Hi Mark,

I had a quick look at the papers on your site.  If I understand correctly, 
you recover a gas stream with most of the CH4 at depth.  You want to 
recover the CO2 that remains in solution, so you pump it to the surface and 
collect the gas, which contains some residual CH4.  You then compress the 
mixture, liquefying the CO2 to separate it from the CH4.  What you'd like 
is a process that collects the CO2 in the first step.

The membrane process produces H+ and shifts the acid/base equilibria from 
HCO3- to dissolved CO2, which is much less water soluble.  Here's a plot of 
the equilibria (at 1 atm):

http://en.wikipedia.org/wiki/File:Carbonate_system_of_seawater.svg

At seawater pH most of the CO2 is present as HCO3- and CO3--.  If you drop 
the pH to about 4, most is present as molecular CO2.

If you acidified the output of the digester by running it through a 
membrane acidifier I'm pretty sure you'd improve the initial take-off of 
CO2.  But I don't know by how much.  It depends on how CO2 solubility and 
the acid-base equilibria change with pressure, and what the phase diagram 
of CO2/seawater looks like at pressure.  In the paper by the PARC 
researchers they used a vacuum pump to pull off the CO2.  I don't know if 
the CO2 would just come out of solution at the concentration/pH/T/P 
condition that prevails in your digester.

You should also consider the cost of energy for the process - PARC measured 
242 kJ/mol CO2 recovered.

Forgive me if I've misunderstood your process, I've only had a quick look,

cheers,
john

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