The experiment you describe fixes the partial pressures of the gases and
EQUILIBRIUM_PHASES is the right keyword data block to use.
The reason you are having numerical problems is related to the introduction
of N2 and O2. PHREEQC calculates redox equilibrium in reaction calculations
and thermodynamically, N2 and O2 should react to form NO3. Fixing partial
pressures of N2 and O2 generates huge amounts of NO3, and the program fails
to converge. If you assume the N2 is essentially inert, the following input
file will make the calculation without allowing N2 to react to NO3, by
defining a new "element" Ngas, which has only one aqueous species, Ngas2
and the gas component Ngas.
David
SOLUTION_MASTER_SPECIES
Ngas Ngas2 0 Ngas2 14
SOLUTION_SPECIES
Ngas2 = Ngas2
LogK 0.0
PHASES
Ngas
Ngas2 = Ngas2
log_k -3.260
delta_h -1.358 kcal
SOLUTION
units mg/l
U 1
EQUILIBRIUM_PHASES 1
CO2(g) -3.5
O2(g) -0.69897
Ngas -0.1079
REACTION
NaOH 1
0 .0000001 .000001 .00001 .0001 .001 .01 .1 1 mol
David Parkhurst (dlpark@xxxxxxxx)
U.S. Geological Survey
Box 25046, MS 413
Denver Federal Center
Denver, CO 80225
Project web page: https://wwwbrr.cr.usgs.gov/projects/GWC_coupled
"Yong Wang"
<ywang2@xxxxxxxx To: "David L Parkhurst" <dlpark@xxxxxxxx>
on.edu> cc:
In-Reply-To: <FOEMLCJFIJMKLGPCIDHCCEAKCAAA.ywang2@xxxxxxxxxxxxxx>
Subject: diolution of Air composition
08/02/02 12:08
PM
Mr. Parkhurst:
Hi, how are you !
I am very appreciated of your help on my question last time . I don't know
if you had time to think over the question on caron dioxide. I remembered
that you said you were out of town for two weeks. I sent a email to you
then
and i am not sure if you got it.
So I here sum it up in this way:
I am trying to simulate the disolution of the gas composition of air in
solution which is bubbled with a humidified air in lab experimental
condition. The concentration of carbonate is unknown.
I tried to set the initial data in
GAS_PHASE 1 Air
-fixed_pressure
-pressure 1.0
-temperature 25.0
CO2(g) 0.000316
O2(g) 0.2
N2(g) 0.78
as well as
EQUILIBRIUM_PHASES 1
Fix_H+ -8.0 NaOH 10.0
CO2(g) -3.5
O2(g) -0.69897
N2(g) -0.1079
The pH are set as fixed from 2-10.
There are 1 mg/l U in the soultion and adsortion by iron oxide are allowed
too.
The first one comes out with the carbonate distribution as shown in
attached
file while the second one doesn't converge. I tried the KNOBS data but
didn't work. Butwhen I took away the O2(g) and N2(g) from the data set, it
gave a fairly good result.
Here is my questions:
1. which one data set should i use to represent the experimental condition
?
2. I used the Fixed_H+ for constant pH. In order to keep the acid-base and
calculation balance, I need to assumed some acid or base present as Manual
recommended. Don't they influence the chemical reaction, such as to
increase or decrease the dissolution of CO2 ? how to avoid using the
assumed
acid or base ? Any advices if necessary?
Thanks a lot for your precious time and help.
Yours sincerely,
Young Wang
Department of Geology
SUNY-Binghamton
(See attached file: question.doc)
Attachment:
question.doc
Description: MS-Word document
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