scare me.


At 04:25 PM 10/24/2008, you wrote:
Thank You, one and all! Got what I needed. Sure 
do enjoy monitoring  this site and I pick up 
goodies all the time. I will make an effort to 
do San Diego next year, mainly to find out what happens at George's Room.


- Original Message - From: George Church [EMAIL PROTECTED]
To: sprinklerforum@firesprinkler.org
Sent: Friday, October 24, 2008 1:09 PM
Subject: RE: Pitot Chart


From Denise at hydro flow:

Here are the pitot formula and coefficients for all sizes of the Hose
Monsters and Nozzle Inserts.

Q = 29.83 * ¡îP * D2 * Coefficient
Where Q = flow rate in GPM, P = pitot pressure, D = nozzle diameter

Product Coefficient
Nozzle Insert 1 1/8¡± 0.99
Nozzle Insert 1 ¨ú¡± 0.975
Hose Monster 2 ¨ö¡± 0.906

The 4¡± and 4 ¨ö¡± Hose Monsters actually use a different formula
because they are not using a pitot, but these numbers work for the above
pitot formula.
Product Coefficient
Hose Monster 4¡± 0.71159
Hose Monster 4 ¨ö¡± 0.54816

The Pitotless Nozzles are different also.

Links to flow charts for low, normal and high pressures:
http://www.hosemonster.com/downloads/FCHM2H.pdf
http://www.hosemonster.com/downloads/FCHM2HLP.pdf
http://www.hosemonster.com/downloads/FCHM2HHP.pdf
* * * *
Obviously, the chart is pretty darn convenient when you're in the field;
rather than use a calculator when I've gone out without the chart, I just
use my cel to call the office and ask someone for the GPM for my pitot
pressure.

Saw the pitotless nozzles last week at AFSA- pretty neat. They've come a
long way!

TGIF
glc

-Original Message-
From: [EMAIL PROTECTED] [mailto:sprinklerforum-
[EMAIL PROTECTED] On Behalf Of Todd Williams - FPDC
Sent: Friday, October 24, 2008 2:35 PM
To: sprinklerforum@firesprinkler.org
Subject: Re: Pitot Chart

Dennis,

Why would the pitot have a chart? Is this actually a diffuser or
nozzle with a built-in pitot?

What I did with my Hose Monster was to use the chart and calc
backwards to come up with the K factor, then I wrote it on the HM
with a permanent marker. That way, if I lose the chart, oh well.


At 02:10 PM 10/24/2008, you wrote:

I have a Sierra  brand Pitot I bought circa 1990 and my Fitter
lost the chart yesterday while doing a flow test. I think it is the
very similar to the one listed in the Potter Roemer catalogue. I was
hoping someone could email or fax me a copy? Hate to buy a new one
over the chart. Thanks in advance.
Fax 541 245 0498
Phone245 0466



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www.fpdc.com
860.535.2080  
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Re: Fire Sprinkler Pipe through Mechanical Duct

2008-10-23 Thread Todd Williams - FPDC
Seen it done before, although it is the last alternative. Everybody 
should sign off on it, though. It may require some re-configuring by 
the HVAC engineer.



At 12:43 PM 10/23/2008, you wrote:

After review of NFPA 13, I cannot find a section that prohibits fire
sprinkler pipe from passing through mechanical duct.  Does anyone know of
something in the Mechanical Code that would prohibit steel fire sprinkler
pipe from passing through mechanical ductwork?  Case in point, 2 1/2 fire
sprinkler line passing through a +/-60 square duct.  Mechanical contractor
would seal the penetrations.

Thanks,
Gregg Fontes
Cen-Cal Fire Systems, Inc.
(209)334-9119


This email was scanned by DG Technology Group Secure Scan and found to
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RE: sizing expansion tanks

2008-10-22 Thread Todd Williams - FPDC
Unfortunately, not all of us can afford the luxury of time off to go 
to conventions (let alone the extra $$). So we just glean what we can 
from here and move forward.




At 04:46 PM 10/22/2008, you wrote:

Travis, nNice mention of being an AFSA member. I don't recall if I did my
annual pre-convention plug for membership, so Steve has at least one good
thought when he sees me.

Those that didn't go to Convention missed another great opportunity for
education that pays dividends, camaraderie, networking, the big trade show
full of new and current products you may be using or should be using, and
seminars. Note the seminars and the education that pays dividends are
separate since you can learn more talking to people and sharing experiences
than in the seminars.

As the late, great Bob McCullough said when asked if he had a lot of
competition in the sprinkler business, he replied I have a lot of friends
in the sprinkler business. One trip to a convention and you'll see and meet
many of the finest people in the industry.

Frankly, I cannot believe people wrestle with the decision- it should be a
no-brainer. There will be a Sprinkler Forum reception in San Diego next
year, and I understand the hotel should have a system with a pretty decent
design- by one of our own here on the Forum. San Diego is a great place to
visit, too.

KUDOS to the AFSA staff for pulling off another one they should be proud
of!!!
Thanks to all
George Church
Rowe Sprinkler

-Original Message-
From: [EMAIL PROTECTED]
[mailto:[EMAIL PROTECTED] On Behalf Of Travis Mack,
SET
Sent: Wednesday, October 22, 2008 3:32 PM
To: sprinklerforum@firesprinkler.org
Subject: RE: sizing expansion tanks

Thanks to everyone who replied.  I have received several spreadsheets that
provide the answer.  You guys are awesome!  This forum alone makes the AFSA
membership fee worth every penny and then some.

Travis


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RE: sizing expansion tanks

2008-10-22 Thread Todd Williams - FPDC
Being a one-man-band does not give a lot of opportunity to get away. 
There is no one to cover. The last 3 days I had off was 
Intermediate Autosprink class and I had to put in 5-6 hours design 
time outside of class each day so I wouldn't get projects pulled. I 
can't imagine doing a convention on a schedule like that. Fortunately 
the New England Chapter of SFPE has a couple of good one day seminars 
that I can usually get to without creating too many problems.




At 06:00 PM 10/22/2008, you wrote:

A Penny wise and Pound foolish Attitude. You Can NOT afford to miss the
training, and learning experiences offered! We make the time, and recognize
the rewards thru the year for the time spent. Time management is as
important a tool as AutoCAD. Learn to schedule 3 days to attend, and you'll
never know how you justified missing the opportunity before.

Thom McMahon, SET
Firetech, Inc.
2560 Copper Ridge Dr
P.O. Box 882136
Steamboat Springs, CO 80488
Tel:  970-879-7952
Fax: 970-879-7926


-Original Message-
From: [EMAIL PROTECTED]
[mailto:[EMAIL PROTECTED] On Behalf Of Todd Williams
- FPDC
Sent: Wednesday, October 22, 2008 3:42 PM
To: sprinklerforum@firesprinkler.org
Subject: RE: sizing expansion tanks

Unfortunately, not all of us can afford the luxury of time off to go
to conventions (let alone the extra $$). So we just glean what we can
from here and move forward.


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suction tank and geothermal heat source

2008-10-20 Thread Todd Williams - FPDC
I am working on a project for an addition to a local church where 
they are required to install sprinklers. There is no public water, so 
a pump and tank will be required. Their latest idea is to install a 
cistern underneath the addition and use a vertical turbine pump. They 
would also like to use the water in the cistern as a heat source for 
a geothermal heating system. Has anyone run into this yet? I'm not 
sure of the exact configuration and I have my questions (direct pump 
vs. coils with transfer fluid), but I would appreciate any thought 
from the gallery.


Todd G. Williams, PE
Fire Protection Design/Consulting
Stonington, Connecticut
www.fpdc.com
860.535.2080  
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Re: Retro-fit with Backflow Device

2008-10-20 Thread Todd Williams - FPDC

Tim,

I have used the 11.2.2 method in the past, but tend to be very 
conservative with it. Hydraulic calculation is an option as well; 
just be aware of what you might find. And yes, the BFP should be 
sized accordingly.



At 02:58 PM 10/20/2008, you wrote:

What does the forum say about retrofitting a pipe scheduled system with a
backflow device? Do we have to use the water supply demand of the NFPA 13
11.2.2.1 (2002 Edition) or calculate various areas to determine the most
remote area (no plans available)?

If the NFPA 13; 11.2.2.1 is used, does the backflow device HAVE to be sized
accordingly?

I have my own ideas but want the input from the forum please.


Timothy W Goins
A  T Services

For I am not ashamed of the gospel of Christ: for it is the power of God
unto salvation to everyone that believeth;. KJV Romans 1:16

Reply to   mailto:[EMAIL PROTECTED] mailto:[EMAIL PROTECTED]


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Re: What does Rated Fire Flow mean to you

2008-10-20 Thread Todd Williams - FPDC
Do the tanks supply hydrants off the pump? If yes, available flow at 
20 psi. If not, then that question has no value.




At 04:51 PM 10/20/2008, you wrote:

We have been asked to supply the rated fire flow on a project I am
involved with.  Based on what I can determine when I google this term, this
is usually the flow at 20 psi.  If I have a tank(s) in the
building supplying the fire protection requirements, do I have this flow
value?

Thanks to anyone that can clear up my confusion.
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Re: Firematic Model D

2008-10-17 Thread Todd Williams - FPDC
I have one, but it is dated 1994. If that would help. let me know and 
I'll fax it over.



At 08:16 AM 10/17/2008, you wrote:
Anyone out there have product cut sheets for a Firematic Model D 4 
Dry pipe valve (1980).


 Daniel L. Merkle, CET
NICET # 118915
Automatic Sprinkler System Layout, Level III
COLONIAL Fire Protection Systems Inc.
937 Linden Ave. W.
E. Rochester, N.Y. 14445
Office-(585) 381-7362
Fax-(585) 381-8263
E-mail - [EMAIL PROTECTED]


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Re: Over-kill? A true situation

2008-10-16 Thread Todd Williams - FPDC
I'll go out on the limb; it does seem like 
overkill. We all know the benefits of sprinklers, 
but economics has to come in at some point. A
blanket regulation without regards to occupancy, 
exposure or other factors, to me, is, well, 
overkill.. Section 903 of the ICC gives guidance 
where sprinkler are required and it is based on 
occupancy classification. I believe that with the 
exception of Group H and I, that the minimum is 
between 5000 sqft and 12000 sqft. That seems like 
a realistic approach, although you could argue 
with the area sizes may need to be looked at, 
given the increase in values since they were 
established, but a blanket 750 seems unreasonable.


I applaud the owner for actually building it and 
Redondo Beach should consider themselves lucky he 
built there. In this part of the world, that 
could be a deal breaker. You sell the land and 
build in the another town where regulations are 
more in line with the Code models.



At 05:07 PM 10/15/2008, you wrote:

Redondo Beach has a sprinkler and standpipe ordinance. 1) Any new
construction greater than 750 square feet is required to have fire
sprinklers installed. 2) If any portion of a (new) building cannot be
reached with 150’ of hose stretched from a fire engine parked on a
public way, fire standpipes shall be installed.

A business owner opened a garden center on a 40’ x 200’ lot.  A
sales/display building sits with the rear of the building 180’ from the
public way. The building is single story, 1100 sqft. The business owner
was required to put in a full blown 13 system with a single 2 ½”
standpipe half way down the lot. That means a 4” supply with a DCVA and
a 2 x 2 ½” FDC . The owner had to trench across the street to reach the
main ($30,000.00).

All said and done, $ 62,000.00 to protect a 1100 sqft., single story
garden center. Is that an AHJ run-a-muck or am I crazy for thinking so?
I would love to hear what you folks have to say.

BTW, the standpipe ordinance was written in 1991 when the fire trucks
carried 150' of preconnect, quick attack hose. In 2001 the fire trucks
were reconfigured with 200' and 300' preconnect hoses.

Owen Evans
Gone from the RBFD plan check office for 6 years.
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www.fpdc.com
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Re: Pesticides Storage

2008-10-16 Thread Todd Williams - FPDC

Ray, Get MSDS's on the stuff and see exactly what you are dealing with.



At 11:29 AM 10/16/2008, you wrote:

Esteemed Collegues:

Can anyone give guidance on a Pesticides Storage warehouse and the 
approriate fire protection requirements?
NFPA-434 doesn't give prescriptove requiremetns or a definitive path 
to follow. It only indicates a risk analysis be done by a competent 
individual (I read PE or FPE) to determine the extent and type of 
fire protection to be provide.


Without regard to storage arrangement and heights, what TYPE of 
commodity would be appropriate to consider, since the amount stored 
is over 10,000 lbs and is extermely varied in the types and 
configurations of products to be stored?
I am leaning towards NFPA-30 Flammable and Combustible Liquids to 
begin my analysis, but would like the opinions of anyone who has had 
experience with this process.


Thanks in advance,

Ray Vance -SET
Chief Sales Designer
Wayne Automatic Fire Sprinklers, Inc.
www.waynefire.comblocked::blocked::http://www.waynefire.com/
(407) 877-5563  office
(321) 436-2184  cell

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Placard fact check

2008-10-15 Thread Todd Williams - FPDC

This weeks crisis, so far...

I am working on a plant in MA where they need to add in rack 
sprinklers. The existing ceiling system is a pipe schedule and the 
placard at the riser says it can deliver .45/2500 at a flow of 1220 
gpm at 52 psi. It seemed light, but I don't jump 'til I crunch the 
numbers. In actuality, it requires 1558 gpm at 286 psi at the supply. 
Everybody, including the HPR carrier, has bought into the numbers on 
the riser. Now the excrement is about to impact the vortex generator.


Moral of the story; don't believe everything you read.

Todd G. Williams, PE
Fire Protection Design/Consulting
Stonington, Connecticut
www.fpdc.com
860.535.2080  
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RE: Placard fact check

2008-10-15 Thread Todd Williams - FPDC
This section of the building was built in the 1950s and was all pipe 
schedule. At some point, some one allegedly did hydraulics (due to 
the rack storage) and this is where the placard came from. There have 
been at least 5 owners that I am aware of. When and how this was done 
is beyond me. As far a due diligence, the last time I saw an FM 
Global guy on a job, he was training someone new in hydraulics. His 
line was Ignore the riser nipples, they don't have any impact. Just 
include the elevation. I doubt if many insurance companies actually 
do hydraulics before they write a risk; they just look at the placards.




At 11:25 AM 10/15/2008, you wrote:

I wonder what the inspectors were doing when they reviewed the info on
the hydraulic placard simple math and some common sense would have
indicated that something was wrong.  The density 0.45 gpm per sq. ft.
times the area of operation 2,500 sq. ft. times 1.3 (30% increase for
hydraulic inefficiency of tree system) indicates a flow requirement of
1,462.5  rounded up to 1,465 gpm for the system. It appears that the
hydraulic placard was based on the design density multiplied by area of
operation plus 100 gpm.

What happened to the HPR carriers plan review of the shop drawings and
hydraulic calculation or due diligence when taking over the account from
another carrier.

I hope that the sprinkler contractor doing the annual inspection is
following NFPA 25 to the letter and not using any modified version of
the NFPA 25 inspection form.

Just goes to show that you must verify all info given to you.


Jim Davidson

Davidson Associates
302-994-9500
-Original Message-
From: [EMAIL PROTECTED]
[mailto:[EMAIL PROTECTED] On Behalf Of Todd
Williams - FPDC
Sent: Wednesday, October 15, 2008 10:15 AM
To: sprinklerforum@firesprinkler.org
Subject: Placard fact check

This weeks crisis, so far...

I am working on a plant in MA where they need to add in rack
sprinklers. The existing ceiling system is a pipe schedule and the
placard at the riser says it can deliver .45/2500 at a flow of 1220
gpm at 52 psi. It seemed light, but I don't jump 'til I crunch the
numbers. In actuality, it requires 1558 gpm at 286 psi at the supply.
Everybody, including the HPR carrier, has bought into the numbers on
the riser. Now the excrement is about to impact the vortex generator.

Moral of the story; don't believe everything you read.

Todd G. Williams, PE
Fire Protection Design/Consulting
Stonington, Connecticut
www.fpdc.com
860.535.2080
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RE: Bio-Diesel

2008-10-06 Thread Todd Williams - FPDC
Containers can also be large (5000 gallons not uncommon) so be aware 
of that as well. This would probably fall under a Group H in the 
Building Code, so take a look at those requirements as well. There is 
someone on the Forum from the Jacksonville area (name escapes me 
right now) who has done this before and gave me some great answers 
when I asked a similar question. Hopefully he'll pipe in, but the 
responses so far have been on target.




At 04:38 PM 10/6/2008, you wrote:
Bio-diesel itself is considered a Class IIIB Combustible.  Flash 
point is higher than standard diesel, usually around 240-250F.


Check with your client and get a list of ALL the chemicals that will 
be used in the process and for support and maintenance.  Usually the 
other two components are Methanol and Sodium Hydroxide (caustic).


There are some blends which use different additives so getting the 
whole list is critical.  Plus they will often times have solvents 
and other potentially flammable substances on hand for service and 
cleaning of equipment.


Since it's a hydrocarbon, it is not water miscible.  Foam-water is 
the best choice but standard water based sprinklers are accepted by 
most AHJ's.  That is another place to start.  Contact the local AHJ 
or fire department to see if there are any local restrictions or 
guidelines for these types of installations.


You'll start with NFPA 30 and most likely end up in NFPA 16.

If this is an amateur setup I'd walk away, if it is a legitimate 
business, tread with caution and do a lot of research.



Craig L. Prahl, CET
Fire Protection Group
Mechanical Department
CH2MHILL
Lockwood Greene
1500 International Drive
PO Box 491, Spartanburg, SC  29304-0491
Direct - 864.599.4102
Fax - 864.599.8439
[EMAIL PROTECTED]
http://www.ch2m.com

-Original Message-
From: [EMAIL PROTECTED] 
[mailto:[EMAIL PROTECTED] On Behalf Of Charles Thurston

Sent: Monday, October 06, 2008 3:54 PM
To: sprinklerforum
Subject: Bio-Diesel

Hello sprinklerforum,

  I know I am not the first to be ask to protect a space that will be
  storing Bio-Diesel and the products to produce it. What hazard should it
  be? I was ask if I could find out as nobody else involved had a clue

  Thank You

--
Best regards,
 Charles Thurston  mailto:[EMAIL PROTECTED]
  Coastal Fire Protection

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Stonington, Connecticut
www.fpdc.com
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RE: Bio-Diesel

2008-10-06 Thread Todd Williams - FPDC
I was thinking more about 5K of Methanol than the Bio-diesel itself. 
I think that would put it in an H-3.


At 05:09 PM 10/6/2008, you wrote:
It would only be an H occupancy if it exceeded 13,200 gallons of 
storage or in use, closed systems for unsprinkled, IIIB.  Double 
that if you have sprinklers.



Craig L. Prahl, CET
Fire Protection Group
Mechanical Department
CH2MHILL
Lockwood Greene
1500 International Drive
PO Box 491, Spartanburg, SC  29304-0491
Direct - 864.599.4102
Fax - 864.599.8439
[EMAIL PROTECTED]
http://www.ch2m.com

-Original Message-
From: [EMAIL PROTECTED] 
[mailto:[EMAIL PROTECTED] On Behalf Of Todd 
Williams - FPDC

Sent: Monday, October 06, 2008 5:02 PM
To: sprinklerforum@firesprinkler.org
Subject: RE: Bio-Diesel

Containers can also be large (5000 gallons not uncommon) so be aware 
of that as well. This would probably fall under a Group H in the 
Building Code, so take a look at those requirements as well. There 
is someone on the Forum from the Jacksonville area (name escapes me 
right now) who has done this before and gave me some great answers 
when I asked a similar question. Hopefully he'll pipe in, but the 
responses so far have been on target.




At 04:38 PM 10/6/2008, you wrote:
Bio-diesel itself is considered a Class IIIB Combustible.  Flash point
is higher than standard diesel, usually around 240-250F.

Check with your client and get a list of ALL the chemicals that will be
used in the process and for support and maintenance.  Usually the other
two components are Methanol and Sodium Hydroxide (caustic).

There are some blends which use different additives so getting the
whole list is critical.  Plus they will often times have solvents and
other potentially flammable substances on hand for service and cleaning
of equipment.

Since it's a hydrocarbon, it is not water miscible.  Foam-water is the
best choice but standard water based sprinklers are accepted by most
AHJ's.  That is another place to start.  Contact the local AHJ or fire
department to see if there are any local restrictions or guidelines for
these types of installations.

You'll start with NFPA 30 and most likely end up in NFPA 16.

If this is an amateur setup I'd walk away, if it is a legitimate
business, tread with caution and do a lot of research.


Craig L. Prahl, CET
Fire Protection Group
Mechanical Department
CH2MHILL
Lockwood Greene
1500 International Drive
PO Box 491, Spartanburg, SC  29304-0491 Direct - 864.599.4102 Fax -
864.599.8439 [EMAIL PROTECTED] http://www.ch2m.com

-Original Message-
From: [EMAIL PROTECTED]
[mailto:[EMAIL PROTECTED] On Behalf Of Charles
Thurston
Sent: Monday, October 06, 2008 3:54 PM
To: sprinklerforum
Subject: Bio-Diesel

Hello sprinklerforum,

   I know I am not the first to be ask to protect a space that will be
   storing Bio-Diesel and the products to produce it. What hazard should it
   be? I was ask if I could find out as nobody else involved had a clue

   Thank You

--
Best regards,
  Charles Thurston  mailto:[EMAIL PROTECTED]
   Coastal Fire Protection

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www.fpdc.com
860.535.2080
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limited combustible concealed space

2008-10-04 Thread Todd Williams - FPDC
An attic space is non-combustible, except for 2x6 joists and plywood 
sheathing for the roof. The joist spaces are going to be filled with 
batt insulation and the only exposed combustibles are the edge of the 
joists. Does this fit the definition of a limited combustible 
concealed space as stated in NFPA 13 (2002) 8.14.1.2?


Todd G. Williams, PE
Fire Protection Design/Consulting
Stonington, Connecticut
www.fpdc.com
860.535.2080  
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shallow pitched roof.

2008-10-02 Thread Todd Williams - FPDC
NFPA 13 (2002) Table 8.6.2.2.1(a)  details sprinkler spacing and 
areas for unoccupied attics, wood joist construction, member less 
than 3 ft o.c., pitch 4:12 or greater. The spacing and pressure 
requirements are very specific. If you are working with a building 
with all of the above except 3:12 pitch, would the design be based on 
just the combustible construction with members less than 3 ft. o.c.? 
Seems like a pretty dramatic change in design for minimal change in slope.


Todd G. Williams, PE
Fire Protection Design/Consulting
Stonington, Connecticut
www.fpdc.com
860.535.2080  
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RE: Protection below steel grating

2008-10-02 Thread Todd Williams - FPDC

From dirt we come and to dirt we shall return?


At 06:20 PM 10/2/2008, you wrote:

All this time to discover it's people that turn to dirt, not water?

Thom McMahon, SET
Firetech, Inc.



Aristotle postulated that water turned to dirt
 Craig L. Prahl, CET

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overhang concealed space

2008-10-01 Thread Todd Williams - FPDC
I am working on a project on a wood frame building which has a 3' 
wide overhang around the perimeter. The framing is likewise wood, the 
space between the joists is greater than 6 and the space is 
separated from the main building by 2x4 blocking. My claim is that is 
is a combustible concealed space and requires protection and the 
architect's claim is that it is an overhang less than 4 ft, so 
sprinklers are not required. I said that is for below the overhang 
only, but he disagrees. I should be able to argue this successfully 
but I've been working too many 12 hour days and weekends so I'm a 
little cooked at the moment. Am I on target?


This is a child care occupancy. The building permit was issued on 8/8 
and they have to turn over the building on 11/5. I got the design 
contract 5 days ago. There is no time to get a big argument going, so 
this needs to be solved fast. Thoughts?


Todd G. Williams, PE
Fire Protection Design/Consulting
Stonington, Connecticut
www.fpdc.com
860.535.2080  
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Re: overhang concealed space

2008-10-01 Thread Todd Williams - FPDC
Let's see. The building permit was issued on 8/8, the sprinkler 
contract was given out on 9/18 and the building has to be turned over 
on 11/5. At what point is there time for and RFI? (I may put it in 
that format anyway)





At 03:02 PM 10/1/2008, you wrote:

Todd,

For what it's worth I agree with you also. Too bad you have that PE. A
moron like myself could easily write a short disclaimer stating my
objection to the architect's interpretation, citing chapter and verse
of course, file a copy with everyone involved and their mothers, ask
the architect for written direction through an RFI, do what he wants
and then bill him for the revised plans required after his idea is
rejected by the local John Drucker.

On Wed, Oct 1, 2008 at 11:50 AM, Ray Vance [EMAIL PROTECTED] wrote:
 Todd,

 In my opinion, you are correct in that you are actually 
addressing two very specific issues:


 (1) The combustible concealed space created by the framing of the overhang
 (2) The use of the space BENEATH the combustible overhang

 Each of the scenarios needs to be addressed separately and again 
I am in agreement with you.


 The combustible concealed space created by the framing needs to 
be protected in accordance with ONE of the allowable protection 
schemes per NFPA-13, most likely either sprinklered or filled with 
nocombustible insulation. The space beneath the overhang should not 
be required to have sprinkler protection since it is less than 4ft 
wide and I am presuming no combustibles are stored or handled beneath it.


 Ray Vance - SET
 Chief Engineering Tech.
 Wayne Automatic Fire Sprinklers, Inc.
 www.waynefire.com
 (407) 877-5563   office
 (321) 436-2184   cell


 -Original Message-
 From: [EMAIL PROTECTED] 
[mailto:[EMAIL PROTECTED] On Behalf Of Todd 
Williams - FPDC

 Sent: 2008-10-01 14:12
 To: sprinklerforum@firesprinkler.org
 Subject: overhang concealed space

 I am working on a project on a wood frame building which has a 3'
 wide overhang around the perimeter. The framing is likewise wood, 
the space between the joists is greater than 6 and the space is 
separated from the main building by 2x4 blocking. My claim is that 
is is a combustible concealed space and requires protection and the 
architect's claim is that it is an overhang less than 4 ft, so 
sprinklers are not required. I said that is for below the overhang 
only, but he disagrees. I should be able to argue this successfully 
but I've been working too many 12 hour days and weekends so I'm a 
little cooked at the moment. Am I on target?


 This is a child care occupancy. The building permit was issued on 
8/8 and they have to turn over the building on 11/5. I got the 
design contract 5 days ago. There is no time to get a big argument 
going, so this needs to be solved fast. Thoughts?


 Todd G. Williams, PE
 Fire Protection Design/Consulting
 Stonington, Connecticut
 www.fpdc.com
 860.535.2080
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--
Ron Greenman
at home
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Todd G. Williams, PE
Fire Protection Design/Consulting
Stonington, Connecticut
www.fpdc.com
860.535.2080  
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RE: overhang concealed space

2008-10-01 Thread Todd Williams - FPDC

Reed,

I must have missed that, although there was a 2 week period around 
then when I got nothing from the Forum. Most of the space is blocked 
off from the open attic with 2x4 or 2x6 blocking. There are some 
openings and they do make some vent channels (The name escapes me, 
but they were recently used in an attic that was filled with 
insulation on a project in MA.) that might help.We'll see what the 
RFI results in.


Todd


At 04:36 PM 10/1/2008, you wrote:

Todd,

I had the same argument with an architect a few weeks ago and I 
posted the question to the forum (Subject: combustible overhang 
8-18-08)  to see how this is typically handled.  I didn't get any 
responses.  Typically, the space can't be filled with insulation 
because it needs to remain open for venting the attic.  Therefore, 
it seems to me that 13 is clear that the space shall be protected by 
sprinklers (8.15.1).


So forum, is this scenario typically ignored and the combustible 
concealed space created above the overhang go unprotected?


I'm quite sure that you are on target with your argument Todd, but I 
would like to know how to best protect this area for future reference.


Reed A. Roisum, CET
Fire Protection Technician

Ulteig Engineers, Inc.
3350 38th Avenue South
Fargo, ND 58104-7079

Direct Number: 701.280.8580
Mobile: 701.212.8810
Main Office: 701.280.8500

-Original Message-
From: [EMAIL PROTECTED] 
[mailto:[EMAIL PROTECTED] On Behalf Of Todd 
Williams - FPDC

Sent: Wednesday, October 01, 2008 1:12 PM
To: sprinklerforum@firesprinkler.org
Subject: overhang concealed space

I am working on a project on a wood frame building which has a 3'
wide overhang around the perimeter. The framing is likewise wood, the
space between the joists is greater than 6 and the space is
separated from the main building by 2x4 blocking. My claim is that is
is a combustible concealed space and requires protection and the
architect's claim is that it is an overhang less than 4 ft, so
sprinklers are not required. I said that is for below the overhang
only, but he disagrees. I should be able to argue this successfully
but I've been working too many 12 hour days and weekends so I'm a
little cooked at the moment. Am I on target?

This is a child care occupancy. The building permit was issued on 8/8
and they have to turn over the building on 11/5. I got the design
contract 5 days ago. There is no time to get a big argument going, so
this needs to be solved fast. Thoughts?

Todd G. Williams, PE
Fire Protection Design/Consulting
Stonington, Connecticut
www.fpdc.com
860.535.2080
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Todd G. Williams, PE
Fire Protection Design/Consulting
Stonington, Connecticut
www.fpdc.com
860.535.2080  
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RE: Alternate to pitch?

2008-09-30 Thread Todd Williams - FPDC
There are other issues that are being addressed as part of this 
project. Engineering, internal investigations, pendent sprinklers, 
alarms, etc are all on the table as well. The cost to heat this place 
is over $1 million per season.



At 02:25 PM 9/30/2008, you wrote:
If you modify the system in regards to pipe pitch are you obligated 
to bring the system up to current code standards?


There seem to be several critical issues with the system that makes 
pipe pitch seem like the least of the concerns.  Actual 
functionality would seem to be the first and foremost concern.


Has anyone performed a cost comparison to do the necessary 
modifications to change this to dry (the right way) versus 
maintaining the building temp at 40F?


Have they shut off all plumbing and other potable supplies?

Any fire alarm panels, smoke detectors?  They don't operate or 
operate properly below certain temperatures either.  Might need to 
check with the mfgrs on that as well.





Craig L. Prahl, CET
Fire Protection Group
Mechanical Department
CH2MHILL
Lockwood Greene
1500 International Drive
PO Box 491, Spartanburg, SC  29304-0491
Direct - 864.599.4102
Fax - 864.599.8439
[EMAIL PROTECTED]
http://www.ch2m.com


On Sep 30, 2008, at 4:49 AM, Todd Williams - FPDC wrote:

 The existing systems are all OH pipe schedule (with 3/4 pipe) and the
 vacant building would be LH. The other consideration is that they
 currently have two 1500 gpm pumps taking suction from a pond and part
 of the program would be to connect it to the public supply.
 Hydraulics and other factors would be taken into consideration, but
 the pitch issue is the most complicated. Besides, with 1,500,000 sqsft
 of pipe network, we'd have to bring in anti-freeze in tank cars


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Todd G. Williams, PE
Fire Protection Design/Consulting
Stonington, Connecticut
www.fpdc.com
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RE: Alternate to pitch?

2008-09-30 Thread Todd Williams - FPDC
The existing systems are all OH pipe schedule (with 3/4 pipe) and 
the vacant building would be LH. The other consideration is that they 
currently have two 1500 gpm pumps taking suction from a pond and part 
of the program would be to connect it to the public supply. 
Hydraulics and other factors would be taken into consideration, but 
the pitch issue is the most complicated. Besides, with 1,500,000 
sqsft of pipe network, we'd have to bring in anti-freeze in tank cars




At 07:29 AM 9/30/2008, you wrote:

When converting systems from wet to dry don't we also have to consider the
hydraulics ?.

Is it acceptable to simply convert them to antifreeze and retain the wet
performance ?

John Drucker
Fire Protection Subcode Official (AHJ)
New Jersey

-Original Message-
From: [EMAIL PROTECTED]
[mailto:[EMAIL PROTECTED] On Behalf Of Dewayne
Martinez
Sent: Tuesday, September 30, 2008 7:20 AM
To: sprinklerforum@firesprinkler.org
Subject: RE: Alternate to pitch?

What about pitching the lines and then heat tracing the mains and aux
drains per 8.16.4.1.3 (13 02ed)?
I don't think this is the best option but you were looking for
alternative ideas.
Dewayne

-Original Message-
From: [EMAIL PROTECTED]
[mailto:[EMAIL PROTECTED] On Behalf Of Todd
Williams - FPDC
Sent: Monday, September 29, 2008 4:00 PM
To: sprinklerforum@firesprinkler.org
Subject: Alternate to pitch?

I visited a site the other day which consisted on 1.5 million sqft of
vacant industrial buildings built in the 1950's. The cost to heat these
building is astronomical and the owners are looking for cut costs. They
would like to convert the 30 +/- systems from wet to dry.
Obviously the biggest obstacle is pipe pitch. Some of the lines appear
to pitch, but most lines and mains are flat (caveat: I have not gone in
with a level to check it, but rod lengths looked the same). The lines
look like they could be pitched, but the mains would be a challenge. Are
there any alternatives out there? I don't know of any, but I didn't know
if the collective mind had run across anything.

Todd G. Williams, PE
Fire Protection Design/Consulting
Stonington, Connecticut
www.fpdc.com
860.535.2080
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Todd G. Williams, PE
Fire Protection Design/Consulting
Stonington, Connecticut
www.fpdc.com
860.535.2080  
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RE: Alternate to pitch?

2008-09-30 Thread Todd Williams - FPDC

What isn't?


At 08:13 AM 9/30/2008, you wrote:

It's $1.29/share

-Original Message-
From: [EMAIL PROTECTED]
[mailto:[EMAIL PROTECTED] On Behalf Of John Drucker
Sent: Tuesday, September 30, 2008 8:08 AM
To: sprinklerforum@firesprinkler.org
Subject: RE: Alternate to pitch?

BUY STOCK ??,  George turn on your television !...which
station doesn't matter the news is all the same.


-Original Message-
From: [EMAIL PROTECTED]
[mailto:[EMAIL PROTECTED] On Behalf Of George Church
Sent: Tuesday, September 30, 2008 8:06 AM
To: sprinklerforum@firesprinkler.org
Subject: RE: Alternate to pitch?

So we should buy stock in Noble?
glc

-Original Message-
From: [EMAIL PROTECTED]
[mailto:[EMAIL PROTECTED] On Behalf Of Todd Williams
- FPDC
Sent: Tuesday, September 30, 2008 7:49 AM
To: sprinklerforum@firesprinkler.org
Subject: RE: Alternate to pitch?

The existing systems are all OH pipe schedule (with 3/4 pipe) and
the vacant building would be LH. The other consideration is that they
currently have two 1500 gpm pumps taking suction from a pond and part
of the program would be to connect it to the public supply.
Hydraulics and other factors would be taken into consideration, but
the pitch issue is the most complicated. Besides, with 1,500,000
sqsft of pipe network, we'd have to bring in anti-freeze in tank cars



At 07:29 AM 9/30/2008, you wrote:
When converting systems from wet to dry don't we also have to consider the
hydraulics ?.

Is it acceptable to simply convert them to antifreeze and retain the wet
performance ?

John Drucker
Fire Protection Subcode Official (AHJ)
New Jersey

-Original Message-
From: [EMAIL PROTECTED]
[mailto:[EMAIL PROTECTED] On Behalf Of Dewayne
Martinez
Sent: Tuesday, September 30, 2008 7:20 AM
To: sprinklerforum@firesprinkler.org
Subject: RE: Alternate to pitch?

What about pitching the lines and then heat tracing the mains and aux
drains per 8.16.4.1.3 (13 02ed)?
I don't think this is the best option but you were looking for
alternative ideas.
Dewayne

-Original Message-
From: [EMAIL PROTECTED]
[mailto:[EMAIL PROTECTED] On Behalf Of Todd
Williams - FPDC
Sent: Monday, September 29, 2008 4:00 PM
To: sprinklerforum@firesprinkler.org
Subject: Alternate to pitch?

I visited a site the other day which consisted on 1.5 million sqft of
vacant industrial buildings built in the 1950's. The cost to heat these
building is astronomical and the owners are looking for cut costs. They
would like to convert the 30 +/- systems from wet to dry.
Obviously the biggest obstacle is pipe pitch. Some of the lines appear
to pitch, but most lines and mains are flat (caveat: I have not gone in
with a level to check it, but rod lengths looked the same). The lines
look like they could be pitched, but the mains would be a challenge. Are
there any alternatives out there? I don't know of any, but I didn't know
if the collective mind had run across anything.

Todd G. Williams, PE
Fire Protection Design/Consulting
Stonington, Connecticut
www.fpdc.com
860.535.2080
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Stonington, Connecticut
www.fpdc.com
860.535.2080
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Alternate to pitch?

2008-09-29 Thread Todd Williams - FPDC
I visited a site the other day which consisted on 1.5 million sqft of 
vacant industrial buildings built in the 1950's. The cost to heat 
these building is astronomical and the owners are looking for cut 
costs. They would like to convert the 30 +/- systems from wet to dry. 
Obviously the biggest obstacle is pipe pitch. Some of the lines 
appear to pitch, but most lines and mains are flat (caveat: I have 
not gone in with a level to check it, but rod lengths looked the 
same). The lines look like they could be pitched, but the mains would 
be a challenge. Are there any alternatives out there? I don't know of 
any, but I didn't know if the collective mind had run across anything.


Todd G. Williams, PE
Fire Protection Design/Consulting
Stonington, Connecticut
www.fpdc.com
860.535.2080  
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Re: Flow Hydrant vs. Test Hydrant

2008-09-23 Thread Todd Williams - FPDC
The way that I have always done it was to try to get the effective 
point of the test as close to the building as possible. The effective 
point is the junction of flowing and non-flowing water. Often is 
turns out to be the intersection of the hydrant spur with the main 
line. There could be exceptions depending on the arrangement of the 
hydrants and the lead in, but that would need to be looked at individually.




At 10:12 AM 9/23/2008, you wrote:

Content-Type: text/plain;
charset=us-ascii
Content-Transfer-Encoding: 7bit
Content-Disposition:

O.K., can someone please help a dummy out (that would be me)? When looking
at a Civil Site Utility plan what method do you use to determine which
hydrant you want to flow and which one you put the gauge on?  I've heard a
couple different ways, just wanted to get a popular opinion


Regards,


http://www.firstdefensefire.com/








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Re: Flow Hydrant vs. Test Hydrant

2008-09-23 Thread Todd Williams - FPDC
When I was at FM, that was the correct way to test a loop; flow one 
side, then the other, then both. However, most of the sprinkler 
designs were based on the flow of both. I don't understand the water 
company's logic unless there is a possibility that the loop could be 
modified, disconnected or impaired. Was the loop all on the property 
in question?



At 10:43 AM 9/23/2008, you wrote:

Todd.
I did a test the other day. The water purveyor insisted that we shut 
one of the control valves on the loop and test the hydrant furthest 
downsteam.  The gauge hydrant was upsteam ofc the test hydrant.

The purveyor insisted that the loop should not be fully open.
Is that corect?  We were getting infp for a future system.
Sent from my Verizon Wireless BlackBerry

-Original Message-
From: Todd Williams - FPDC [EMAIL PROTECTED]

Date: Tue, 23 Sep 2008 10:38:39
To: sprinklerforum@firesprinkler.org
Subject: Re: Flow Hydrant vs. Test Hydrant


The way that I have always done it was to try to get the effective
point of the test as close to the building as possible. The effective
point is the junction of flowing and non-flowing water. Often is
turns out to be the intersection of the hydrant spur with the main
line. There could be exceptions depending on the arrangement of the
hydrants and the lead in, but that would need to be looked at individually.



At 10:12 AM 9/23/2008, you wrote:
Content-Type: text/plain;
 charset=us-ascii
Content-Transfer-Encoding: 7bit
Content-Disposition:

O.K., can someone please help a dummy out (that would be me)? When looking
at a Civil Site Utility plan what method do you use to determine which
hydrant you want to flow and which one you put the gauge on?  I've heard a
couple different ways, just wanted to get a popular opinion


Regards,


http://www.firstdefensefire.com/








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Re: PDF drawings

2008-09-22 Thread Todd Williams - FPDC

Thanks, Gregg. I'll take a look.



At 08:52 AM 9/22/2008, you wrote:
Todd, Here is a program that I found last week that converts pdf to 
dxf files. the dxf can then imported into autocad and converted to 
dwg. it  makes the drawing usable in autocad. when you download it 
you get 20 free uses . maybe worth checking out. It is called Aide 
PDF to DXF Converter 9.0.  info can be found at http://www.aidecad.com/   Gregg


Todd Williams - FPDC wrote:
I am running into situations more and more where I am given PDF 
files instead of paper copies of plans. Some of the CD's I am 
getting have 50 to 60 drawings on them. I have to open each one, 
figure out what it is and plot it if necessary. Then if I need to 
refer to something else, I have to start opening files again and 
search through. This takes significantly more time than going 
through a set of paper plans. There is a lot of additional time and 
expense with PDFs, which I don't have built into my cost. Has 
anyone been charging a surcharge for receiving PDFs only? I'm 
thinking about doing that and was wondering if anyone else is?

Todd G. Williams, PE
Fire Protection Design/Consulting
Stonington, Connecticut
www.fpdc.com
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PDF drawings

2008-09-20 Thread Todd Williams - FPDC
I am running into situations more and more where I am given PDF files 
instead of paper copies of plans. Some of the CD's I am getting have 
50 to 60 drawings on them. I have to open each one, figure out what 
it is and plot it if necessary. Then if I need to refer to something 
else, I have to start opening files again and search through. This 
takes significantly more time than going through a set of paper 
plans. There is a lot of additional time and expense with PDFs, which 
I don't have built into my cost. Has anyone been charging a surcharge 
for receiving PDFs only? I'm thinking about doing that and was 
wondering if anyone else is?


Todd G. Williams, PE
Fire Protection Design/Consulting
Stonington, Connecticut
www.fpdc.com
860.535.2080  
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Re: viscosities

2008-09-19 Thread Todd Williams - FPDC





IN case the angry mob finds me, does anyone have a painless way for
removing tar and feathers?



Wear a flesh-toned body suit, but don't sen any pics.


Todd G. Williams, PE
Fire Protection Design/Consulting
Stonington, Connecticut
www.fpdc.com
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Re: (no subject)

2008-09-19 Thread Todd Williams - FPDC
I-2 has to be 13. Are the occupants able to get 
out on their own in case of fire? If it is an 
institutional occupancy, chances are they may not 
be able to. When they say group home, you have to 
be sure who the group is. Been there, done that, 
have the T-shirt. (Assumption IBC with no state modifications)




At 11:37 AM 9/19/2008, you wrote:
Occupancy I 2.We can use NFPA 13r for this 
occupancy can't we? The architect is implying 
that it needs to be 13. Its a single story group home 3200 sq ft.


Forest Wilson
Cherokee fire
Sent from my Verizon Wireless BlackBerry

-Original Message-
From: Travis Mack, SET [EMAIL PROTECTED]

Date: Thu, 18 Sep 2008 15:09:57
To: sprinklerforum@firesprinkler.org
Subject: RE: viscosities


Ed:

This system is entirely in the attic.  The riser is the only portion that is
in the heated space.

I do these calculations in 2 parts.  I calculate the system back to the
interface of anti-freeze solution / water and get a pressure  flow demand
at that point utilizing the DW calcs.  I then do a second calculation using
HW that is from the city supply to the interface point.

It is basically how we used to do rack systems calculations.  You calc the
rack system and get a k-factor with pressure/flow demands.  Plug that into
the overhead system and there you go.

In several people that I have talked to today about this, I am getting about
50/50 of saying to use each temp.  It is pretty funny.  I am still waiting
on the AHJ.  Hopefully, I can get a pretty decent concensus soon.



-Original Message-
From: [EMAIL PROTECTED]
[mailto:[EMAIL PROTECTED] On Behalf Of Ed Kramer
Sent: Thursday, September 18, 2008 2:43 PM
To: sprinklerforum@firesprinkler.org
Subject: RE: viscosities

Travis,

This doesn’t address your question, but I'm curious if the entire AF system
is subject to outdoor temps (or just part of it).

I ask, because if a significant part of the system is in a heated area, then
it further complicates selecting an appropriate viscosity.  My limited
understanding of HydraCalc is that a single viscosity and a single density
is entered for the entire calc (if I'm wrong, someone please correct me).
Do you use the high viscosity (extreme min temp), the medium viscosity
(average min temp) or the low viscosity (room temp)?  Obviously the room
temp viscosity wouldn't be appropriate, but how's a designer to choose?  As
in your example, the selected viscosity can make a whale of a difference in
system costs.

I've yet to calc an AF system using Darcy-Weisbach, so I'm hoping someone
can enlighten me.

Ed Kramer
Littleton, CO



 Ok..another viscosity question.

 When using HydraCalc to calculate antifreeze systems using the Darcy
 method, it asks for viscosities of solutions.  I have a data sheet
 with the viscosities at various concentrations and various
 temperatures.  My question is, do you use the average daily minimum
 temperature for an area, or the extreme daily minimum for an area?
 For this particular project, the difference is 40°F in the 2
 temperatures.  With the average daily minimum temperature, the system
works with the available pressure.
 With the extreme daily minimum, the city supply is not even close.
 There is a 100+ psi swing in the demands.

 So, do we go with average minimums, or extreme minimums?

 There is always the option to go to a dry system, but the increased
 design areas and reduced c factor will also force a pump on this
 project.  An anti-freeze system at average daily minimum works without
 a fire pump.
 However, we don't want to design/install an inadequate system.


 Please feel free to call if you have any questions or comments.

 Travis Mack, SET
 MFP Design, LLC
 2508 E Lodgepole Dr
 Gilbert, AZ 85298
 480-505-9271
 [EMAIL PROTECTED]


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Todd G. Williams, PE
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Stonington, Connecticut
www.fpdc.com
860.535.2080  
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Re: Hydro and UG Test Thoughts #2

2008-09-16 Thread Todd Williams - FPDC

The Forum is alive! I haven't heard anything for about 3 weeks. Cool


At 12:00 AM 9/16/2008, you wrote:

I just went through this on a recent department store inspection.
I agree that the inspector should conduct a thorough inspection of 
any acceptance test.
Many look at the gauge and leave, I try to walk them through and 
point out system components. In Ohio we have around 200 building 
departments and 400 fire districts and every area is different. 
that's why its good for ahj's to join an organization like the afsa 
or Nfsa so they utilize the training and know what they're doing. 
Unfortunately, many don't and the inspections turn out to be an 
added cost of doing business.

Sent from my Verizon Wireless BlackBerry

-Original Message-
From: Dave Phelan [EMAIL PROTECTED]

Date: Mon, 15 Sep 2008 21:12:31
To: sprinklerforum@firesprinkler.org
Subject: Hydro and UG Test Thoughts #2


After posting on the underground flush topic last week I got a few emails of
encouragement and such that brought another idea to mind and I figured why
not take my soapbox out for another spin .

The hydrostatic test is apparently overlooked or not witnessed by AHJ's in a
good portion of the areas represented.  Im sure many reason that it's a
wasted trip to look at a gauge and no one is going to come back in two hours
to re-check it.  I agree as far as not standing there for 2 hours watching a
gauge but how about not standing but instead walking .

You call for a hydro test / inspection and I show up somewhere close to the
time scheduled and sure enough the gauge reads 200 PSI  time to start
walking fellas - approved plans in hand we start from the base of riser and
move outward through the trim and piping checking pipe size, trim, valves,
head positions, head SIN's, hanging and bracing methods, seismic (GASP !!),
numbers of branch lines, number of heads on branch lines, and of course the
obstructions that never were conceived on the drawing table such as ducts,
structural elements, etc .

Wow, would you look at the time  easily that process can take me 45
minutes on a 2,000 ft/2 restaurant and exponentially from there as height
and area increases.  Care to guess on the inspection of the 238,000 ft/2 big
box store???  Before long the two hour test and contractor certification has
real meaning because as an AHJ I spent a comprable amount of time checking
the system itself.  I dont want people thinking I run around with a ruler
checking every little dimension but I can sure count heads on a branch and
branches on a cross main and get an idea quickly if something isn't quite
right.  I am actually amazed myself at how often things come up 'short' in
the field and send it back for either resubmission by the designer or field
correction to match the approved plans.

Note to self ... a hydro test is supposed to be about pipe integrity and the
ability to hold itself together under pressure similar to those likely to be
found under actual fire conditions.  If all we were supposed to do was look
at the gauge we could just call it a gauge test and skip all that fancy
nomenclature.  Getting it right is indeed 'good enough' in my inspection
world.

Thanks once again.

Dave P.

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Re: Paint booths - explosion proof tamper switch

2008-09-16 Thread Todd Williams - FPDC
I have run into something similar in the past. I believe the 
reference may be in NFPA 33 or 72 on locations for explosion proof equipment



At 11:40 AM 9/16/2008, you wrote:

Has anyone heard of a rule that if an electrical device (ie: valve
tamper switch) is within 3 ft from the paint booth opening that it and
it's associated wiring must be in explosion proof casings?
Thanks,
Dewayne
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anybody out there?

2008-08-26 Thread Todd Williams - FPDC

Was it something I said?

Todd G. Williams, PE
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Xerxes tank suction line

2008-08-25 Thread Todd Williams - FPDC
I have two projects where I am considering using 20,000 gallon Xerxes 
tanks as suction sources from fire pumps. However, the arrangement of 
the anti-vortex plate (AVP) and suction line do not conform to NFPA 
20, as I read it. Instead of the down-turned elbow with AVP at the 
intake, they have a straight suction line with an AVP on top of and 
extending beyond the end of the pipe. The Xerxes rep (who is a 
reputable person, in my experience) has assured that hundreds of them 
have been used and it is acceptable. I'm not convinced yet. Does 
anyone have experience with these tanks?


Todd G. Williams, PE
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underground through building

2008-08-18 Thread Todd Williams - FPDC
I am working on a church building with no public water. They proposal 
is to install a fire pump and 20,000 gallons of impounded water. The 
building is built and the underground partially installed, but is 
wrong and needs to be replaced. The fire pump room is in the middle 
of the building and cannot be relocated. The elevation of the bottom 
of the tank is going to be approximately 8 ft above the floor of the 
pump room. The site is on a side hill. The basement is walkout at the 
far end of the building and the front of the building is 
approximately grade level at first floor.


The proposal is to go underground in the pump room with the new 8 
line, over to a stairway by an outside wall, back up through the 
slab, up approximately 4 ft and out through the foundation wall to 
the tank. The pipe would then be run to the suction tank(s). By 
raising up inside, the 350' +?- of trench will only need to be 6 ft 
instead of 10-12.


Is this proposal an acceptable arrangement? I could not find anything 
in NFPA 24 that says otherwise. Do I need or would any additional 
valve be installed on the indoor section of pipe?




Todd G. Williams, PE
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Stonington, Connecticut
www.fpdc.com
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RE: underground through building

2008-08-18 Thread Todd Williams - FPDC
This is an existing project where the original contractor screwed up 
and was thrown off the job. One of my regular clients took it and 
asked me to help straighten it out.


There is no way presently to avoid running under the building. The 
requirements of 6.2 are being applied.


The pump room cannot be directly accessed from the outside. If they 
can get the pump in, they should be able to get it out as well. The 
room, while tight, is adequate size. The local AHJ is aware of it and 
has supposedly accepted the arrangement.


Drainage is another issue we are working on.

There is more, but not for this post

Todd



At 11:54 AM 8/18/2008, you wrote:

You've got a bunch of issues there.


Pipe under buildings:  check NFPA 24, 10.6.1 PIPE SHALL NOT BE RUN 
UNDER BUILDINGS.


There is some allowance when it can't be avoided as listed in 10.6.2.

Can the pump room be accessed directly from outside?  Is there any 
way to service or even remove the pump if necessary once the building is done?


Is there adequate drainage from the pump room to prevent it from 
being flooded?







Craig L. Prahl, CET
Fire Protection Group
Mechanical Department
CH2MHILL
Lockwood Greene
1500 International Drive
PO Box 491, Spartanburg, SC  29304-0491
Direct - 864.599.4102
Fax - 864.599.8439
[EMAIL PROTECTED]
http://www.ch2m.com

-Original Message-
From: [EMAIL PROTECTED] 
[mailto:[EMAIL PROTECTED] On Behalf Of Todd 
Williams - FPDC

Sent: Monday, August 18, 2008 11:14 AM
To: sprinklerforum@firesprinkler.org
Subject: underground through building

I am working on a church building with no public water. They 
proposal is to install a fire pump and 20,000 gallons of impounded 
water. The building is built and the underground partially 
installed, but is wrong and needs to be replaced. The fire pump room 
is in the middle of the building and cannot be relocated. The 
elevation of the bottom of the tank is going to be approximately 8 
ft above the floor of the pump room. The site is on a side hill. The 
basement is walkout at the far end of the building and the front of 
the building is approximately grade level at first floor.


The proposal is to go underground in the pump room with the new 8
line, over to a stairway by an outside wall, back up through the 
slab, up approximately 4 ft and out through the foundation wall to 
the tank. The pipe would then be run to the suction tank(s). By 
raising up inside, the 350' +?- of trench will only need to be 6 ft 
instead of 10-12.


Is this proposal an acceptable arrangement? I could not find 
anything in NFPA 24 that says otherwise. Do I need or would any 
additional valve be installed on the indoor section of pipe?




Todd G. Williams, PE
Fire Protection Design/Consulting
Stonington, Connecticut
www.fpdc.com
860.535.2080
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Re: Sterilization

2008-08-15 Thread Todd Williams - FPDC
Sterilization is, by definition, the elimination of bacteria or 
microorganisms. In order to make something truly free of 
microorganisms, the components would needs to be free as well. This 
means that the water to flush the system at the end of 8 hours would 
have to be sterile in order to make the system sterile. Where are you 
going to get the sterile water to flush? Is there a test for 
sterility required? Water in underground mains is not sterile. Once 
you introduce public water into the mains, it is no longer sterile. 
Decontaninated would be a better word.


Note to all on Friday afternoon: I am fully aware that underground 
mains cannot by themselves reproduce, so that definition of 
sterilization was deemed not applicable




Todd G. Williams, PE (son of bacterilolgist)
Fire Protection Design/Consulting
Stonington, Connecticut
www.fpdc.com
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green dry chemical agent

2008-08-13 Thread Todd Williams - FPDC
A while back, there was a post that mentioned a dry chemical agent 
that was a more 'green' product that FM-200 or Inergen. I can't seem 
to find the reference. Anybody out there remember what it was?


Todd G. Williams, PE
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www.fpdc.com
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Re: green dry chemical agent

2008-08-13 Thread Todd Williams - FPDC

Yea, that's the ticket... Thanks



At 07:26 AM 8/13/2008, you wrote:

NOVEC 1230 I believe.

Andrew Weisfield




Todd Williams - FPDC [EMAIL PROTECTED]
Sent by: [EMAIL PROTECTED]
08/13/2008 07:21 AM
Please respond to
sprinklerforum@firesprinkler.org


To
sprinklerforum@firesprinkler.org
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Subject
green dry chemical agent






A while back, there was a post that mentioned a dry chemical agent
that was a more 'green' product that FM-200 or Inergen. I can't seem
to find the reference. Anybody out there remember what it was?

Todd G. Williams, PE
Fire Protection Design/Consulting
Stonington, Connecticut
www.fpdc.com
860.535.2080
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RE: Backflows

2008-08-07 Thread Todd Williams - FPDC

I'm sure FM tests more than leakage.



At 01:32 PM 8/7/2008, you wrote:

Dear All,

Question about UL listed FM Approved Flexible Pipes.

A contractor told me:

A.  The cost of UL listed/FM approved Flexible Pipe is four (4) times as
much as UL listed pipe.

B.  There is no history about leakage of UL listed flexible pipe, thus
the addition of FM approval is redundant.

I would appreciate any comments, public or private.

Dan





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pre action literature

2008-08-06 Thread Todd Williams - FPDC
Are there any good non-technical data sheets describing pre-action 
systems? I have an IT department that wants some kind of overview, 
but mfr. data sheets are a little too technical and are just specific 
to their product


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RE: pre action literature

2008-08-06 Thread Todd Williams - FPDC

Never explored that part of their web site. thanks


At 11:49 AM 8/6/2008, you wrote:

Todd,

Viking has some nice data in their book under Tech Data.

R/
Matt

-Original Message-
From: [EMAIL PROTECTED]
[mailto:[EMAIL PROTECTED] On Behalf Of Todd
Williams - FPDC
Sent: Wednesday, August 06, 2008 10:35 AM
To: sprinklerforum@firesprinkler.org
Subject: pre action literature

Are there any good non-technical data sheets describing pre-action
systems? I have an IT department that wants some kind of overview, but
mfr. data sheets are a little too technical and are just specific to
their product

Todd G. Williams, PE
Fire Protection Design/Consulting
Stonington, Connecticut
www.fpdc.com
860.535.2080
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indoor suction tanks

2008-08-06 Thread Todd Williams - FPDC
I am working on a project where we need to have a 20,000 gallon 
impounded water supply to feed a fire pump. One of the owner's 
options is to install two 10,000 gallon tanks in a basement. The 
latest similar project I was involved in turned out to be a disaster, 
because they ordered the wrong tanks and built the building over them 
before anybody found out (I was brought in to pick up the pieces). 
Does anyone have a good or bad experience with any specific tanks 
when they are installed inside? I was thinking steel because most of 
the fiberglass ones I looked at were designed for underground. Thoughts?


Todd G. Williams, PE
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Re: Panel Construction vs room less than 300 sqft.

2008-08-06 Thread Todd Williams - FPDC
I have applied this in the past, but only in specific circumstances 
where it would save extra sprinklers in  a small space. It seems to 
meet the letter of the standard, but perhaps not the intent.


I think we should apply for a grant to study this at the Bitter End 
Yacht Club on Virgin Gorda for about 3 weeks in February. Anybody wanna help?



At 07:06 PM 8/6/2008, you wrote:

Excellent question.  Inquiring minds want to know

Here's how it plays out in my mind and the discussion I would prompt
within the technical committee.  The describe scenario certainly traps
the heat within an area less than 300sf.  Is a standard drop ceiling
an issue since beamed construction indicates a floor or roof
assemblies that is a tad more robust than a drop ceiling?

A final question, is someone interested enough in this issue to pay
for a fact finding trip to some fabulous golf course.  No wait, that's
only applicable to Congress.

What do you folks (non-gender specific) think?

Roland

On Aug 6, 2008, at 3:03 PM, Fletcher, Ron wrote:


Okay, this is really reaching but what to heck.

A 10'x15' light hazard room with a duct (bottom @24) running down the
center and sometimes turning or teeing off at 90 degrees would require
two and sometimes three sprinklers to comply with the obstruction
rules.

If each wall is considered a structural member capable of trapping
heat
could the 22 deflector distance for panel construction be used? The
members (walls) are more than 7.5 ft apart and area of the panel is
less
than 300 sqft. At a 22 deflector it would spray under the duct

It just makes no sense to allow 22 deflector distances for gluelam
beams 8 ft. on center in a large open area but then enforce a 12
deflector distance in a 150 sqft noncombustible room.

Ron Fletcher
Aero Automatic Sprinkler
Phoenix, AZ
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RE: Floating Ceilings

2008-08-05 Thread Todd Williams - FPDC
Almost concealed? Almost only counts in horseshoes and nuclear war. 
Now concealed spaces?



At 02:47 PM 8/5/2008, you wrote:

okay, I'll add more fuel to this pile.
Check out the 2009 Report on Proposals, Item 13-210, for a new paragraph
8.15.22.3, which it appears that the committee accepted in principle.

This would allow for a largely unsprinklered noncombustible space
above a lower ceilings of an office or retail sales area...and the space
above the ceiling doesn't even have to be cut-off from the storage
areas. Sprinklers are required below the ceiling, but the sprinklers at
the high roof would only extend into a portion of the space above the
ceiling. The proposal even calls this an almost concealed space.

I personally don't agree with this proposal, but it on the books for
discussion.
rick matsuda
city of dallas
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RE: effective tank volume

2008-08-03 Thread Todd Williams - FPDC
The other detail is that I have to give them an elevation for the 
bottom of the tank. In addition, there is about 315 equivalent feet 
of pipe from the tank to the pump. the building requires a 500 gpm 
pump and I plan on calling for an 8 suction line. I was also 
thinking about insisting that the center line of the suction line be 
6 ft above the centerline of the pump for just that reason.



At 11:56 PM 8/2/2008, you wrote:
Yes - but remember that you have positive pressure when the tank is 
filled.  (Normally, a horizontal, split-case pump is taking suction 
from a tank whose water elevation - when filled - is above the 
centerline of the pump). It is only after the tank has nearly 
emptied that you'd have a negative pressure condition. At that 
point, you'll be in a siphon condition.


Mark Sornsin, PE
Ulteig engineers, Inc.
Fargo, ND

-Original Message-
From: [EMAIL PROTECTED] 
[mailto:[EMAIL PROTECTED] On Behalf Of Russell

Sent: Friday, August 01, 2008 3:57 PM
To: sprinklerforum@firesprinkler.org
Subject: RE: effective tank volume

Would not anything below the centerline of the pump impellor be a negative
pressure? Split-case centrifugal pumps have to have a positive pressure on
the suction side. Or have I misunderstood the situation?

Russell Rewis
Brown Automatic Sprinklers, Inc.
107C Hemlock Street
Valdosta, Georgia 31601
229-244-8130
[EMAIL PROTECTED]
-Original Message-
From: [EMAIL PROTECTED]
[mailto:[EMAIL PROTECTED] On Behalf Of Ed Kramer
Sent: Friday, August 01, 2008 2:14 PM
To: sprinklerforum@firesprinkler.org
Subject: RE: effective tank volume

I recently completed a similar project.  I agree with Mark, the available
water is that part of the tank below the inlet of the overflow and above the
bottom of the vortex plate.  Also, reference NFPA 22 section 4.1.3  (03
edition).

Ed Kramer
Littleton, CO

 -Original Message-
 From: [EMAIL PROTECTED] [mailto:sprinklerforum-
 [EMAIL PROTECTED] On Behalf Of Todd Williams - FPDC
 Sent: Friday, August 01, 2008 7:05 AM
 To: sprinklerforum@firesprinkler.org
 Subject: effective tank volume

 I am working on a project where the water supply for the facility
 will be fed from concrete tank(s). The absolute volume (completely
 full) of the tank is 10098 gallons. A 6 suction line with elbow 
 anti-vortex plate will need to be installed. According to NFPA 22,
 the face of the suction elbow has to be a minimum of 6 above the
 bottom of the tank. The take-out for the elbow is 8 and the top of
 the pipe will be 4 (+/-) above that. I am trying to calculate the
 effective or usable volume in the tank based on what my minimum
 height above the floor can be relied on for suction. Would it be the
 6 to the bottom of the elbow? 14 to the center line of the suction
 pipe? 18 to the top of the suction pipe? The tank is 10 feet tall,
 so this could have a significant impact on available water. (BTW, I
 am already assuming that the tank will only be filled 9 to 12 from
 the top; would that be reasonable?)

 Todd G. Williams, PE
 Fire Protection Design/Consulting
 Stonington, Connecticut
 www.fpdc.com
 860.535.2080
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effective tank volume

2008-08-01 Thread Todd Williams - FPDC
I am working on a project where the water supply for the facility 
will be fed from concrete tank(s). The absolute volume (completely 
full) of the tank is 10098 gallons. A 6 suction line with elbow  
anti-vortex plate will need to be installed. According to NFPA 22, 
the face of the suction elbow has to be a minimum of 6 above the 
bottom of the tank. The take-out for the elbow is 8 and the top of 
the pipe will be 4 (+/-) above that. I am trying to calculate the 
effective or usable volume in the tank based on what my minimum 
height above the floor can be relied on for suction. Would it be the 
6 to the bottom of the elbow? 14 to the center line of the suction 
pipe? 18 to the top of the suction pipe? The tank is 10 feet tall, 
so this could have a significant impact on available water. (BTW, I 
am already assuming that the tank will only be filled 9 to 12 from 
the top; would that be reasonable?)


Todd G. Williams, PE
Fire Protection Design/Consulting
Stonington, Connecticut
www.fpdc.com
860.535.2080  
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RE: effective tank volume

2008-08-01 Thread Todd Williams - FPDC
This tank in question is basically a concrete vault that will be 
retrofitted as a suction tank. We are going to have to add the 
suction line, fill line overflow and probably some sort of a fill 
gauge. I'm assuming that there is an opening in the tank for access. 
They don't want to pay the extra for a fiberglass tank with 
everything already installed, so we are going to have to make this work.


My guess is that we are going to lose a total of 12-15 from the tank 
height, so the effective volume will be around 8700 gallons, instead 
of the 10,000 gallons rated.


At 12:50 PM 8/1/2008, you wrote:

Todd:  I believe you want to use the '6 in. to bottom of elbow' option.

Once flow begins to the pump, the pump will siphon the water up the 
elbow and out the tank until air can enter the pipe - which will 
occur when the level in the tank drops to the 6 inch depth (where 
the opening of the elbow is positioned above the floor of the tank).


As to the upper elevation of the water, I think you can assume full 
depth of the tank - at least to the over-flow pipe.


Mark A. Sornsin, PE
Fire Protection Engineer
Ulteig Engineers, Inc.

[EMAIL PROTECTED]
www.ulteig.com




-Original Message-
From: [EMAIL PROTECTED] 
[mailto:[EMAIL PROTECTED] On Behalf Of Todd 
Williams - FPDC

Sent: Friday, August 01, 2008 8:05 AM
To: sprinklerforum@firesprinkler.org
Subject: effective tank volume

I am working on a project where the water supply for the facility
will be fed from concrete tank(s). The absolute volume (completely
full) of the tank is 10098 gallons. A 6 suction line with elbow 
anti-vortex plate will need to be installed. According to NFPA 22,
the face of the suction elbow has to be a minimum of 6 above the
bottom of the tank. The take-out for the elbow is 8 and the top of
the pipe will be 4 (+/-) above that. I am trying to calculate the
effective or usable volume in the tank based on what my minimum
height above the floor can be relied on for suction. Would it be the
6 to the bottom of the elbow? 14 to the center line of the suction
pipe? 18 to the top of the suction pipe? The tank is 10 feet tall,
so this could have a significant impact on available water. (BTW, I
am already assuming that the tank will only be filled 9 to 12 from
the top; would that be reasonable?)

Todd G. Williams, PE
Fire Protection Design/Consulting
Stonington, Connecticut
www.fpdc.com
860.535.2080
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Todd G. Williams, PE
Fire Protection Design/Consulting
Stonington, Connecticut
www.fpdc.com
860.535.2080  
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beam strength for hangers

2008-07-25 Thread Todd Williams - FPDC
NFPA 13 (2002) 9.1.1.2(1) states that Hangers shall be designed to 
support five times the weight of water-filled pipe plus 250 lb at 
each point of piping support. Does this mean the hanger assembly 
only, or does make it incumbent on the structural steel to actually 
support this load as well? For a 10 ft piece of 4 sch 10, this would 
equate to a point load of 839 pounds. We have to get some information 
to a CE to figure out how to hang a system.


Todd G. Williams, PE
Fire Protection Design/Consulting
Stonington, Connecticut
www.fpdc.com
860.535.2080  
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RE: beam strength for hangers

2008-07-25 Thread Todd Williams - FPDC

Never saw that one before. Thanks


At 03:06 PM 7/25/2008, you wrote:

Todd,

see 9.2.1.3 (07) under building structure. Not sure which parag, in 02

R/

Matt

-Original Message-
From: [EMAIL PROTECTED]
[mailto:[EMAIL PROTECTED] On Behalf Of Todd
Williams - FPDC
Sent: Friday, July 25, 2008 1:40 PM
To: sprinklerforum@firesprinkler.org
Subject: beam strength for hangers

NFPA 13 (2002) 9.1.1.2(1) states that Hangers shall be designed to
support five times the weight of water-filled pipe plus 250 lb at each
point of piping support. Does this mean the hanger assembly only, or
does make it incumbent on the structural steel to actually support this
load as well? For a 10 ft piece of 4 sch 10, this would equate to a
point load of 839 pounds. We have to get some information to a CE to
figure out how to hang a system.

Todd G. Williams, PE
Fire Protection Design/Consulting
Stonington, Connecticut
www.fpdc.com
860.535.2080
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Todd G. Williams, PE
Fire Protection Design/Consulting
Stonington, Connecticut
www.fpdc.com
860.535.2080  
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RE: Deperming Pier

2008-07-24 Thread Todd Williams - FPDC
I would be very concerned about joint restraint if plastic pipe is 
used. There cold be a significant water hammer with that type of flow 
from dry system.


The EoR should be consulted, but it is always best to go into that 
discussion with as much information as possible.




At 09:27 AM 7/24/2008, you wrote:

I'd be concerned about two things with CPVC-
Effects of sunlight, even under the pier you'd likely get strong reflections
off the water; and where are you getting 6 CPVC?
I have no idea if regular plumber's PVC would work; if you have a
low-pressure DPV, and you're looking at a 2.5 DPV as your activating device
(and combo exhauster, it's a pretty big orifice) then wouldn't the air never
be at high pressure and so it shouldn't be a problem to use PVC?

NFI, just a thought that would save my tax dollars versus SS316.

glc

-Original Message-
From: [EMAIL PROTECTED]
[mailto:[EMAIL PROTECTED] On Behalf Of
[EMAIL PROTECTED]
Sent: Thursday, July 24, 2008 8:49 AM
To: sprinklerforum@firesprinkler.org
Subject: RE: Deperming Pier

What if you ran plastic, CPVC is approved for fire protection above grade
per NFPA 13.  See 6.3 of NFPA 13, 2007.






Craig L. Prahl, CET
Fire Protection Group
Mechanical Department
CH2MHILL
Lockwood Greene
1500 International Drive
PO Box 491, Spartanburg, SC  29304-0491
Direct - 864.599.4102
Fax - 864.599.8439
[EMAIL PROTECTED]
http://www.ch2m.com

-Original Message-
From: [EMAIL PROTECTED]
[mailto:[EMAIL PROTECTED] On Behalf Of Rick Green
Sent: Thursday, July 24, 2008 8:19 AM
To: sprinklerforum@firesprinkler.org
Subject: Deperming Pier


I am installing a dry pipe system (no sprinklers) supplying four hose valves
on a pier.

The dry pipe valve assembly is located in a heated area.  Extending out from
the dry pipe valve assembly  is 6 galvanized steel pipe.  The steel pipe is
routed below the pier out to the  location of four hose valves.

The pier is used for Deperming ships, submarines.

Deperming is a procedure for erasing the permanent magnetism from ships and
submarineshttp://en.wikipedia.org/wiki/Submarines to
camouflagehttp://en.wikipedia.org/wiki/Camouflage them against magnetic
detection vessels and enemy marine
mineshttp://en.wikipedia.org/wiki/Naval_mines.

Anyway, there is about a 200' section of the pier that requires that all
materials be non-magnetic.

*Galvanized steel pipe that NAVY specified obviously want work.

*CPVC plastic pipe will not work because installing dry system -
correct on this right?

*Provided them pricing for stainless steel, copper, brass and now
they want pricing for Aluminum,.

So a few questions

o   Ever used aluminum pipe for sprinkler installations?

o   Is there some other pipe type that I am not thinking about

Help would be most appreciated.

Rick E. Green
District Manager
East Coast Fire Protection, Inc.
1113 Cavalier Boulevard
Chesapeake, Virginia 23323
757/485-7486(p), 757/295-0956(direct), 757/328-0131(cell) [EMAIL PROTECTED]

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Todd G. Williams, PE
Fire Protection Design/Consulting
Stonington, Connecticut
www.fpdc.com
860.535.2080  
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RE: domed ceiling

2008-07-22 Thread Todd Williams - FPDC
This is kind of what I thought, but wanted to bounce it off the group 
before I shot my mouth off




At 03:34 PM 7/21/2008, you wrote:
Todd:  I think the temptation is to suggest that since the dome is 
smaller than the required area of sprinkler operation of 1,500 
sq.ft., then we shouldn't have to increase the design area for the 
sloped portions of the dome.  If the room was no more than 1,500 
sq.ft. in area, I would agree with that approach.  But in this case, 
the remote area could include flat ceiling adjacent to the dome.  A 
fire could conceivably open more heads within the dome (and outside 
the base design area) due to the sloped ceiling.


Bottom line is that at there is no verbiage in NFPA 13 to suggest 
you can ignore the sloped ceilings of a dome when considering area increases.



Mark A. Sornsin, PE
Fire Protection Engineer
Ulteig Engineers, Inc.
3350 38th Avenue S.
Fargo, ND 58104-7079


-Original Message-
From: [EMAIL PROTECTED] 
[mailto:[EMAIL PROTECTED] On Behalf Of Todd 
Williams - FPDC

Sent: Monday, July 21, 2008 9:29 AM
To: sprinklerforum@firesprinkler.org
Subject: domed ceiling

This must be sloped ceiling day. I have a client with a church
project where the sanctuary is a cross and at the intersection is a
dome. The ceilings around the dome are flat at approx 28 ft and the
dome rises to 57 ft. The room area is approx 6400 sqft and the dome
is 1200 sqft. Do we have to include the 30% increase for roof slope
in the design area because of the dome?

Todd G. Williams, PE
Fire Protection Design/Consulting
Stonington, Connecticut
www.fpdc.com
860.535.2080
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www.fpdc.com
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Re: sloped attic rrofs

2008-07-21 Thread Todd Williams - FPDC

Both are considered a peak


At 09:50 AM 7/21/2008, you wrote:

Does the reference to a peak in 8.6.4.1.4.2 2007 edition refer to
where two slopes meet ONLY; or does it also refer to a single sloped
roof that meets a vertical wall?

Thanks,
Greg McGahan
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domed ceiling

2008-07-21 Thread Todd Williams - FPDC
This must be sloped ceiling day. I have a client with a church 
project where the sanctuary is a cross and at the intersection is a 
dome. The ceilings around the dome are flat at approx 28 ft and the 
dome rises to 57 ft. The room area is approx 6400 sqft and the dome 
is 1200 sqft. Do we have to include the 30% increase for roof slope 
in the design area because of the dome?


Todd G. Williams, PE
Fire Protection Design/Consulting
Stonington, Connecticut
www.fpdc.com
860.535.2080  
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Re: ex cov sprinklers

2008-07-20 Thread Todd Williams - FPDC

Stick with the cut sheets; anything else could get you in trouble.



At 04:15 PM 7/19/2008, you wrote:

I have a big box retail project where the design criteria is 0.19 gpm / sq
ft over 2000 sq ft.  The design documents specify to use Tyco EC-11 ex cov
sprinklers.  The sprinklers are spaced at 16X16 sq ft.  Per the data sheet,
for OH2 (0.20 density), the sprinkler is req'd to discharge 51 gpm.
However, the consultant is saying that because our specified density is 0.19
that we are able to only discharge 48.64 (256*.19)gpm per sprinkler.  Has
anyone done this before?  Is it acceptable?  I thought I had to go with the
minimum the sprinkler cut sheet shows for OH2 (51 gpm).

Any thoughts?

T

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Re: Is this going thru

2008-07-17 Thread Todd Williams - FPDC

No, It's not coming through. Can you speak louder?



At 04:47 PM 7/17/2008, you wrote:

Someone respond and let me know if this is being posted.  Thanks in advance

Geoffrey H. Dyce
Sales Manager
Contractor I, #87582700012007
NICET IV
Industrial Fire  Safety Inc.
Ph:727-573-1556
Fx:727-572-7266
Cell:  727-644-8872

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Re: Egress distance

2008-07-16 Thread Todd Williams - FPDC

CT uses Table 1015.1



At 08:11 PM 7/15/2008, you wrote:

Gentlemen,
Would you please share with me building code info of state that you are
working in.
I need to collect info related to egress distance for S-1 and F-1 occupancy
in different states (with and without sprinkler system). Would you be so
kind and let me know required egress distance, state and edition of
International Building Code that your state is using (NC has those
information in Table 1015.1 of Building Code).
I would appreciate you help.

Anna Reich
E-mail: [EMAIL PROTECTED]

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Todd G. Williams, PE
Fire Protection Design/Consulting
Stonington, Connecticut
www.fpdc.com
860.535.2080  
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This could get interesting.....

2008-07-16 Thread Todd Williams - FPDC

http://www.wtnh.com/Global/story.asp?S=8682369

I'll try to keep everyone informed as this develops

Todd G. Williams, PE
Fire Protection Design/Consulting
Stonington, Connecticut
www.fpdc.com
860.535.2080  
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Re: Entry Vestibule situation...

2008-07-16 Thread Todd Williams - FPDC
If you find something, let me know. If it is part 
of the building egress, you may not have an option except to sprinkler it.




At 11:24 AM 7/16/2008, you wrote:

Content-Type: multipart/related;
boundary==_reb-r1671FF6F-t487E15F9
Content-Language: en-us



Forum…

Have a building with a situation that I need help in addressing ­ small
entry vestibule (14’8” x 7’) which has glass exterior and interior doors and
windows ­ full height; with concrete walls, floor, and ceiling enclosing it.
Access to this area is close to impossible…  Is there anything in NFPA that
I’m missing which would allow me to exclude this area?



Thanks in advance.



RFP Chuck


No virus found in this outgoing message.
Checked by AVG.
Version: 7.5.524 / Virus Database: 270.5.0/1555 - Release Date: 7/16/2008
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Todd G. Williams, PE
Fire Protection Design/Consulting
Stonington, Connecticut
www.fpdc.com
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Re: incoming vs. 'need'

2008-07-16 Thread Todd Williams - FPDC
Does the size of the existing underground pipe 
match the pipe sizing requirements of NFPA 20?




At 01:12 PM 7/16/2008, you wrote:

Content-Type: multipart/related;
boundary==_reb-r4F874F0F-t487E2C2A
Content-Language: en-us



Another one to throw at all…

Just got off the phone with a g.c. regarding the need for an ‘upsizing’ of
the already installed, buried, and built-upon underground feed.  He said
that he would like to (at his own $$) provide a booster pump (instead of
installing a larger underground feed) prior to the domestic / fire sprinkler
service connection(s) which would inevitably increase the characteristics of
the supply.



This all came about as from bid to build ­ changes galore have happened and
thus we have had to double the quantity of heads on a proposed dry system!



I’m seeing several concerns in the grand scheme of things… and I need some
help in pinpointing something in NFPA that will say “yay” or “nay” to what
they want to do.



Thanks again Forum,

RFP Chuck




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Checked by AVG.
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Todd G. Williams, PE
Fire Protection Design/Consulting
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www.fpdc.com
860.535.2080  
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Re: Explosives

2008-07-15 Thread Todd Williams - FPDC
I kind of go along with the comments that this should not be parked 
under a grandstand, especially when occupied. If this thing is moved, 
I would look into some form of self-contained protection, such as a 
dry chemical. But the purpose would only be to keep the combustible 
construction from igniting the fireworks. Why don't they get a 
container and put it on a trailer? At least that is all metal and 
would eliminate the wood construction.



At 04:54 AM 7/15/2008, you wrote:


- Original Message - From:  douglas hicks [EMAIL PROTECTED]
To: sprinkler board sprinklerFORUM@firesprinkler.org
Sent: Monday, July 14, 2008 3:03 PM
Subject: Explosives


I have a customer who stores a quantity of less than 2 # of Class 
1.4G explosives.  These explosives are comparable to fireworks.  The 
1.4G is stored in a metal cabinet, not rated. The storage unit is 8 
foot wide x 8 foot high x 12 foot long.  The construction is wood 
frame, plywood floor, wood panel interior, and metal outside.  If 
this sounds like a job trailer, your are right.  The trailer is 
parked under a grandstand.  the steel/wood grandstand is protected 
with a dry system, under the grandstands.  Other contents are 
ordinary combustibles, wood, paper, cardboard.


Upon occasion, the trailer is moved to other locations for 
shows.  Then the trailer is parked under the grandstand.  unless the 
trailer is put in the exact same spot, connection to the sprinkler 
system will be difficult.  Can the flex head work for this 
application?  As the 1.4G is in a cabinet, I would feel better with 
a sprinkler head in the cabinet, with a head or heads protecting the trailer.


Any suggestions?

Douglas Hicks
General Fire Equipment Co of Eastern Oregon, Inc


Oops, I was not clear enough on the these explosives are comparable 
to fireworks  I did not mean the arial rockets.  I meant the kind 
you get from the tents for the kids to fire off for the Fourth of 
July.  Maybe I should have said pyrotechnics, as these are like 
you might see at a rock concert. But keep the comments coming.  When 
I told the FM I would post on the Sprinkler Board, he was relieved 
to have the input from the Board.

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www.fpdc.com
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Re: Institutional Sprinklers

2008-07-14 Thread Todd Williams - FPDC

100 psi water and don't open the door for 30 seconds.



At 03:52 PM 7/14/2008, you wrote:

Problem; we have some institutional sprinklers in a holding cell at a local
jail that repeatedly are getting knocked out by the temporary inmates. Has
anybody come up with a good solution to this problem from our end; specialty
sprinkler guards or anything?



Thank you in advance,



Bobby Gillett

Project Manager

[EMAIL PROTECTED]

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Todd G. Williams, PE
Fire Protection Design/Consulting
Stonington, Connecticut
www.fpdc.com
860.535.2080  
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Re: Water supply question

2008-07-09 Thread Todd Williams - FPDC
Without doing any engineering and no other 
information, I would say probably not. According 
to A.5.6.3, cartoned carpet tiles are a Group A 
plastic. The latex foam pads are another bundle 
of joy. 55psi may not be enough to handle the 
demand. More engineering is needed on this 
project to make an actual determination. 
(Disclaimer: my opinion only and may not have any basis in fact)




At 10:10 AM 7/9/2008, you wrote:


I am looking at a 25,000 sq foot former 
manufacturing facility that is being renovated 
and a wet system is being provided. A storage 
area- 4700 sq ft. will contain rolled up rugs 
(nylon type  and latex foam pads) that will be 
stored on 12 foot high racks along with boxes of 
water based adhesive and carpet tiles. The 
storage area has a 20 foot high ceiling with 
30” steel joists and masonry construction.  I 
was told that by an outside source that FM 
Global has design criteria for this type of material.
Problem is the water supply is 55 static and 45 
at 920 gpm residual. and 1808 gpm  at 20 psi 
(this was projected by the water provider.).


I am questioning whether this is enough water 
for this type of hazard. Any thoughts?


David Bryan
fpii
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www.fpdc.com
860.535.2080  
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Re: Water supply question

2008-07-09 Thread Todd Williams - FPDC

Sounds like tank time (at least for the sprinkler)



At 11:17 AM 7/9/2008, you wrote:
Thanks! We will have a pump but...the water 
supply (gpm) seems too low for the demand 
especially factoring in hose allowance.


David Bryan
fpii
-Original Message-
From: Todd Williams - FPDC [EMAIL PROTECTED]
To: sprinklerforum@firesprinkler.org
Sent: Wed, 9 Jul 2008 10:55 am
Subject: Re: Water supply question


Without doing any engineering and no other 
information, I would say probably not. According 
to A.5.6.3, cartoned carpet tiles are a Group A 
plastic. The latex foam pads are another bundle 
of joy. 55psi may not be enough to handle the 
demand. More engineering is needed on this 
project to make an actual determination. 
(Disclaimer: my opinion only and may not have any basis in fact)Â

Â
Â
At 10:10 AM 7/9/2008, you wrote:Â
Â
I am looking at a 25,000 sq foot 
former manufacturing facility that is being 
renovated and a wet system is being 
provided. A storage area- 4700 sq ft. will 
contain rolled up rugs (nylon type  and 
latex foam pads) that will be stored on 12 
foot high racks along with boxes of water 
based adhesive and carpet tiles. The storage 
area has a 20 foot high ceiling with 30â€Â 
steel joists and masonry constructioon. 
I was told that by an outside source that 
FM Global has design criteria for this type of material.Â
Problem is the water supply is 55 static and 
45 at 920 gpm residual. and 1808 gpm  at 20 
psi (this was projected by the water provider.).Â

Â
I am questioning whether this is enough 
water for this type of hazard. Any thoughts?Â

Â
David BryanÂ
fpiiÂ
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Â
Todd G. Williams, PEÂ
Fire Protection Design/ConsultingÂ
Stonington, ConnecticutÂ
www.fpdc.comÂ
860.535.2080 ___Â
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Â
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Todd G. Williams, PE
Fire Protection Design/Consulting
Stonington, Connecticut
www.fpdc.com
860.535.2080  
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Re: Pressure reducing valve location for a fire pump

2008-07-09 Thread Todd Williams - FPDC
If this location has an HPR carrier (i.e. FM Global, etc.), you had 
better check with them. They may dictate what you can and cannot do. 
Ran into this with an FM job with an oversized pump.




At 12:07 PM 7/9/2008, you wrote:

I have to install a pressure reducing valve on the discharge side of
the fire pump.  I know from past discussions that if standpipes are
present, the valve must be installed after the last control valve for
the fire pump to satisfy NFPA 14.  What if this is a large warehouse
falling strictly under 13?  Could it be placed between the pump
discharge and check valve (just like pressure relief valve on a diesel
FP) and sized per minimum relief valve in 2-20 (NFPA 20 99ed)?  I have a
2000gpm pump with a 8 discharge flange and would like to get a 8
pressure reducing valve to work instead of a 10in (size required for
discharge pipe) to save some money.  I checked the spec sheets and the
8 valve can handle the flow at 150%.

Thanks,
Dewayne
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Todd G. Williams, PE
Fire Protection Design/Consulting
Stonington, Connecticut
www.fpdc.com
860.535.2080  
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Re: Drawing Details

2008-07-03 Thread Todd Williams - FPDC

Anything specific you are looking for?

At 02:10 PM 7/3/2008, you wrote:

Hello sprinklerforum,

  I am looking for a good source of details in .DWG format to use in design
  drawings. I would like to find details like provided in many of the NFPA
  books but they will not release them. Any and All leads and links will be
  perused. Thanks

--
Best regards,
 Charles Thurston  mailto:[EMAIL PROTECTED]
  Coastal Fire Protection

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Todd G. Williams, PE
Fire Protection Design/Consulting
Stonington, Connecticut
www.fpdc.com
860.535.2080  
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Re: Stolen fire sprinkler parts - again

2008-07-01 Thread Todd Williams - FPDC
What part could you steal off a sprinkler system that would render it 
useless without either shutting off a valve (activate tamper switch) 
or get somebody wet (and set off the flow alarm)? Another inside job?


I have maintained for a long time that this business is ripe for 
sleeze-balls (I worked for one of the classics) because you get paid 
big bucks to install something that most likely will never operate. 
This puts a big burden on the local AHJs and those doing the NFPA 25 
inspections to make sure that this is done right and stays that way.




At 10:44 PM 6/30/2008, you wrote:

Here we go again.  Another report of fire sprinkler parts being stolen off
an active system.  This time the system was protecting the Lehigh Valley
Hospital in Allentown, PA.

The story was reported at
http://www.mcall.com/news/local/all-lvhgarages0630-cn,0,1033688.story


Ryan J. Smith

ResidentialFireSprinklers.com - Your Source for Home Fire Protection
http://www.ResidentialFireSprinklers.com



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www.fpdc.com
860.535.2080  
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LS pumps and transfer switches

2008-07-01 Thread Todd Williams - FPDC
I am working on a project (group home - non ambulatory) with a 
limited service fire pump taking suction from a tank. Main power is 
from the public utility and there is a back-up generator. The 
generator is hooked up through a standard transfer switch, which I am 
not sure is listed for use with a fire pump. The generator is sized 
to run the fire pump and emergency lighting only. The switch is 
satisfactorily sized, the system tested fine and the AHJ has signed 
off on it. Is there a problem? If this was a normal fire pump, I 
would say yes, but being limited service, I'm not sure. I know that 
the pumps can only be used when specifically approved by the AHJ, but 
don't know if they can accept a non-standard arrangement.


Todd G. Williams, PE
Fire Protection Design/Consulting
Stonington, Connecticut
www.fpdc.com
860.535.2080  
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Flexhead on CPVC

2008-06-27 Thread Todd Williams - FPDC
I'm working on a project where the client wants to use flexheads (or 
one of the clones) off CPVC pipe. Is there any restriction on this? 
Could the bending of the flexhead potentially put some weird forces 
on the CPVC pipe and glued fittings that could cause a problem? They 
claim they do it all of the time, but I've never seen it.


Todd G. Williams, PE
Fire Protection Design/Consulting
Stonington, Connecticut
www.fpdc.com
860.535.2080  
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noncombustible insulation

2008-06-24 Thread Todd Williams - FPDC
Is there criteria or a definition for noncombustible insulation? A 
client wants to fill a space with insulation in lieu of sprinklering 
it (good idea). However, the question comes up as to what constitutes 
noncombustible insulation. Would fiberglass batt qualify?


Todd G. Williams, PE
Fire Protection Design/Consulting
Stonington, Connecticut
www.fpdc.com
860.535.2080  
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Re: Sand or silt clogging strainers

2008-06-24 Thread Todd Williams - FPDC

Would the local fire department be any help in getting this thing flushed?


At 10:18 AM 6/24/2008, you wrote:

We have 1500 gpm diesel pump equipped with a PLD. While running at full
flow the strainers to the PLD and in the cooling line become clogged
with sand or fine silt causing the engine to over heat and the PLD to
fail. The city pressure and volume is not sufficient to adequately flush
the 16 dead end main coming to the site so we have to live with the
contaminated water for the time being. We are going to install a
strainer in the suction to the pump but that will only catch rocks and
stuff not the sand and silt.

The problem is how to flush or prevent the strainers from clogging
during a pump run. I have heard of cyclonic generator as a possible
solution but have not been able to find and information on one.

We are looking for ideas, suggestions or proven solutions if there are
any.

Thanks for your help.

Ron Fletcher
Aero Automatic
Phoenix, AZ
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www.fpdc.com
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Re: worried about Sprinklers leakage

2008-06-23 Thread Todd Williams - FPDC

Jaber,

If they are really concerned, look into a double-interlock pre-action 
system. That would be about the best way to bring the chance of 
accidental discharge to a minimum. Considering you e-mail address, 
should I assume this is outside the United States? What do the local 
codes say about replacing sprinklers with a chemical agent?



At 08:44 AM 6/23/2008, you wrote:
Newly constructed research and development lab facility is protected 
by a wet type sprinkler system, one of the lab scientist is worried 
about the accidental release of the automatic sprinkler  heads on 
top  or  in the  vicinity of the high tech., expensive analytical 
instruments such as NMR, FTMS, autospec GC/MS and ESEM , which 
present a potential risk of damage to these instruments in case 
these sprinklers kick off during actual emergency or broken by 
mistake by a maintenance personnel or a lab personnel.  He suggests 
gas suppression instead. I explained to him that accidental leakage 
of wet type sprinkler system is very minimal. The question is what 
the probability of activation and how much will it cost to replace 
the existing system with a gas suppression system.  Your 
recommendations/insights are highly appreciated.

Jaber Al-Haji
[EMAIL PROTECTED]
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www.fpdc.com
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Re: PLay areas

2008-06-23 Thread Todd Williams - FPDC

Greg,

I did a play space about a year ago. The existing system was design 
to OH2 and that seemed consistent with what was going to be put in. 
There was plastic, but very little concentration or continuity. The 
standard obstruction rules apply. Your swiss cheese decks should be 
treated like any grated floor. If they start putting the injection 
moulded stuff in there, that changes everything.



At 12:05 PM 6/23/2008, you wrote:

OK, I have experienced the inflatable Bounce structures and read the
previous post's concerning the same. However; what about the open type
playground structure made out of metal with Poly netting and foam insulation
around the posts to protect the kids noggins? All of the decks are steel
with holes to like swiss cheese so water could penetrate the structure all
the way down to the floor. I do not believe there is a roof over this
structure either.

I guess this is similar to what the old McDonalds playgrounds were like.

I am thinking a max of OH2 would be fine and the engineer doesn't know. Any
ideas?

Thank you,
Greg McGahan

Living Water Fire Protection, LLC
1160 McKenzie Road
Cantonment, FL 32533
850-937-1850
Fax: 850-937-1852



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