A method of cold recovery in a cold compressed natural gas cycle, the method comprising: compressing air; drying air; heat exchanging air with cold compressed natural gas from a storage vessel, in a first heat exchanger, thereby forming cooled air; heat exchanging the cooled air with liquid methane,
A method of cold recovery in a cold compressed natural gas cycle, the method comprising: compressing air; drying air; heat exchanging air with cold compressed natural gas from a storage vessel, in a first heat exchanger, thereby forming cooled air; heat exchanging the cooled air with liquid methane, in a second heat exchanger, such that the cooled air becomes liquid air and the liquid methane becomes methane; heat exchanging the liquid air with natural gas from a pipeline, in a third heat exchanger, such that the natural gas cools to a cold compressed natural gas and the liquid air becomes air in a gaseous state; discharging the air in a gaseous state. A system of cold recovery comprising: an air dryer; an air compressor in fluid communication with the air dryer; a first heat exchanger in fluid communication with the air compressor; a second heat exchanger in fluid communication with the first heat exchanger; a third heat exchanger in fluid communication with the second heat exchanger; a methane expander valve in fluid communication with the second heat exchanger; a fourth heat exchanger in fluid communication with the methane expansion valve; a methane compressor in fluid communication with the second heat exchanger and with the fourth heat exchanger; a natural gas scrubber in fluid communication with a third heat exchanger; a natural gas pipeline in fluid communication with the first heat exchanger; the fourth heat exchanger, and the natural gas scrubber; and a storage vessel in fluid communication with the first heat exchanger, the third heat exchanger, and the fourth heat exchanger.
대표청구항▼
What is claimed is: 1. A method of cold recovery in a cold compressed natural gas cycle, the method comprising: compressing air; drying air; heat exchanging air with cold compressed natural gas from a storage vessel, in a first heat exchanger, thereby forming cooled air; heat exchanging the cooled
What is claimed is: 1. A method of cold recovery in a cold compressed natural gas cycle, the method comprising: compressing air; drying air; heat exchanging air with cold compressed natural gas from a storage vessel, in a first heat exchanger, thereby forming cooled air; heat exchanging the cooled air with liquid methane, in a second heat exchanger, such that the cooled air becomes liquid air and the liquid methane becomes methane; heat exchanging the liquid air with natural gas from a pipeline, in a third heat exchanger, such that the natural gas cools to a cold compressed natural gas and the liquid air becomes air in a gaseous state; discharging the air in a gaseous state; and delivering the cold compressed natural gas to a location selected from the group consisting of the storage vessel and a pipeline. 2. The method of claim 1, further comprising: compressing the methane gas; heat exchanging the compressed methane gas with cold compressed natural gas from the storage vessel, in a fourth heat exchanger, such that the methane becomes liquid methane and the cold compressed natural gas becomes natural gas in a typical gaseous state suitable for typical pipeline transportation; delivering the natural gas to a pipeline; expanding the liquid methane; and delivering the expanded liquid methane to the second heat exchanger. 3. A system of cold recovery comprising: an air dryer; an air compressor in fluid communication with the air dryer; a first heat exchanger in fluid communication with the air compressor; a second heat exchanger in fluid communication with the first heat exchanger; a third heat exchanger in fluid communication with the second heat exchanger; a methane expander valve in fluid communication with the second heat exchanger; a fourth heat exchanger in fluid communication with the methane expansion valve; a methane compressor in fluid communication with the second heat exchanger and with the fourth heat exchanger; a natural gas scrubber in fluid communication with a third heat exchanger; a natural gas pipeline in fluid communication with the first heat exchanger; the fourth heat exchanger, and the natural gas scrubber; and a storage vessel in fluid communication with the first heat exchanger, the third heat exchanger, and the fourth heat exchanger. 4. The system of claim 3, wherein the storage vessel is a subterranean storage facility. 5. The system of claim 3, further comprising: a liquid air storage tank in fluid communication with the second heat exchanger; and a liquid air pump in fluid communication with the third heat exchanger and the liquid air storage tank. 6. A system of cold recovery comprising: a first subsystem; the first subsystem comprising: an air dryer; an air compressor in fluid communication with the air dryer; a first heat exchanger in fluid communication with the air compressor and with the CCNG pipeline; a second heat exchanger in fluid communication with the first heat exchanger; a methane expander valve in fluid communication with the second heat exchanger; a liquid air expander valve in fluid communication with the second heat exchanger; a liquid methane heat exchanger in fluid communication with the methane expansion valve; a methane compressor in fluid communication with the liquid methane heat exchanger and with the second heat exchanger; a natural gas pipeline in fluid communication with the first heat exchanger; and a liquid air storage vessel in fluid communication with the first heat exchanger, the liquid air expander valve, and the liquid methane heat exchanger; and a liquid air pump in fluid communication with the liquid air storage vessel and the CCNG pipeline; a CCNG pipeline in fluid communication with the first subsystem; a second subsystem in fluid communication with the CCNG pipeline; and wherein the CCNG pipeline is configured to deliver liquid air from the first subsystem to the second subsystem, and the CCNG pipeline is further configured to deliver CCNG from the second subsystem to the first subsystem. 7. The system of claim 6, wherein the second subsystem comprises: a liquid air pump in fluid communication with the CCNG pipeline; a chilling cycle system in fluid communication with the liquid air pump, a CCNG storage vessel; and a natural gas scrubber; and a natural gas pipeline in fluid communication with the natural gas scrubber.
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이 특허에 인용된 특허 (10)
Wakana, Harumi; Chino, Koichi; Yokomizo, Osamu, Cold heat reused air liquefaction/vaporization and storage gas turbine electric power system.
Hoskinson ; deceased Robert L. (late of Pacific Palisades CA by Violet Vivian Hoskinson ; heir), Power conversion system utilizing reversible energy of liquefied natural gas.
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