CHE 3341 Mass Transfer Operations
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Transcript of CHE 3341 Mass Transfer Operations
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Molecular Thermodynamics of
Brine Chemistry
Chau-Chyun Chen
Jack Maddox Distinguished Engineering Chair
Department of Chemical Engineering
Texas Tech University
Presented at the UpTec Workshop, May 16, 2014
Slide 1
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Slide 2
http://www.nobelprize.org/nobel_prizes/chemistry/laureates/1901/
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Composition of Oilfield Produced Water
Slide 3
Igunnu and Chen, Int J Low Carbon Tech., 2012, 0, 1-21; Lou et al., 2014
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Composition of Oilfield Produced Water
Slide 4
Igunnu and Chen, Int J Low Carbon Tech., 2012, 0, 1-21; Lou et al., 2014
Anions
Cations
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Slide 5
Lou et al., 2014
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Slide 6
Lou et al., 2014
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Slide 7
Lou et al., 2014
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Slide 8Accurate thermodynamic model is the scientific foundation of process simulation
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Slide 9Accurate thermodynamic model is the scientific foundation of process simulation
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Composition of Brines/Injection
Water/Formation Water
Slide 10
Fluid Phase Equilibria, 2014, 373, 43-54
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Slide 11
Fluid Phase Equilibria, 2014, 373, 43-54
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Important Salts in Hexary Oceanic Salt
Systems (Na+/K+/Mg2+/Ca2+,Cl-/SO42-)
Slide 12
Pure Appl Chem, 2001, 73, 831-844
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Slide 13
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Pitzer’s Ion-Interaction Model
Slide 14
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Slide 15
Pure & Applied Chemistry, 2001, 73, 831-844
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Slide 16
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Pitzer Model for Hexary Oceanic Salt
Systems (Na+/K+/Mg2+/Ca2+,Cl-/SO42-)
o 3 parameters per binary and additional 2 per ternary
o 8 binary and 16 ternary systems
o 56 isothermal parameters and additional 2 for 2-2 valent
electrolytes (MgSO4 and CaSO4) -> 58 parameters
o Parameters & code available in PHREEQC, ChemApp,
GEMS, MINEQL+, etc.) for room temperature applications
To cover 0 to 200 °C, up to 8 temperature coefficients are
necessary for each Pitzer parameter -> 464 coefficients
Predictive power limited at ionic strength > 6 molal
Need models with smaller number of parameters -> one
general approach is NRTL+xDH
Slide 17
Pure Appl Chem, 2011, 83, 1015-1030
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Slide 18
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Electrolyte NRTL Model
Slide 19
I&ECR, 2009, 48, 7788-7797
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Development of TTU Thermodynamic
Model for Brines & Produced Water
Based on symmetric electrolyte NRTL model
An industry standard and a comprehensive thermodynamic
model capable of handling aqueous electrolytes, nonaqueous
electrolytes, nonelectrolytes, ionic liquids, etc.
Successfully used to model scale formation in oil reservoirs
during water injection, CO2 capture with amines, and CO2
solubility in saline water
Cover temperatures up to 200 °C and salt concentrations up to
saturation
Code available in Aspen process simulator
Slide 20
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eNRTL Model for Hexary Oceanic Salt
Systems (Na+/K+/Mg2+/Ca2+,Cl-/SO42-)
2 parameters per binary and additional 2 per ternary
8 binary and 16 ternary systems
48 isothermal parameters
To cover 0 to 200 °C, up to 3 temperature coefficients
are necessary for each eNRTL parameter -> 144
parameters (vs. 464 for Pitzer)
Predictive up to saturation
Slide 21
Pure Appl Chem, 2011, 83, 1015-1030
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Slide 22
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Model Development: KCl-H2O Binary
Slide 23
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Model Development: KCl-NaCl-H2O
Ternary
Slide 24
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NaCl-Na2SO4 at 25 °C
Slide 25
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NaCl-MgCl2 at 25 °C
Slide 26
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MgCl2-MgSO4 at 25 °C
Slide 27
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MgCl2-MgSO4 at 75 °C
Slide 28
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MgSO4-Na2SO4 at 25 °C
Slide 29
Astrakhanite: MgSO4.Na2SO4.4H2O
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MgSO4-Na2SO4 at 75 °C
Slide 30
Loweite: 2MgSO4.2Na2SO4.5H2O; Vanthoffite: MgSO4.3Na2SO4
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Next Steps
Molecular thermodynamic model for the hexary
oceanic salt system within ~12 months
Molecular thermodynamic model for hydraulic
fracturing (adding Ba2+/Sr2+, HCO3-,) within ~24
months
TTU models should support process modeling and
simulation of produced water treatment processes and
mixing of brines/produced water
TTU models should have applications in many other
fieldsSlide 31