Waste heat driven desalination process
View Patent ↗Disclosed is a process for improving the efficiency of a combined-cycle power generation plant and desalination unit. The process includes supplying exhaust gases from a gas turbine set used to generate electrical power to a heat recovery steam generator (HRSG) and then directing the steam from the HRSG to a steam turbine set. Salinous water is supplied into an effect of the desalination unit. Steam exhausted from the steam turbine set is utilized in the effect of the desalination unit to produce a distillate vapor and brine from the effect by heat exchange. Additionally, steam is introduced steam from at least one additional heat source from the combined-cycle power generation plant to the effect to increase the mass flow rate of steam into the effect. In one embodiment, the additional heat source is an intercooler heat exchanger. Heated water from the intercooler heat exchanger is provided to a reduced atmosphere flash tank, and the steam flashed in the flash tank is provided to the effect.
1. A process for improving the efficiency of a combined-cycle power generation plant and desalination unit, the process comprising:
supplying exhaust gases from a gas turbine set used to generate electrical power to a heat recovery steam generator (HRSG);
supplying salinous water into a thermal desalination unit;
utilizing steam from the HRSG as a first heat source in the thermal desalination unit to produce a distillate vapor and brine from the desalination unit by heat exchange; and
introducing thermal energy from a second heat source from the combined-cycle power generation plant to the thermal desalination unit to increase the mass flow rate of product water from the desalination unit, said second heat source comprising a heat exchanger fed by condensate from said thermal desalination unit, wherein hot water from said heat exchanger is provided to a reduced atmosphere flash tank to generate steam that is provided to said thermal desalination unit;
said method further comprising providing a third heat source, wherein said third heat source is an economizer heat exchanger in the HSRG;
providing heated water from said economizer heat exchanger to said reduced atmosphere flash tank and wherein a portion of said heated water from said economizer heat exchanger is also directed to a salinous feed water heat exchanger via a three-way valve to preheat salinous feed water of a reverse osmosis unit.
2. The process of claim 1 wherein said heat exchanger is an intercooler heat exchanger, wherein said hot water from the intercooler heat exchanger is provided to said reduced atmosphere flash tank and steam flashed in the flash tank is provided to the thermal desalination unit.
3. The process as recited in claim 1 wherein said thermal desalination unit is a multi-effect distillation unit.