MondayTuesday Thermodynamics of aqueous solutions Ion association Pitzer

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Monday-Tuesday • Thermodynamics of aqueous solutions – Ion association – Pitzer – SIT •

Monday-Tuesday • Thermodynamics of aqueous solutions – Ion association – Pitzer – SIT • SOLUTION – – – Units p. H—ratio of HCO 3 -/CO 2 pe—ratio of oxidized/reduced valence states Charge balance Phase boundaries • Saturation indices – Uncertainties – Useful minerals • Identify potential reactants 1

PHREEQC Programs • PHREEQC Version 3 – PHREEQC: Batch with Charting – Phreeqc. I:

PHREEQC Programs • PHREEQC Version 3 – PHREEQC: Batch with Charting – Phreeqc. I: GUI with Charting – IPhreeqc: Module for programming and scripting • PHAST – – Serial—soon to be Multithreaded Parallel—MPI for transport and chemistry TVD (not done) 4 Windows—GUI just accepted • WEBMOD-Watershed reactive transport 2

Solutions 3

Solutions 3

Solution Definition and Speciation Calculations SO 4 Ca Na Mg Cl Fe HCO 3

Solution Definition and Speciation Calculations SO 4 Ca Na Mg Cl Fe HCO 3 Inverse Modeling Saturation Indices Speciation calculation Reactions Transport 4

SOLUTION: Seawater, ppm Constituent p. H pe Temperature Ca Mg Na K Fe Alkalinity

SOLUTION: Seawater, ppm Constituent p. H pe Temperature Ca Mg Na K Fe Alkalinity as HCO 3 Cl SO 4 Value 8. 22 8. 45 10 412. 3 1291. 8 10768 399. 1. 002 141. 682 19353 2712 5

Periodic_table. bmp 6

Periodic_table. bmp 6

Initial Solution 1. Questions 1. What is the approximate molality of Ca? 2. What

Initial Solution 1. Questions 1. What is the approximate molality of Ca? 2. What is the approximate alkalinity in meq/kgw? 3. What is the alkalinity concentration in mg/kgs as Ca. CO 3? 4. What effect does density have on the calculated molality? PHREEQC results are always moles or molality 7

Initial Solution 1. For most waters, we can assume most of the mass in

Initial Solution 1. For most waters, we can assume most of the mass in solution is water. Mass of water in 1 kg seawater ~ 1 kg. 1. 412/40 ~ 10 mmol/kgw ~ 0. 01 molal 2. 142/61 ~ 2. 3 meq/kgw ~ 0. 0023 molal 3. 2. 3*50 ~ 116 mg/kgw as Ca. CO 3 4. None, density will only be used when concentration is specified as per liter. 8

Default Gram Formula Mass Element/Redox State Default “as” phreeqc. dat/wateq 4 f. dat Alkalinity

Default Gram Formula Mass Element/Redox State Default “as” phreeqc. dat/wateq 4 f. dat Alkalinity Ca. CO 3 C, C(4) HCO 3 CH 4 NO 3 - N NH 4+ N PO 4 P Si Si. O 2 SO 4 Default GFW is defined in 4 th field of SOLUTION_MASTER_SPECIES in database file. 9

Databases • Ion association approach – – – – Phreeqc. dat—simplest (subset of Wateq

Databases • Ion association approach – – – – Phreeqc. dat—simplest (subset of Wateq 4 f. dat) Amm. dat—same as phreeqc. dat, NH 3 is separated from N Wateq 4 f. dat—more trace elements Minteq. dat—translated from minteq v 2 Minteq. v 4. dat—translated from minteq v 4 Llnl. dat—most complete set of elements, temperature dependence Iso. dat—(in development) thermodynamics of isotopes • Pitzer specific interaction approach – Pitzer. dat—Specific interaction model (many parameters) • SIT specific interaction theory – Sit. dat—Simplified specific interaction model (1 parameter) 10

PHREEQC Databases Other data blocks related to speciation SOLUTION_MASTER_SPECIES—Redox states and gram formula mass

PHREEQC Databases Other data blocks related to speciation SOLUTION_MASTER_SPECIES—Redox states and gram formula mass SOLUTION_SPECIES—Reaction and log K PHASES—Reaction and log K 11

Solutions • Required for all PHREEQC calculations • SOLUTION and SOLUTION _SPREAD – –

Solutions • Required for all PHREEQC calculations • SOLUTION and SOLUTION _SPREAD – – – Units p. H pe Charge balance Phase boundaries • Saturation indices – Useful minerals – Identify potential reactants 12

What is a speciation calculation? • Input: – p. H – pe – Concentrations

What is a speciation calculation? • Input: – p. H – pe – Concentrations • Equations: – Mass-balance—sum of the calcium species = total calcium – Mass-action—activities of products divided by reactants = constant – Activity coefficients—function of ionic strength • Output – Molalities, activities – Saturation indices 13

Mass-Balance Equations Analyzed concentration of sulfate = (SO 4 -2) + (Mg. SO 40)

Mass-Balance Equations Analyzed concentration of sulfate = (SO 4 -2) + (Mg. SO 40) + (Na. SO 4 -) + (Ca. SO 40) + (KSO 4 -) + (HSO 4 -) + (Ca. HSO 4+) + (Fe(SO 4)2 -) + (Fe. HSO 4+2) () indicates molality 14

Mass-Action Equations Ca+2 + SO 4 -2 = Ca. SO 40 [] indicates activity

Mass-Action Equations Ca+2 + SO 4 -2 = Ca. SO 40 [] indicates activity 15

Activity WATEQ activity coefficient Davies activity coefficient 16

Activity WATEQ activity coefficient Davies activity coefficient 16

Uncharged Species bi, called the Setschenow coefficient Value of 0. 1 used in phreeqc.

Uncharged Species bi, called the Setschenow coefficient Value of 0. 1 used in phreeqc. dat, wateq 4 f. dat. 17

Pitzer Activity Coefficients ma concentration of anion mc concentration of cation Ion specific parameters

Pitzer Activity Coefficients ma concentration of anion mc concentration of cation Ion specific parameters F function of ionic strength, molalities of cations and anions 18

SIT Activity Coefficients mk concentrations of ion Interaction parameter A = 0. 51, B

SIT Activity Coefficients mk concentrations of ion Interaction parameter A = 0. 51, B = 1. 5 at 25 C 19

Aqueous Models Ion association – Pros • Data for most elements (Al, Si) •

Aqueous Models Ion association – Pros • Data for most elements (Al, Si) • Redox – Cons • • Ionic strength < 1 Best only in Na, Cl medium Inconsistent thermodynamic data Temperature dependence 20

Aqueous Models • Pitzer specific interaction – Pros • High ionic strength • Thermodynamic

Aqueous Models • Pitzer specific interaction – Pros • High ionic strength • Thermodynamic consistency for mixtures of electrolytes – Cons • • Limited elements Little if any redox Difficult to add elements Temperature dependence 21

Aqueous Models • SIT – Pros • Possibly better for higher ionic strength than

Aqueous Models • SIT – Pros • Possibly better for higher ionic strength than ion association • Many fewer parameters • Redox • Actinides – Cons • Poor results for gypsum/Na. Cl in my limited testing • Temperature dependence • Consistency? 22

Phreeqc. I: SOLUTION Data Block 23

Phreeqc. I: SOLUTION Data Block 23

Number, p. H, pe, Temperature 24

Number, p. H, pe, Temperature 24

Solution Composition Set units! Default is mmol/kgw Select elements Set concentrations “As”, special units

Solution Composition Set units! Default is mmol/kgw Select elements Set concentrations “As”, special units Click when done 25

Run Speciation Calculation Run Select files 26

Run Speciation Calculation Run Select files 26

Seawater Exercise A. Use phreeqc. dat to run a speciation calculation for file seawater.

Seawater Exercise A. Use phreeqc. dat to run a speciation calculation for file seawater. pqi B. Use file seawaterpitzer. pqi or copy input to a new buffer • • Ctrl-a (select all) Ctrl-c (copy) File->new or ctrl-n (new input file) Ctrl-v (paste) Units are ppm Constituent p. H p. E Temperature Ca Mg Na K Fe Alkalinity as HCO 3 Cl SO 4 Value 8. 22 8. 45 10 412. 3 1291. 8 10768 399. 1. 002 141. 682 19353 2712 27

Ion Association Model Results 28

Ion Association Model Results 28

Results of 2 Speciation Calculations Tile Ion Association Pitzer 29

Results of 2 Speciation Calculations Tile Ion Association Pitzer 29

Questions 1. Write the mass-balance equation for calcium in seawater for each database. 2.

Questions 1. Write the mass-balance equation for calcium in seawater for each database. 2. What fraction of the total is Ca+2 ion for each database? 3. What fraction of the total is Fe+3 ion for each database? 4. What are the log activity and log activity coefficient of CO 3 -2 for each database? 5. What is the saturation index of calcite for each database? 30

Initial Solution 2. Answers () indicates molality 1 a. Ca(total)= 1. 066 e-2 =

Initial Solution 2. Answers () indicates molality 1 a. Ca(total)= 1. 066 e-2 = (Ca+2) + (Ca. SO 4) + (Ca. HCO 3+) + (Ca. CO 3) + (Ca. OH+) + (Ca. HSO 4+) 1 b. Ca(total) = 1. 066 e-2 = (Ca+2) + (Ca. CO 3) 2 a. 9. 5/10. 7 ~ 0. 95 2 b. 1. 063/1. 066 ~ 1. 0 3 a. 3. 509 e-019 / 3. 711 e-008 ~ 1 e-11 3 b. No Fe+3 ion. 4 a. log activity CO 3 -2 = -5. 099; log gamma CO 3 -2 = -0. 68 4 b. log activity CO 3 -2 = -5. 091; log gamma CO 3 -2 = -1. 09 5 a. SI(calcite) = 0. 76 5 b. SI(calcite) = 0. 70 31

SATURATION INDEX The thermodynamic state of a mineral relative to a solution IAP is

SATURATION INDEX The thermodynamic state of a mineral relative to a solution IAP is ion activity product K is equilibrium constant 32

SATURATION INDEX SI < 0, Mineral should dissolve SI > 0, Mineral should precipitate

SATURATION INDEX SI < 0, Mineral should dissolve SI > 0, Mineral should precipitate SI ~ 0, Mineral reacts fast enough to maintain equilibrium Maybe – Kinetics – Uncertainties 33

Rules for Saturation Indices • Mineral cannot dissolve if it is not present •

Rules for Saturation Indices • Mineral cannot dissolve if it is not present • If SI < 0 and mineral is present—the mineral could dissolve, but not precipitate • If SI > 0—the mineral could precipitate, but not dissolve • If SI ~ 0—the mineral could dissolve or precipitate to maintain equilibrium 34

Saturation Indices • SI(Calcite) • SI(CO 2(g)) = log(PCO 2) 35

Saturation Indices • SI(Calcite) • SI(CO 2(g)) = log(PCO 2) 35

Useful Mineral List Minerals that may react to equilibrium relatively quickly 36

Useful Mineral List Minerals that may react to equilibrium relatively quickly 36

PHREEQC: Reactions in a Beaker SOLUTION MIX + REACTION_TEMPERATURE SOLUTION EXCHANGE SURFACE REACTION BEAKER

PHREEQC: Reactions in a Beaker SOLUTION MIX + REACTION_TEMPERATURE SOLUTION EXCHANGE SURFACE REACTION BEAKER EQUILIBRIUM_ PHASES EQUILIBRIUM _PHASES EXCHANGE SURFACE KINETICS GAS_PHASE REACTION_PRESSURE GAS_PHASE 37

 • Files (double click to edit) Data Tree – Simulation (END) • Keywords

• Files (double click to edit) Data Tree – Simulation (END) • Keywords (double click to edit) – Data 38

Edit Screen • Text editor 39

Edit Screen • Text editor 39

Tree Selection • • • Input Output Database Errors Pf. W 40

Tree Selection • • • Input Output Database Errors Pf. W 40

Keyword Data Blocks Also right click in data tree—Insert keyword 41

Keyword Data Blocks Also right click in data tree—Insert keyword 41

Pf. W Style 42

Pf. W Style 42

Total Inorganic Carbon • Number of moles of carbon of valence 4 Alkalinity •

Total Inorganic Carbon • Number of moles of carbon of valence 4 Alkalinity • Approximately HCO 3 - + 2 x. CO 3 -2 + OH- - H+ • Alkalinity is independent of PCO 2 43

SOLUTION_SPREAD 44

SOLUTION_SPREAD 44

Carbon and Alkalinity solution_spread. pqi SOLUTION_SPREAD SELECTED_OUTPUT USER_GRAPH 45

Carbon and Alkalinity solution_spread. pqi SOLUTION_SPREAD SELECTED_OUTPUT USER_GRAPH 45

Carbon Speciation and Alkalinity 46

Carbon Speciation and Alkalinity 46

p. H and pe Keywords SOLUTION—Solution composition END—End of a simulation USE—Reactant to add

p. H and pe Keywords SOLUTION—Solution composition END—End of a simulation USE—Reactant to add to beaker REACTION—Specified moles of a reaction USER_GRAPH—Charting 47

SOLUTION, mmol/kgw Constituent p. H pe Temperature Alkalinity Na Value 7 4 25 1

SOLUTION, mmol/kgw Constituent p. H pe Temperature Alkalinity Na Value 7 4 25 1 1 charge END 48

USE Solution 1 REACTION CO 2 1. 0 1, 100, 1000 mmol USER_GRAPH -axis_titles

USE Solution 1 REACTION CO 2 1. 0 1, 100, 1000 mmol USER_GRAPH -axis_titles "CO 2 Added, mmol" "p. H" "Alkalinity" -axis_scale x_axis auto log -axis_scale sy_axis 0 0. 002 -start 10 GRAPH_X rxn 20 GRAPH_Y -LA("H+") 30 GRAPH_SY ALK -end 49

Input file p. H. pqi SOLUTION 1 temp 25 p. H 7 pe 4

Input file p. H. pqi SOLUTION 1 temp 25 p. H 7 pe 4 redox pe units mmol/kgw density 1 Alkalinity 1 Na 1 charge -water 1 # kg END USE solution 1 REACTION 1 CO 2 1 1 10 1000 millimoles USER_GRAPH 1 -axis_titles "CO 2 Added, mmol" "p. H" "Alkalinity" -axis_scale x_axis auto log -axis_scale sy_axis 0 0. 002 -start 10 GRAPH_X rxn 20 GRAPH_Y -LA("H+") 30 GRAPH_SY ALK -end END 50

p. H is the ratio of HCO 3 - to CO 2(aq) Alkalinity is

p. H is the ratio of HCO 3 - to CO 2(aq) Alkalinity is independent of PCO 2 51

What is p. H? p. H = 6. 3 + log[(HCO 3 -)/(CO 2)]

What is p. H? p. H = 6. 3 + log[(HCO 3 -)/(CO 2)] p. H = 10. 3 + log[(CO 3 -2)/(HCO 3 -)] p. H = log. K + log[(PO 4 -3)/(HPO 4 -2)] Questions 1. How does the p. H change when CO 2 degasses during an alkalinity titration? 2. How does p. H change when plankton respire CO 2? 3. How does p. H change when calcite dissolves? 52

SOLUTION, mmol/kgw Constituent p. H pe Temperature Fe(3) Cl Value 2 4 25 1

SOLUTION, mmol/kgw Constituent p. H pe Temperature Fe(3) Cl Value 2 4 25 1 1 charge END 53

USE Solution 1 REACTION Fe. Cl 2 1. 0 1, 100, 1000 mmol USER_GRAPH

USE Solution 1 REACTION Fe. Cl 2 1. 0 1, 100, 1000 mmol USER_GRAPH -axis_titles "Fe. Cl 2 Added, mmol" "pe" "" -axis_scale x_axis auto log -start 10 GRAPH_X rxn 20 GRAPH_Y -LA("e-") -end 54

Input file SOLUTION 1 temp 25 p. H 3 pe 4 redox pe units

Input file SOLUTION 1 temp 25 p. H 3 pe 4 redox pe units mmol/kgw density 1 Cl 1 charge Fe(3) 1 -water 1 # kg END USE solution 1 REACTION 1 Fe. Cl 2 1 1 10 1000 millimoles USER_GRAPH 1 -axis_titles "Fe. Cl 2 Added, mmol" "pe" "" -axis_scale x_axis auto log -start 10 GRAPH_X rxn 20 GRAPH_Y -LA("e-") -end END 55

pe 56

pe 56

What is pe? Fe+2 = Fe+3 + epe = log( [Fe+3]/[Fe+2] ) + 13

What is pe? Fe+2 = Fe+3 + epe = log( [Fe+3]/[Fe+2] ) + 13 HS- + 4 H 2 O = SO 4 -2 + 9 H+ + 8 epe = log( [SO 4 -2]/[HS-] ) – 9/8 p. H + 4. 21 N 2 + 6 H 2 O = 2 NO 3 - + 12 H+ + 10 epe = 0. 1 log( [NO 3 -]2/[N 2] ) – 1. 2 p. H + 20. 7 pe = 16. 9 Eh, Eh in volts (platinum electrode measurement) 57

Redox and pe in SOLUTION Data Blocks • When do you need pe for

Redox and pe in SOLUTION Data Blocks • When do you need pe for SOLUTION? – To distribute total concentration of a redox element among redox states [e. g. Fe to Fe(2) and Fe(3)] – A few saturation indices with e- in dissociation reactions • Pyrite • Native sulfur • Manganese oxides • Can use a redox couple Fe(2)/Fe(3) in place of pe • Rarely, pe = 16. 9 Eh. (25 C and Eh in Volts). • pe options can only be applied to speciation calculations; thermodynamic pe is used for all other calculations 58

Iron Speciation with Phree. Plot 59

Iron Speciation with Phree. Plot 59

Redox Elements Element Redox state Species Carbon C(4) CO 2 Iron Fe(3) Fe+3 C(-4)

Redox Elements Element Redox state Species Carbon C(4) CO 2 Iron Fe(3) Fe+3 C(-4) CH 4 Fe(2) Fe+2 S(6) SO 4 -2 Manganese Mn(2) Mn+2 S(-2) HS- Arsenic As(5) As. O 4 -3 N(5) NO 3 - As(3) As. O 3 -3 N(3) NO 2 - U(6) UO 2+2 N(0) N 2 U(4) U+4 N(-3) NH 4+ Cr(6) Cr. O 4 -2 O(0) O 2 Cr(3) Cr+3 O(-2) H 2 O Se(6) Se. O 4 -2 H 2 O Se(4) Se. O 3 -2 H 2 Se(-2) HSe- Sulfur Nitrogen Oxygen Hydrogen H(1) H(0) Uranium Chromium Selenium 60

Seawater Initial Solution Fe total was entered. How were Fe(3) and Fe(2) concentrations calculated?

Seawater Initial Solution Fe total was entered. How were Fe(3) and Fe(2) concentrations calculated? For initial solutions For “reactions” 61

Final thoughts on pe • pe sets ratio of redox states • Some redox

Final thoughts on pe • pe sets ratio of redox states • Some redox states are measured directly: – – NO 3 -, NO 2 -, NH 3, N 2(aq) SO 4 -2, HSO 2(aq) Sometimes Fe, As • Others can be assumed: – – – Fe, always Fe(2) except at low p. H Mn, always Mn(2) As, consider other redox elements Se, consider other redox elements U, probably U(6) V, probably V(5) 62

Berner’s Redox Environments • • Oxic Suboxic Sulfidic Methanic Thorstenson (1984) 63

Berner’s Redox Environments • • Oxic Suboxic Sulfidic Methanic Thorstenson (1984) 63

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Parkhurst and others (1996) 65

Parkhurst and others (1996) 65

Summary on Solutions • • • Aqueous model SOLUTION p. H—Ratio of HCO 3

Summary on Solutions • • • Aqueous model SOLUTION p. H—Ratio of HCO 3 - to CO 2 pe—Ratio of oxidized to reduced state Saturation indices 66

Reaction Simulations • SOLUTION, SOLUTION_SPREAD, MIX, USE solution, or USE mix Equilibrium EQUILIBRIUM_PHASES EXCHANGE

Reaction Simulations • SOLUTION, SOLUTION_SPREAD, MIX, USE solution, or USE mix Equilibrium EQUILIBRIUM_PHASES EXCHANGE SURFACE SOLID_SOLUTION GAS_PHASE REACTION_TEMPERATURE REACTION_PRESSURE Nonequilibrium • END KINETICS REACTION 67

Keywords SOLUTION END USE REACTION_TEMPERATURE USER_GRAPH REACTION_PRESSURE 68

Keywords SOLUTION END USE REACTION_TEMPERATURE USER_GRAPH REACTION_PRESSURE 68

Plot the SI of Calcite with Temperature Seawater-t&p. pqi 69

Plot the SI of Calcite with Temperature Seawater-t&p. pqi 69

SI Calcite for Seawater with T 70

SI Calcite for Seawater with T 70

SI Calcite for Seawater with P 71

SI Calcite for Seawater with P 71

Initial Solution 11. Exercise Rainwater, Concentration in mg/L Constituent p. H Ca Mg Na

Initial Solution 11. Exercise Rainwater, Concentration in mg/L Constituent p. H Ca Mg Na K C(4) Value 4. 5 0. 384 0. 043 0. 141 0. 036 ? Constituent Cl S(6) N(5) N(-3) P Value 0. 236 1. 3 0. 237 0. 208 0. 0003 1. Calculate the carbon concentration that would be in equilibrium with the atmosphere (log PCO 2 = -3. 5). 72

Initial Solution 11. Answer 1. Calculate the carbon concentration that would be in equilibrium

Initial Solution 11. Answer 1. Calculate the carbon concentration that would be in equilibrium with the atmosphere (log PCO 2 = -3. 5). 1. 1 e-5 mol C per kilogram water 73

Initial Solution 12. Exercise 1. Calculate the p. H and TDIC of a solution

Initial Solution 12. Exercise 1. Calculate the p. H and TDIC of a solution in equilibrium with the PCO 2 of air (10 -3. 5) at 25 C. 2. Calculate the p. H and TDIC of a solution in equilibrium with a soil-zone PCO 2 of 10 -2. 0 at 25 C. 3. Calculate the p. H and TDIC of a solution in equilibrium with a soil-zone PCO 2 of 10 -2. 0 at 10 C. 74

Initial Solution 12. Answers 1. p. H = 5. 66, TDIC = 13 umol/kgw

Initial Solution 12. Answers 1. p. H = 5. 66, TDIC = 13 umol/kgw 2. p. H = 4. 91, TDIC = 353 umol/kgw 3. p. H = 4. 87, TDIC = 552 umol/kgw 75

SATURATION INDEX The thermodynamic state of a mineral relative to a solution IAP is

SATURATION INDEX The thermodynamic state of a mineral relative to a solution IAP is ion activity product K is equilibrium constant 76

SATURATION INDEX SI < 0, Mineral should dissolve SI > 0, Mineral should precipitate

SATURATION INDEX SI < 0, Mineral should dissolve SI > 0, Mineral should precipitate SI ~ 0, Mineral reacts fast enough to maintain equilibrium Maybe – Kinetics – Uncertainties 77

Rules for Saturation Indices • Mineral cannot dissolve if it is not present •

Rules for Saturation Indices • Mineral cannot dissolve if it is not present • If SI < 0 and mineral is present—the mineral could dissolve, but not precipitate • If SI > 0—the mineral could precipitate, but not dissolve • If SI ~ 0—the mineral could dissolve or precipitate to maintain equilibrium 78

Uncertainties in SI: Analytical data • 5% uncertainty in element concentration is. 02 units

Uncertainties in SI: Analytical data • 5% uncertainty in element concentration is. 02 units in SI. • 0. 5 p. H unit uncertainty is 0. 5 units in SI of calcite, 1. 0 unit in dolomite • 1 pe or p. H unit uncertainty is 8 units in SI of Fe. S for the following equation: SI(Fe. S) = log[Fe+3]+log[SO 4 -2]-8 p. H-8 pe-log K(Fe. S) 79

Uncertainties in SI: Equation • Much smaller uncertainty for SI(Fe. S) with the following

Uncertainties in SI: Equation • Much smaller uncertainty for SI(Fe. S) with the following equation : SI(Fe. S) = log[Fe+2]+log[HS-]+p. H-log K(Fe. S) • For minerals with redox elements, uncertainties are much smaller if the valence states of the elements in solution are measured. 80

Uncertainties in SI: Log K Apatite from Stumm and Morgan: Ca 5(PO 4)3(OH) =

Uncertainties in SI: Log K Apatite from Stumm and Morgan: Ca 5(PO 4)3(OH) = 5 Ca+2 + 3 PO 4 -3 + OH- Apatite from Wateq: log K = -55. 4 Log Ks especially uncertain for aluminosilicates 81

Useful Mineral List Minerals that may react to equilibrium relatively quickly 82

Useful Mineral List Minerals that may react to equilibrium relatively quickly 82

Initial Solution 13. Exercise Examine solution compositions in spreadsheet “solution_spread. xls”. Calculate saturation indices

Initial Solution 13. Exercise Examine solution compositions in spreadsheet “solution_spread. xls”. Calculate saturation indices using phreeqc. dat. Try out Run. Phreeqc macro or copy/paste into Phreeqc. I. What can you infer about the hydrologic setting, mineralogy, and possible reactions for these waters? 83

Solution_spread. xls + is 13. xls 84

Solution_spread. xls + is 13. xls 84

Summary Aqueous speciation model – Mole-balance equations—Sum of species containing Ca equals total analyzed

Summary Aqueous speciation model – Mole-balance equations—Sum of species containing Ca equals total analyzed Ca – Aqueous mass-action equations—Activity of products over reactants equal a constant Activity coefficient model – • • – Ion association with individual activity coefficients Pitzer specific interaction approach SI=log(IAP/K) 85

Summary SOLUTION and SOLUTION _SPREAD – – – Units p. H—ratio of HCO 3/CO

Summary SOLUTION and SOLUTION _SPREAD – – – Units p. H—ratio of HCO 3/CO 2 pe—ratio of oxidized/reduced valence states Charge balance Phase boundaries • Saturation indices – Uncertainties – Useful minerals • Identify potential reactants 86

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