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A system for multi-stage recovery and comprehensive utilization of LNG cold energy and its application method

A cold energy and refrigerant technology, applied in the field of LNG cold energy multi-stage recovery and comprehensive utilization system, can solve the problems of large heat transfer temperature difference, difficult utilization efficiency of LNG cold energy, and large loss of cold fire, etc., and achieve the goal of improving the comprehensive utilization rate Effect

Inactive Publication Date: 2016-02-17
北京天成山泉电子科技有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Due to the large release temperature span of LNG cold energy and the large difference in heat transfer temperature, the loss of cold energy is large, and it is difficult to improve the utilization efficiency of LNG cold energy. Generally, the utilization rate of LNG cold energy is only about 30%.

Method used

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  • A system for multi-stage recovery and comprehensive utilization of LNG cold energy and its application method

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Experimental program
Comparison scheme
Effect test

Embodiment 1

[0034] Such as figure 1 As shown, the LNG cold energy multi-stage recovery comprehensive utilization system provided by the present invention comprises:

[0035] 1), LNG composed of LNG storage tank 1, booster pump 2, first condenser 3, second condenser 8, first heat exchanger 13, second heat exchanger 16 and third expansion turbine 19 The main circuit of vaporization, heating and expansion is connected with the natural gas pipeline network or users;

[0036] 2), a first-stage Rankine cycle power generation unit composed of the first condenser 3, the first compressor 4, the first evaporator 5, the first expansion turbine 6 and the first generator 7;

[0037] 3), a second-stage Rankine cycle power generation unit composed of a second condenser 8, a second compressor 9, a second evaporator 10, a second expansion turbine 11 and a second generator 12;

[0038] 4), a low-temperature ice storage cooling unit composed of the first heat exchanger 13, the first circulation pump 14 an...

Embodiment 2

[0051] Such as figure 1 Shown, the using method of the LNG cold energy multistage recovery comprehensive utilization system of the present invention is as follows:

[0052] In the main loop of LNG vaporization, heating and expansion, the LNG output from the LNG storage tank 1 is pressurized by the booster pump 2 and sent to the first condenser 3, and in the first condenser 3, the LNG absorbs the heat of the refrigerant working medium 1 and vaporizes It is the saturated steam of natural gas, which enters the first heat exchanger 13 after absorbing the heat of the refrigerant working medium II in the second condenser 8, and in the first heat exchanger 13, the natural gas absorbs the heat of the refrigerant working medium III and continues to heat up , the heated natural gas enters the second heat exchanger 16, in the second heat exchanger 16 the natural gas absorbs the heat of the working medium water to heat up again, the heated natural gas enters the third expansion turbine 19...

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Abstract

The invention discloses a multi-level recovering and comprehensive utilization system of liquefied nature gas (LNG) cold energy and a using method thereof. The system comprises an LNG vaporization warming expansion main circuit, a primary rankine cycle power generation unit, a secondary rankine cycle power generation unit, a low-temperature ice-storage cooling unit, an LNG heating low-temperature heating unit and an expansion power generation unit. The LNG vaporization warming expansion main circuit is composed of an LNG storage tank (1), a pressurizing pump (2), a first condenser (3), a second condenser (8), a first heat exchanger (13), a second heat exchanger (16) and a third expansion turbine motor (19); the primary rankine cycle power generation unit is composed of the first condenser (3), a first compressor (4), a first evaporator (5), a first expansion turbine motor (6) and a first power generator (7); the secondary rankine cycle power generation unit is composed of the second condenser (8), a second compressor (9), a second evaporator (10), a second expansion turbine motor (11) and a second power generator (12); the low-temperature ice-storage cooling unit is composed of the first heat exchanger (13), a first circulation pump (14) and an ice storage tank (15); the LNG heating low-temperature heating unit is composed of the second heat exchanger (16), a second circulation pump (17) and a water heater (18); and the expansion power generation unit is composed of the third expansion turbine motor (19) and a third power generator (20).

Description

technical field [0001] The invention relates to the field of energy conversion and utilization, in particular to an LNG (liquefied natural gas) cold energy multi-stage recovery and comprehensive utilization system and a use method thereof. According to the vaporization characteristic curve of LNG, the system adopts a multi-stage recovery and comprehensive utilization method for LNG cold energy, which improves the recovery rate of LNG cold energy. Background technique [0002] With the country's increasing requirements for reducing carbon emissions and improving energy efficiency, my country's energy consumption structure will rely more on natural gas. In the future supply of natural gas, LNG from overseas will account for a large proportion. Whether it is LNG imported from overseas or LNG produced in my country, a large amount of cold energy is released during vaporization, generally 830-860kJ / kg. All countries in the world are trying to explore ways and methods to improve...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): F01K25/10F01D15/10F01K11/02F25D3/02
Inventor 廖品常付成山
Owner 北京天成山泉电子科技有限公司