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US 7,789,159 B1Granted
Methods to de-sulfate saline streams
OwnerMansour S. Baderinventor
Life of this patent
Estimating the term…
Abstract
Methods are disclosed to de-sulfate saline streams such as seawater, brine from seawater desalination plants, and the like. The disclosed methods can also co-produce de-ionized water and inorganic materials from such de-sulfated saline streams.
Claims38
A method for separating sulfate from saline water to produce nearly sulfate-free saline stream and inorganic materials, said method comprising the steps of:
- (a) removing sulfate from said saline water by
- (i) mixing calcium chloride rich formation water with said saline water to allow the concentration of the calcium ion to exceed the concentration of the sulfate ion in said saline water to produce intermediate concentrate;
- (ii) pressurizing said intermediate concentrate into a precipitator at pressure between 50 psi and 1,200 psi through at least one nozzle to produce a jet stream of said intermediate concentrate;
- (iii) pressurizing amine solvent or amine solvent with modifier into said precipitator at pressure between 50 psi and the critical pressure of said amine solvent or said amine solvent with modifier through at least one nozzle to form precipitates comprising gypsum from said intermediate concentrate;
- (iv) removing said precipitates from said intermediate concentrate by filter to produce gypsum slurry;
- (v) removing at least most of said amine solvent or said amine solvent with modifier from said intermediate concentrate by stripper to produce said nearly sulfate-free saline stream;
- (b) injecting said nearly sulfate-free saline stream into subterranean formation for hydrocarbons recovery;
- or
- (c) feeding said nearly sulfate-free saline stream into conventional seawater desalinations plants and auxiliary equipments;
- or
- (d) producing de-ionized water from said nearly sulfate-free saline stream by membrane distillation;
- (e) producing gypsum boards or gypsum materials from said gypsum slurry by
- (i) separating said gypsum slurry into moist solid gypsum and liquor stream by filter;
- (ii) removing at least most of remaining said amine solvent or said amine solvent with modifier from said liquor stream by stripper;
- (iii) recycling said liquor stream to said intermediate concentrate;
- (iv) molding said moist solid gypsum to produce said gypsum boards or said gypsum materials;
- (v) allowing said gypsum boards or said gypsum materials to dry;
- or
- (f) producing potassium sulfate and calcium chloride from said gypsum slurry by
- (i) adding sylvite or sylvinite to said gypsum slurry to produce intermediate liquor stream;
- (ii) adding said amine solvent or said amine solvent with modifier to said intermediate liquor stream to form precipitates comprising said potassium sulfate;
- (iii) removing said precipitates from said intermediate liquor stream by filter;
- (iv) removing at least most of said amine solvent or said amine solvent with modifier by stripper;
- (v) recycling said intermediate liquor stream comprising at least dissolved calcium chloride to said intermediate concentrate;
- or
- (vi) recovering said intermediate liquor stream comprising at least calcium chloride brine.
23 more elements
A method for separating sulfate and brucite from saline water to produce nearly sulfate-brucite free saline stream and inorganic materials, said method comprising the steps of
- (a) removing sulfate from said saline water by
- (i) mixing calcium chloride rich formation water with said saline water to allow the concentration of the calcium ion to exceed the concentration of the sulfate ion in said saline water to produce intermediate concentrate;
- (ii) pressurizing said intermediate concentrate into a precipitator at pressure between 50 psi and 1,200 psi through at least one nozzle to produce a jet stream of said intermediate concentrate;
- (iii) pressurizing amine solvent or amine solvent with modifier into said precipitator at pressure between 50 psi and the critical pressure of said amine solvent or said amine solvent with modifier through at least one nozzle to form precipitates comprising gypsum from said intermediate concentrate;
- (iv) removing said precipitates from said intermediate concentrate by filter to produce gypsum slurry;
- (v) removing at least most of said amine solvent or said amine solvent with modifier from said intermediate concentrate by stripper to produce said nearly sulfate-free saline stream;
- (b) removing brucite from said nearly sulfate-free saline stream by
- (i) pressurizing said nearly sulfate-free saline stream into a second precipitator at pressure between 50 psi and 1,200 psi through at least one nozzle to produce a jet stream of said nearly sulfate-free saline stream;
- (ii) pressurizing amine solvent or amine solvent with modifier into said second precipitator at pressure between 50 psi and the critical pressure of said amine solvent or said amine solvent with modifier through at least one nozzle to form precipitates comprising said brucite from said nearly sulfate-free saline stream;
- (iii) removing said precipitates from said nearly sulfate-free saline stream by filter to produce brucite slurry;
- (iv) removing at least most of said amine solvent or said amine solvent with modifier from said nearly sulfate-free saline stream by stripper to produce said nearly sulfate-brucite free saline stream;
- (c) injecting said nearly sulfate-brucite free saline stream into subterranean formation for hydrocarbons recovery;
- or
- (d) feeding said nearly sulfate-brucite free saline stream into conventional seawater desalinations plants and auxiliary equipments;
- or
- (e) producing de-ionized water from said nearly sulfate-brucite free saline stream by membrane distillation;
- (f) producing gypsum boards or gypsum materials from said gypsum slurry by
- (i) separating said gypsum slurry into moist solid gypsum and liquor stream by filter;
- (ii) removing at least most of remaining said amine solvent or said amine solvent with modifier from said liquor stream by stripper;
- (iii) recycling said liquor stream to said intermediate concentrate;
- (iv) molding said moist solid gypsum to produce said gypsum boards or said gypsum materials;
- (v) allowing said gypsum boards or said gypsum materials to dry;
- or
- (g) producing potassium sulfate and calcium chloride from said gypsum slurry by
- (i) adding sylvite or sylvinite to said gypsum slurry to produce intermediate liquor stream;
- (ii) adding said amine solvent or said amine solvent with modifier to said intermediate liquor stream to form precipitates comprising said potassium sulfate;
- (iii) removing said precipitates from said intermediate liquor stream by filter;
- (iv) removing at least most of said amine solvent or said amine solvent with modifier by stripper;
- (v) recycling said intermediate liquor stream comprising at least dissolved calcium chloride to said intermediate concentrate;
- or
- (vi) recovering said intermediate liquor stream comprising at least calcium chloride brine.
28 more elements
A method for separating sulfate from saline water to produce nearly sulfate-free saline stream and inorganic materials, said method comprising the steps of:
- (a) separating calcium chloride rich produced water from wet oil by hydrophobic membranes;
- (b) removing sulfate from said saline water by
- (i) mixing said calcium chloride rich produced water with said saline water to allow the concentration of the calcium ion to exceed the concentration of the sulfate ion in said saline water to produce intermediate concentrate;
- (ii) pressurizing said intermediate concentrate into a precipitator at pressure between 50 psi and 1,200 psi through at least one nozzle to produce a jet stream of said intermediate concentrate;
- (iii) pressurizing amine solvent or amine solvent with modifier into said precipitator at pressure between 50 psi and the critical pressure of said amine solvent or said amine solvent with modifier through at least one nozzle to form precipitates comprising gypsum from said intermediate concentrate;
- (iv) removing said precipitates from said intermediate concentrate by filter to produce gypsum slurry;
- (v) removing at least most of said amine solvent or said amine solvent with modifier from said intermediate concentrate by stripper to produce said nearly sulfate-free saline stream;
- (c) injecting said nearly sulfate-free saline stream into subterranean formation for hydrocarbons recovery;
- or
- (d) feeding said nearly sulfate-free saline stream into conventional seawater desalinations plants and auxiliary equipments;
- or
- (e) producing de-ionized water from said nearly sulfate-free saline stream by membrane distillation;
- (f) producing gypsum boards or gypsum materials from said gypsum slurry by
- (i) separating said gypsum slurry into moist solid gypsum and liquor stream by filter;
- (ii) removing at least most of remaining said amine solvent or said amine solvent with modifier from said liquor stream by stripper;
- (iii) recycling said liquor stream to said intermediate concentrate;
- (iv) molding said moist solid gypsum to produce said gypsum boards or said gypsum materials;
- (v) allowing said gypsum boards or said gypsum materials to dry;
- or
- (g) producing potassium sulfate and calcium chloride from said gypsum slurry by
- (i) adding sylvite or sylvinite to said gypsum slurry to produce intermediate liquor stream;
- (ii) adding said amine solvent or said amine solvent with modifier to said intermediate liquor stream to form precipitates comprising said potassium sulfate;
- (iii) removing said precipitates from said intermediate liquor stream by filter;
- (iv) removing at least most of said amine solvent or said amine solvent with modifier by stripper;
- (v) recycling said intermediate liquor stream comprising at least dissolved calcium chloride to said intermediate concentrate;
- or
- (vi) recovering said intermediate liquor stream comprising at least calcium chloride brine.
24 more elements
A method for separating sulfate and brucite from saline water to produce nearly sulfate-brucite free saline stream and inorganic materials, said method comprising the steps of:
- (a) separating calcium chloride rich produced water from wet oil by hydrophobic membranes;
- (b) removing sulfate from said saline water by
- (i) mixing calcium chloride rich produced water with said saline water to allow the concentration of the calcium ion to exceed the concentration of the sulfate ion in said saline water to produce intermediate concentrate;
- (ii) pressurizing said intermediate concentrate into a precipitator at pressure between 50 psi and 1,200 psi through at least one nozzle to produce a jet stream of said intermediate concentrate;
- (iii) pressurizing amine solvent or amine solvent with modifier into said precipitator at pressure between 50 psi and the critical pressure of said amine solvent or said amine solvent with modifier through at least one nozzle to form precipitates comprising gypsum from said intermediate concentrate;
- (iv) removing said precipitates from said intermediate concentrate by filter to produce gypsum slurry;
- (v) removing at least most of said amine solvent or said amine solvent with modifier from said intermediate concentrate by stripper to produce said nearly sulfate-free saline stream;
- (c) removing brucite from said nearly sulfate-free saline stream by
- (i) pressurizing said nearly sulfate-free saline stream into a second precipitator at pressure between 50 psi and 1,200 psi through at least one nozzle to produce a jet stream of said nearly sulfate-free saline stream;
- (ii) pressurizing amine solvent or amine solvent with modifier into said second precipitator at pressure between 50 psi and the critical pressure of said amine solvent or said amine solvent with modifier through at least one nozzle to form precipitates comprising said brucite from said nearly sulfate-free saline stream;
- (iii) removing said precipitates from said nearly sulfate-free saline stream by filter to produce brucite slurry;
- (iv) removing at least most of said amine solvent or said amine solvent with modifier from said nearly sulfate-free saline stream by stripper to produce said nearly sulfate-brucite free saline stream;
- (d) injecting said nearly sulfate-brucite free saline stream into subterranean formation for hydrocarbons recovery;
- or
- (e) feeding said nearly sulfate-brucite free saline stream into conventional seawater desalinations plants and auxiliary equipments;
- or
- (f) producing de-ionized water from said nearly sulfate-brucite free saline stream by membrane distillation;
- (g) producing gypsum boards or gypsum materials from said gypsum slurry by
- (i) separating said gypsum slurry into moist solid gypsum and liquor stream by filter;
- (ii) removing at least most of remaining said amine solvent or said amine solvent with modifier from said liquor stream by stripper;
- (iii) recycling said liquor stream to said intermediate concentrate;
- (iv) molding said moist solid gypsum to produce said gypsum boards or said gypsum materials;
- (v) allowing said gypsum boards or said gypsum materials to dry;
- or
- (h) producing potassium sulfate and calcium chloride from said gypsum slurry by
- (i) adding sylvite or sylvinite to said gypsum slurry to produce intermediate liquor stream;
- (ii) adding said amine solvent or said amine solvent with modifier to said intermediate liquor stream to form precipitates comprising said potassium sulfate;
- (iii) removing said precipitates from said intermediate liquor stream by filter;
- (iv) removing at least most of said amine solvent or said amine solvent with modifier by stripper;
- (v) recycling said intermediate liquor stream comprising at least dissolved calcium chloride to said intermediate concentrate;
- or
- (vi) recovering said intermediate liquor stream comprising at least calcium chloride brine.
29 more elements
Dependencies are inferred from the claim text.