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CO2 solubility in water
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7/18/2019 CO2 SoluBility
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CARBON IN LAKES
I. The CO2 carbonate system
A. Sources and Sinks o CO2
!" Sources
a" atmos#here $ %%% ##m b" res#iration
c" combustion
i. natura&
ii industria&
d" so&ution
2" Sinks
a" #hotosynthesis
b" biomass
c" sedimentation ' #reci#itation
B. So&ubi&ity in the CO2 system
!" CO2 ( $!)2" So&ution *ure +ater , #- ./ 0 -enry1s &a+ , 2/oC % mmo& &0!
3!45 m(&0!6
C. Chemistry o CO2
!" -ydration o CO2 (
CO2 7 -2O -2CO%
-2CO% -CO%0 7 -7
-CO% CO%8 7 -7
2" re&ations +ith #-
-i(h #- CO%8 dominates
9id ran(e #- -CO%
0
dominatesLo+ #- -2CO% :CO2; dominates
%" Eects o Ca&cium <and 9a(nesium"
Ca<-CO%"2 CaCO% 7 CO2 7 -2O
Buerin( ca#acity
A&ka&inity
II. Bio&o(ica& =actors in&uencin( Carbon in &akes
A. *hotosynthesis
!" *hotosynthesis and #-
2" Carbon &imitationB. Res#iration
!" Res#iration and #-
2" BO>
C. Or(anic Carbon
!" Losses
2" Sinks
!
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Carbon dioxide in water equilibrium
1. Introduction
Carbon dioxide does dissolve in water, however the system is somewhat complex [1].
First the CO2 dissolves according to:
1! CO2 g! CO2 l!
"t room temperat#re, the sol#bility o$ carbon dioxide is abo#t %& cm' o$ CO2 per 1&& ml watercl(cg ) &.*!.
"ny water+sol#ble gas becomes more sol#ble as the temperat#re decreases, d#e to the
thermodynamics o$ the reaction: "- l! "- g!. he entropy change, ∆-, o$ this reaction
is positive beca#se the gas molec#les are less constrained than the gas molec#les in
sol#tion. he change in Free energy o$ reaction with an increase in temperat#re is +/∆-. his
e$$ect is partic#larly large $or gases li0e CO2 that #ndergo speci$ic reactions with water.
#ilibri#m is established between the dissolved CO2 and 32CO', carbonic acid.
2! CO2 l! 4 32O l! 32CO' l!
his reaction is 0inetically slow. "t e#ilibri#m, only a small $raction ca. &.2 + 15! o$ thedissolved CO2 is act#ally converted to 32CO'. 6ost o$ the CO2 remains as solvated molec#larCO2. "s e#ation:
[ ]
[ ]%
2
%2 !/..! −≈=l
r
CO
CO H K
7n $act, the p8a most reported $or carbonic acid p8a1 ) 9.'! is not really the tr#e p8a o$carbonic acid. ;ather, it is the p8a o$ the e#ilibri#m mixt#re o$ CO2 l! and carbonic acid.Carbonic acid is act#ally a m#ch stronger acid than this, with a tr#e p8a1 val#e o$ '.<*.3owever these val#es are also temperat#re dependent.
Carbonic acid is a wea0 acid that dissociates in two steps[2].
'! 32CO' 4 32O 3'O4 4 3CO'
+ p8a1 2< =C! ) 9.'
>! 3CO'
+ 4 32O 3'O4 4 CO'
2+ p8a2 2< =C! ) 1&.2<
?ote that these carbonate anions can interact with the cations present in the water to $orminsol#ble carbonates. For instance, i$ Ca24 is present limestone, CaCO' is $ormed and i$ 6g24
is present 6gCO' is $ormed. he $ormation o$ these deposits is an additional driving $orce thatcan p#ll the e#ilibri#m more to the right res#lting in acidi$ication o$ the water [2].
<! Ca24 4 CO'2+ CaCO' - ) >.%9 x 1&+% - ) sol#bility constant!
9! 6g24 4 CO'
2+ 6gCO' - ) 9.*2 x 1&+9
he above presented more schematically:
4 32O 4 32O 4 32O 4 Ca24
CO2g! CO2 l! 32CO' 3CO'+
CO'2+
CaCO'
4 3'O4 4 3'O
4
?ote that the reverse is also tr#e and that the scheme represents the sol#bility o$ CaCO' in anacidic sol#tion res#lting in the liberation o$ CO2 in the atmosphere.
2
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2. Deriving [H2CO3]
7$ we ass#me CO2 is a simple gas we can apply 3enry@s law that describes the e#ilibri#mbetween vapor and li#id. h#s:
pCO2 ) 8 . xCO2
where pCO2 is the partial press#re o$ the gas in the b#l0 atmosphere Aa!, 8 is a constant Aa!and xCO2 is the e#ilibri#m mole $raction o$ sol#te in li#id phase.
he sol#bility o$ CO2 is temperat#re dependent, as shown in able 1: -ol#bility o$ CO2 at apartial press#re $or CO2 o$ 1 bar abs ['] .
Table 1: Solubility of CO2 at a partial pressure for CO2 of 1 bar abs[3].
emperat#re oC! & 1& 2& '& >& <& *& 1&&
-ol#bilitycm' CO2(g water!
1.* 1.' &.** &.9< &.<2 &.>' &.2% &.29
F#rthermore, as stated above, CO2 reacts with the water on dissol#tion and there$ore onewo#ld expect that 3enry@s law has to be modi$ied.
3owever, according to Carrol and 6ather [>] a $orm o$ 3enry@s law can be #sed $or modelingthe sol#bility o$ carbon dioxide in water $or press#res #p to abo#t 1&& 6Aa, as can be seen inFig#re 1: 3enryBs Constant $or Carbon ioxide in Dater + $rom Carroll et al. [>] .
Figure 1: Henry's Constant for Carbon Dioi!e in "ater # fro$ Carroll et al. [%]
%
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hey concl#de that the 8richevs0y+8asarnovs0y #ation, which can be derived $rom 3enry@sEaw, can be #sed to model the system CO2+32O at temperat#res below 1&& oC.
h#s in the range o$ interest, 2&+'< =C, the 3enry coe$$icient $or CO2 in water goes $rom 1<& +2&& 6Aa(mole $raction
"pplying the above to the conditions #nder investigation:emperat#re range: 2& '< =CAress#re range: *& %& bar CO2 concentration in gas phase: 1.'+1. mol5
he partial press#re o$ CO2 in the gas phase is there$ore in the range:1.'(1&& G *& G &.1 ) &.1&> 6Aa1.(1&& G %& G &.1 ) &.1<' 6Aa
"pplying 3enry@s Eaw we calc#late a CO2 mole $raction in water in the range:xlow ) &.1&> ( 2&& ) &.&&&<2xhigh ) &.1<' ( 1<& ) &.&&1&2
Converting mole $ractions to concentrations: "t 2& =C the molar density o$ water ) %%*.21(1*.&2 ) <<.'% mol(l "t '< =C the molar density o$ water ) %%>.'(1*.&2 ) <<.1* mol(l
h#s the CO2 concentration range in water #nder these conditions is:clow ) &.&&&<2 G <<.1* ) &.&2% mol(lchigh ) &.&&1&2 G <<.'% ) &.&<9 mol(l
3. Calculating the H[!]
he basic e#ations needed to calc#late the p3 are derived $rom e#ation '! and >!.
?ote: x ) [3'O4] and y ) [O3+]
he protolysis constants:
63
63
"63
63
63
63<
63
63
%
2
%2
2
%
%22
%
%2
%!
−
−
−−−
=
≈
+
≈=
HCO
CO x K
CO
HCO x
CO H CO
HCO x
CO H
HCO x K
a
l
a
"ss#ming the initial concentration o$ carbonic acid ) c then we derive the ste#chiometricrelation:
c ) [32CO'] 4 [3CO'+] 4 [CO'
2+] he water constant: x.y ) 8w and p8w )1>
he electro ne#trality e#ation:2[CO'
2+] 4 [3CO'+] 4 y ) x
De now have < e#ations and < #n0nowns.From the e#ilibri#m constants we derive
2
2
%
%6363
a K
CO x HCO
−− =
?
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and
2!
2
%
2
%2
6363
aa K K
CO xCO H
−
=
-#bstit#ting these into the ste#chiometric relation we derive:
2!!
2
!%
2!!
2
2!2
%
2!
2
2
2
%
2
%
2
2
%
2!
2
%
2
.
..63
.
.63
!63636363
aaa
a
aaa
aa
aaaaaa
K K x K x
c x K HCO
K K x K x
c K K CO
K K
x
K
xCOCO
K
CO x
K K
CO xc
++=
++=
⇒
++=++=
−
−
−−
−−
hese e#ations can be #sed to calc#late in which p3 area which CO 2 species dominates as
can be seen in Fig#re 2: p3 and CO2 species.
H"CO2 equilibra
&.&
&.1
&.2
&.'
&.>
&.<
&.9
&.
&.*
&.%
1.&
& 1 2 ' > < 9 * % 1& 11 12 1' 1>
H
c # m
o l " l $
[3CO'+]
[CO' 2+]
[32CO'])[CO2]l
Figure 2: pH an! CO2 spe&ies
-#bstit#ting these into the electro ne#trality e#ation:
x y K K x K x
x K K K c
x y K K x K x
c x K
K K x K x
c K K
aaa
aaa
aaa
a
aaa
aa
=+
++
+
⇒=+
++
+
++
2!!
2
!2!
2!!
2
!
2!!
2
2!
.
..2.
.
..
.
.2
Combining the above with 8w)x.y we derive a > th degree e#ation in x:
@
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x x
K
K K x K x
x K K K c w
aaa
aaa=+
++
+
2!!
2
!2!
.
..2.
Compare:
2!!
2
!2!
.
..2
aaa
aaa
K K x K x
x K K K
+++
with
2!2!
2
2!2!
2
2
!
!
..
...2
aaaa
aaaa
a
a
a
a
K K x K x K x
x K x K K K
x K
K
x K
K
+++
++⇒
+
+
+
7$ 8a1 HH 8a2 then 8a1.x HH 8a2.x and we can consider the e#ations e#al and derive $or theelectro ne#trality e#ation:
x x
K c x K
K c x K
K w
a
a
a
a =++
++ 2
2
!
!
stimating the di$$erence between 8a and x can help simpli$ying the e#ation even $#rther.
F#rthermore: p3 ) +log x.
"pplying the e#ations derived above to the CO2 concentrations calc#lated we calc#late byapplying that i$ 8a II x a valid approach i$ the p3 is ca. > we can write:
waawaa K c K c K x x
x
K c
x
K c
x
K ++=⇒=++ 2!
2! .
h#s with the CO2 concentration range in water calc#lated above we calc#late $or the p3range:
clow ) &.&2% mol(l p3 ) '.%<
chigh ) &.&<9 mol(l p3 ) '.*1
Jeri$ication has been done #sing the basic e#ation1 via a n#meric sol#tion in excelemploying the goal see0 $#nction. he same p3 val#es as derived above are $o#nd.
7t is possible to re$ine the res#lt even $#rther. he dissociation constant is also depending onthe temperat#re o$ the sol#tion.
Table 2: Disso&iation &onstant ( 1)* of &arboni& a&i! at +arious te$peratures[2].
emperat#re oC! & < 1& 1< 2& 2< '& '< >& >< <&
81".1& 2.9> '.&> '.>> '.*1 >.19 >.>< >.1 >.%& <.&> <.1' <.1%
! By transormin( the basic euation
( ) /2.
..2.
2!!
2
!2!2!
%
!
?
2!!
2
!2!
=−−−−−++
⇒=+
++
+
waawaaaawaaa
w
aaa
aaa
K K K x K K xc K c K K K K K x K x
x
x
K
K K x K x
x K K K c
4
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3owever, as can be seen in able 2: issociation constant 81"! o$ carbonic acid at vario#stemperat#res [2] ., the p8a1 does not change eno#gh to in$l#ence the p3 signi$icantly.
%. &''ect o' in(oluble carbonate( 'ormation #deo(it($ on H
Formation o$ scale! deposits will in$l#ence the p3 o$ sol#tion is an indicator $or a p3 above 9+. he sol#bility o$ CaCO' as a $#nction o$ the p3 can be described by:
"!<63663332!
2
2
22
%
2
aaa K K
x
K
xS CaCOCaS ++=⇒= +−+
"t lower p3@s the sol#bility o$ the carbonate increases signi$icantly as can be seen in Fig#re ':-ol#bility o$ CaCO' as a $#nction o$ p3.
)olubilit* o' CaCO3 a( a 'unction o' H
&
1&&&
2&&&
'&&&
>&&&
<&&&
9&&&
&&&
1 2 ' > < 9H
[ C a 2 + ] # m o l " l $
Figure 3: Solubility of CaCO3 as a fun&tion of pH
h#s the absence o$ scaling in combination with relatively high Ca24 and(or 6g24 concentrations can be an indicator $or a p3 o$ the water below 9.
!. Conclu(ion
"t the conditions #nder investigation, a press#re range o$ *&+%& bar, a temperat#re range o$2&'< =C and a CO2 gas phase concentration range o$ 1.'+1. mol5 the p3 o$ the water isca. >.
,. -e'erence(
[1] ;obert C. ;eid, Kohn 6. Ara#snitL, and Mrice . Aoling, The Properties of Gases &Liquids, > ed. Moston: 6craw+3ill, 1%*.
[2] avid ;. Eide, CRC Handbook of Chemistry and Physics, 1 ed. Moca ;aton, "nn "rbor, Moston: C;C Aress, 1%%&+1%%1.
['] Ahysical and ngineering ata, Kan#ary 1%* ed. he 3ag#e: -hell 7nternationaleAetrole#m 6aatschappiN MJ, 1%*.
[>] Kohn K. Carroll and "lan . 6ather, he -ystem Carbon ioxide+Dater and the8richevs0y+8asarnovs0y #ation, Ko#rnal o$ -ol#tion Chemistry, vol. 21, pp. 9&+921, 1%%2.