Zero pollution hybrid desalination and energy production system
The hybrid desalination and energy production system includes a desalination system for separating seawater into purified water and brine, an electrodialysis system for treating the brine and outputting low salinity water, a hypersaline brine solution, and H 2 gas; an evaporator for treating the hypersaline brine solution and outputting salt and water vapor; a superheater for treating the water vapor and outputting a superheated water vapor; a turbine for receiving the superheated water vapor to generate energy; a gas scrubber for receiving the H 2 gas from the electrodialysis system and producing dry hydrogen; and a hydrogen cell for receiving the dry hydrogen and outputting energy. A condenser converts the vapor into condensate and low salinity water. A desalinated water collection tank receives the desalinated or low salinity water. A pressure retarded osmosis system receives the brine, the low salinity water, and condensate from the condenser to produce dilute brine.
1. A zero pollution hybrid desalination and energy production system, comprising:
a desalination system for separating seawater into purified water and brine;
an electrodialysis system for treating the brine and outputting low salinity water, a hypersaline brine solution, and H 2 gas;
an evaporator for treating the hypersaline brine solution and outputting salt and water vapor;
a superheater for treating the water vapor and outputting a superheated water vapor;
a turbine for receiving the superheated water vapor to generate energy;
a gas scrubber for receiving the H 2 gas from the electrodialysis system and producing dry hydrogen (H 2 ); and
a hydrogen (H 2 ) cell for receiving the dry hydrogen (H 2 ) and outputting energy.
2. The system of claim 1 , further comprising a power plant for receiving the energy generated by the turbine and the energy output from the hydrogen (H 2 ) cell.
3. The system of claim 1 , wherein the desalination system comprises a thermal-based system for separating seawater into purified water and brine.
4. The system of claim 3 , wherein the thermal-based system for separating seawater into purified water and brine is selected from the group consisting of a multistage flash distillation system, a multiple effect distillation system, a vapour compression evaporation system, a cogeneration system, and a solar water desalination system.
5. The system of claim 1 wherein the desalination system comprises a membrane-based system for separating seawater into purified water and brine.
6. The system of claim 5 , wherein the membrane-based system for separating seawater into purified water and brine is selected from the group consisting of a reverse osmosis system, an electrodialysis system, and a membrane distillation system.
7. The system of claim 1 , wherein the desalination system comprises a multistage flash system for separating seawater into purified water and a brine reject waste stream.
8. The system of claim 1 , wherein the desalination system comprises a reverse osmosis system for separating seawater into purified water and a brine reject waste stream.
9. The system of claim 1 , wherein the desalination system comprises a multi-effect desalination process for separating seawater into purified water and a brine reject waste stream.
10. The system of claim 1 , further comprising a condenser for converting the water vapor from the evaporator into condensate and low salinity water.
11. The system of claim 1 , wherein the salt produced by the evaporator includes edible salt and wet salt.
12. The system of claim 11 , further comprising a refinery for refining the wet salt to produce NaOH, NaClO, Cl 2 , and HCl.
13. The system of claim 1 , further comprising a pressure retarded osmosis system for receiving the brine from the desalination system and condensate from the condenser to produce dilute brine.
14. A zero pollution hybrid desalination and energy production method for water desalination, comprising:
a desalination step for separating seawater into purified water and brine;
an electrodialysis step including treating the brine and outputting low salinity water, a hypersaline brine solution, and H 2 gas;
an evaporation step including treating the hypersaline brine solution and outputting salt and water vapor;
a superheating step including treating the water vapor and outputting a superheated water vapor;
a first energy-generation step including transferring the superheated water vapor to a turbine and moving the blades of the turbine to generate energy;
a gas scrubbing step including receiving H 2 gas from the electrodialysis system and producing dry hydrogen (H 2 ); and
a second energy-generation step including receiving dry hydrogen (H 2 ) and outputting energy.
15. The method of claim 14 , further comprising transferring the energy generated by the first energy-generation step and the second energy-generation step to a power plant.
16. The method of claim 14 , wherein the desalination step comprises using a thermal-based process for separating seawater into purified water and brine.
17. The method of claim 14 , wherein the desalination step comprises using a membrane-based process for separating seawater into purified water and brine.
18. The method of claim 14 , wherein the desalination step comprises using a multistage flash process for separating seawater into purified water and brine.
19. The method of claim 14 , wherein the desalination step comprises using a reverse osmosis process for separating seawater into purified water and brine.
20. The method of claim 14 , wherein the desalination step comprises using a multi-effect desalination process for separating seawater into purified water and brine.