초록 ▼

According to one embodiment of the invention, a vapor-compression evaporation system includes a plurality of vessels in series each containing a feed having a nonvolatile component. A first set of the plurality of vessels includes vapor-compression evaporators and a second set of the plurality of ve

According to one embodiment of the invention, a vapor-compression evaporation system includes a plurality of vessels in series each containing a feed having a nonvolatile component. A first set of the plurality of vessels includes vapor-compression evaporators and a second set of the plurality of vessels includes multi-effect evaporators. A mechanical compressor is coupled to the last vessel in the series of vapor-compression evaporators and is operable to receive a vapor therefrom. A turbine is coupled to, and operable to drive, the mechanical compressor. A pump is operable to deliver a cooling liquid to the mechanical compressor, and a tank is coupled to the mechanical compressor and is operable to separate liquid and vapor received from the mechanical compressor. A plurality of heat exchangers is coupled inside respective ones of the vessels, wherein the heat exchanger in the first vessel in the first set is operable to receive the vapor from the tank, and at least some of the vapor condenses therein. The heat of condensation provides the heat of evaporation to the first vessel in the first set, and at least some of the vapor inside the first vessel in the first set is delivered to the heat exchanger in the next vessel in the first set, whereby the condensing, evaporating, and delivering steps continue until the last vessel in the second set is reached.

대표청구항 ▼

What is claimed is: 1. A vapor-compression evaporation system, comprising: a plurality of vessels in series each containing a feed having a nonvolatile component, a first set of the plurality of vessels comprising vapor-compression evaporators and a second set of the plurality of vessels comprising

What is claimed is: 1. A vapor-compression evaporation system, comprising: a plurality of vessels in series each containing a feed having a nonvolatile component, a first set of the plurality of vessels comprising vapor-compression evaporators and a second set of the plurality of vessels comprising multi-effect evaporators; a mechanical compressor coupled to the last vessel in the series of vapor-compression evaporators and operable to receive a vapor therefrom; a turbine coupled to, and operable to drive, the mechanical compressor; a pump operable to deliver a cooling liquid to the mechanical compressor; a tank coupled to the mechanical compressor and operable to separate liquid and vapor received from the mechanical compressor; a plurality of heat exchangers coupled inside respective ones of the vessels, the heat exchanger in the first vessel in the first set operable to receive the vapor from the tank, at least some of the vapor condensing therein, whereby the heat of condensation provides the heat of evaporation to the first vessel in the first set; and wherein at least some of the vapor inside the first vessel in the first set is delivered to the heat exchanger in the next vessel in the first set, whereby the condensing, evaporating, and delivering steps continue until the last vessel in the second set is reached. 2. The vapor-compression evaporation system of claim 1, wherein the nonvolatile component is selected from the group consisting of salt and sugar. 3. The vapor-compression evaporation system of claim 1, wherein the feed is degassed feed. 4. The vapor-compression evaporation system of claim 1, wherein the turbine comprises a gas turbine. 5. The vapor-compression evaporation system of claim 1, wherein the turbine comprises a gas turbine and a steam turbine. 6. The vapor-compression evaporation system of claim 1, further comprising a condenser coupled to the last vessel in the second set for removing energy from the last vessel in the second set. 7. The vapor-compression evaporation system of claim 1, further comprising a plurality of devices coupled to respective ones of the vessels for removing concentrated feed from respective ones of the vessels. 8. The vapor-compression evaporation system of claim 1, wherein the cooling liquid comprises saltwater or freshwater. 9. The vapor-compression evaporation system of claim 1, wherein the mechanical compressor comprises first and second mechanical compressors in series, the first mechanical compressor driven by one of a steam turbine and a gas turbine, the second mechanical compressor driven by the other of the steam turbine and the gas turbine. 10. The vapor-compression evaporation system of claim 9, further comprising an intercooler coupled between the first and second mechanical compressors, the intercooler operable to receive the cooling liquid from the pump. 11. The vapor-compression evaporation system of claim 8, wherein the intercooler comprises a demister operable to prevent liquid droplets from entering the second mechanical compressor. 12. The vapor-compression evaporation system of claim 1, wherein the mechanical compressor comprises first and second mechanical compressors in parallel, the first mechanical compressor driven by one of a steam turbine and a gas turbine, the second mechanical compressor driven by the other of the steam turbine and the gas turbine. 13. A vapor-compression evaporation system, comprising: a plurality of vessels in series each containing a feed having a nonvolatile component, a first set of the plurality of vessels comprising vapor-compression evaporators and a second set of the plurality of vessels comprising multi-effect evaporators; a mechanical compressor coupled to the last vessel in the series of vapor-compression evaporators and operable to receive a vapor therefrom; an internal combustion engine coupled to the mechanical compressor and operable to drive the mechanical compressor; a pump operable to deliver a cooling liquid to the mechanical compressor; a tank coupled to the mechanical compressor and operable to separate liquid and vapor received from the mechanical compressor; a plurality of heat exchangers coupled inside respective ones of the vessels, the heat exchanger in the first vessel in the first set operable to receive the vapor from the tank, at least some of the vapor condensing therein, whereby the heat of condensation provides the heat of evaporation to the first vessel in the first set; and wherein at least some of the vapor inside the first vessel in the first set is delivered to the heat exchanger in the next vessel in the first set, whereby the condensing, evaporating, and delivering steps continue until the last vessel in the second set is reached. 14. The vapor-compression evaporation system of claim 13, wherein the nonvolatile component is selected from the group consisting of salt and sugar. 15. The vapor-compression evaporation system of claim 13, wherein the internal combustion engine comprises a Diesel engine or an Otto cycle engine. 16. The vapor-compression evaporation system of claim 13, further comprising a condenser coupled to the last vessel in the second set for removing energy from the last vessel in the second set. 17. The vapor-compression evaporation system of claim 13, further comprising a plurality of devices coupled to respective ones of the vessels for removing concentrated feed from respective ones of the vessels. 18. The vapor-compression evaporation system of claim 13, wherein the cooling liquid comprises saltwater or freshwater. 19. The vapor-compression evaporation system of claim 13, further comprising a packed column coupled to the internal combustion engine, the packed column operable to receive an exhaust gas from the internal combustion engine. 20. A vapor-compression evaporation system, comprising: a plurality of vessels in series each containing a feed having a nonvolatile component, a first set of the plurality of vessels comprising vapor-compression evaporators and a second set of the plurality of vessels comprising membrane evaporators; a mechanical compressor coupled to the last vessel in the series of vapor-compression evaporators and operable to receive a vapor therefrom; an internal combustion engine coupled to the mechanical compressor and operable to drive the mechanical compressor; a pump operable to deliver a cooling liquid to the mechanical compressor; a tank coupled to the mechanical compressor and operable to separate liquid and vapor received from the mechanical compressor; a plurality of heat exchangers coupled inside respective ones of the vapor-compression evaporators, the heat exchanger in the first vessel in the first set operable to receive the vapor from the tank, at least some of the vapor condensing therein, whereby the heat of condensation provides the heat of evaporation to the first vessel in the first set; and wherein at least some of the vapor inside the first vessel in the first set is delivered to the heat exchanger in the next vessel in the first set, whereby the condensing, evaporating, and delivering steps continue until the last vessel in the first set is reached. 21. The vapor-compression evaporation system of claim 20, wherein the nonvolatile component is selected from the group consisting of salt and sugar. 22. The vapor-compression evaporation system of claim 20, wherein the internal combustion engine comprises a Diesel engine or an Otto cycle engine. 23. The vapor-compression evaporation system of claim 20, further comprising a condenser coupled to the last vessel in the second set for removing energy from the last vessel in the second set. 24. The vapor-compression evaporation system of claim 20, further comprising a plurality of devices coupled to respective ones of the vessels for removing concentrated feed from respective ones of the vessels. 25. The vapor-compression evaporation system of claim 20, wherein the cooling liquid comprises saltwater or freshwater. 26. The vapor-compression evaporation system of claim 20, wherein each membrane evaporator comprises an inner chamber and two outer chambers defined by an impermeable membrane and a hydrophobic vapor-permeable membrane. 27. The vapor-compression evaporation system of claim 26, wherein the two outer chambers have saltwater flowing therethrough and the inner chamber has freshwater flowing therethrough. 28. The vapor-compression evaporation system of claim 26, wherein an exhaust gas from the internal combustion engine is operable to create steam that is fed into the heat exchanger in the first vessel in the first set. 29. A vapor-compression evaporation method, comprising: delivering a feed having a nonvolatile component to a plurality of vessels in series; coupling a mechanical compressor to the last vessel in the series; receiving, by the mechanical compressor, a vapor from the last vessel in the series; driving the mechanical compressor with a turbine; delivering a cooling liquid to the mechanical compressor; separating liquid and vapor received from the mechanical compressor; receiving, by a heat exchanger coupled to the first vessel in the series, the separated vapor, at least some of the vapor condensing therein, whereby the heat of condensation provides the heat of evaporation to the first vessel in the series; and delivering at least some of the vapor inside the first vessel in the series to a heat exchanger coupled to the next vessel in the series, whereby the condensing, evaporating, and delivering steps continue until the last vessel in the series is reached. 30. The vapor-compression evaporation method of claim 29, further comprising degassing the feed. 31. The vapor-compression evaporation method of claim 29, wherein driving the mechanical compressor with a turbine comprises driving the mechanical compressor with a gas turbine. 32. The vapor-compression evaporation method of claim 29, wherein driving the mechanical compressor with a turbine comprises driving the mechanical compressor with a gas turbine and a steam turbine. 33. The vapor-compression evaporation method of claim 29, further comprising removing energy from the last vessel in the series. 34. The vapor-compression evaporation method of claim 29, further comprising removing concentrated feed from respective ones of the vessels. 35. The vapor-compression evaporation method of claim 29, wherein the mechanical compressor comprises first and second mechanical compressors in series, the method further comprising driving the first mechanical compressor by a steam turbine and driving the second mechanical compressor by a gas turbine. 36. The vapor-compression evaporation method of claim 29, further comprising coupling an intercooler between the first and second mechanical compressors, the intercooler operable to receive the cooling liquid from the pump. 37. The vapor-compression evaporation method of claim 29, further comprising preventing liquid droplets from entering the second mechanical compressor. 38. The vapor-compression evaporation method of claim 29, wherein the mechanical compressor comprises first and second mechanical compressors in parallel, the method further comprising driving the first mechanical compressor by a steam turbine and driving the second mechanical compressor by a gas turbine.