Microcondenser device and evaporative emission control system and method having microcondenser device
US-9334837-B2 · May 10, 2016 · US
US10038131B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10038131-B2 |
| Application number | US-201615138554-A |
| Country | US |
| Kind code | B2 |
| Filing date | Apr 26, 2016 |
| Priority date | Sep 18, 2015 |
| Publication date | Jul 31, 2018 |
| Grant date | Jul 31, 2018 |
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Disclosed herein is a method and apparatus that uses a brine from a well that is used to both generate electricity and recover valuable minerals present in the brine. The method and apparatus uses a hydrophobic membrane to separate water vapor from the brine to concentrate the brine that is then used to recover the minerals.
Opening claim text (preview).
What is claimed is: 1. A method for generating electricity and recovering a mineral from a brine comprising the steps of: a) providing a first brine comprising water, silica, one or more polyvalent ions, and at least one mineral from a well, wherein the first brine has a temperature from about 150° C. to about 300° C.; b) removing at least a portion of the silica from the first brine, thereby producing a second brine; c) removing at least a portion of the water from the second brine by passing water vapor generated from the second brine through a hydrophobic membrane, thereby producing a third brine, wherein the third brine has a higher concentration of the at least one mineral than the second brine, wherein the second brine in step c) has a temperature from about 150° C. to about 190° C.; d) contacting at least a portion of the water vapor that passed through the hydrophobic membrane with a thermoelectric module, thereby generating electricity; and e) recovering at least a portion of the at least one mineral from the third brine. 2. The method of claim 1 , wherein the at least one mineral comprises lithium, zinc, magnesium, or uranium, or a combination thereof. 3. The method of claim 1 , wherein the concentration of the at least one mineral in the first brine is less than 0.1 wt %. 4. The method of claim 1 , wherein the second brine has a silica concentration of less than 0.01 wt %. 5. The method of claim 1 , wherein the method further comprises before step c) a step comprising removing at least a portion of the one or more polyvalent ions present in the first brine. 6. The method of claim 1 , wherein the concentration of the at least one mineral in the third brine is from about 0.02 wt % to about 0.3 wt %. 7. The method of claim 1 , wherein the thermoelectric module is configured to operate with a hot side of at a temperature from about 100° C. to about 180° C., and a cool side of about 10° C. to about 80° C. 8. The method of claim 1 , wherein recovering at least a portion of the at least one mineral from the third brine comprises extracting the at least one mineral from the third brine. 9. A method for generating electricity and recovering a mineral from a brine comprising the steps of: a) providing a first brine comprising water, silica, one or more polyvalent ions, and at least one mineral from a well, wherein the first brine has a temperature from about 150° C. to about 300° C.; b) removing at least a portion of the water from the first brine by passing water vapor generated from the first brine through a first hydrophobic membrane, thereby producing a fourth brine, wherein the fourth brine is at least about 5% more concentrated in total solids than the first brine; c) contacting at least a portion of the water vapor that passed through the first hydrophobic membrane with a thermoelectric module, thereby generating electricity; d) removing at least a portion of the silica and removing at least a portion of the one or more polyvalent ions from the fourth brine, thereby producing a fifth brine; e) removing at least a portion of the water from the fifth brine by passing water vapor generated from the fifth brine through a second hydrophobic membrane, wherein the temperature of the fifth brine in step e) is below about 150° C. thereby producing a sixth brine, wherein the sixth brine has a higher concentration of the at least one mineral than the fifth brine; and f) recovering at least a portion of the at least one mineral from the sixth brine. 10. The method of claim 9 , wherein the method further comprises contacting at least a portion of the water vapor that was generated from the fifth brine and passed through the second hydrophobic membrane with a thermoelectric module, thereby generating electricity. 11. The method of claim 9 , wherein the first brine has a temperature from about 150° C. about 190° C. 12. The method of claim 9 , wherein the first hydrophobic membrane is a ceramic hydrophobic membrane. 13. The method of claim 9 , wherein the second hydrophobic membrane is a polymeric hydrophobic membrane.
Hydrophobic membranes · CPC title
relating to the preparation of the feed · CPC title
Multistep processes · CPC title
using inorganic sorbents · CPC title
by flocculation or precipitation of suspended impurities {(C02F1/463 takes precedence)} · CPC title
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