Integrated LNG gasification and power production cycle
The present disclosure provides an integrated power generating system and method and liquefied natural gas (LNG) vaporization system and method. More particularly, heat from a CO 2 containing stream from the power generating system and method can be used to heat the LNG for re-gasification as gaseous CO 2 from CO 2 containing stream is liquefied. The liquefied CO 2 can be captured and/or recycled back to a combustor in the power generating system and method.
1. A power generating system comprising:
a combustor adapted to receive a carbonaceous fuel, oxygen, and pressurized, recycled CO 2 and output a pressurized combustion product comprising CO 2 ;
a power producing turbine fluidly connected with the combustor and adapted to expand the pressurized combustion product comprising CO 2 and output a turbine exhaust comprising CO 2 ;
an economizer heat exchanger fluidly connected at a hot end of the economizer heat exchanger with the power producing turbine and the combustor and adapted to transfer heat from the turbine exhaust stream comprising CO 2 to the pressurized, recycled CO 2 and output from a cold end of the economizer heat exchanger a cooled turbine exhaust comprising CO 2 ;
a separator fluidly connected to the economizer heat exchanger and adapted to output substantially pure CO 2 ;
a liquid CO 2 pump adapted to compress liquefied CO 2 ;
a CO 2 liquefier heat exchanger fluidly connected at a cold end of the CO 2 liquefier heat exchanger to the separator and to the economizer heat exchanger and fluidly connected at a hot end of the CO 2 liquefier heat exchanger to both of an input of the liquid CO 2 pump and an output of the liquid CO 2 pump;
a source of liquefied natural gas (LNG) fluidly connected with the hot end of the CO 2 liquefier heat exchanger; and
a further heat exchanger positioned between the economizer heat exchanger and the CO 2 liquefier heat exchanger so as to be fluidly connected with the cold end of the economizer heat exchanger and the hot end of the CO 2 liquefier heat exchanger;
wherein the further heat exchanger includes an inlet fluidly connected with an outlet on the cold end of the economizer heat exchanger, an inlet fluidly connected with an outlet on the hot end of the CO 2 liquefier heat exchanger, and an outlet fluidly connected with an inlet on the hot end of the CO 2 liquefier heat exchanger.
2. The system of claim 1 , wherein the separator is positioned between the outlet of the further heat exchanger and the inlet on the hot end of the CO 2 liquefier heat exchanger.
3. The system of claim 1 , wherein the power producing turbine is adapted to provide shaft power for the liquid CO 2 pump.
4. The system of claim 1 , further comprising an air separation plant.
5. The system of claim 4 , wherein the air separation plant is a cryogenic air separation plant.