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Heat exchanging method of liquid natural gas cold energy used for high-temperature-level cold energy user

A technology of liquefied natural gas and heat method, which is applied in applications, household appliances, household refrigeration devices, etc., can solve the problems of large investment in civil engineering, difficulties in detection and control, and large demand for refrigerants, etc., to reduce equipment investment and land occupation Large area, good operating flexibility, good safety effect

Active Publication Date: 2015-07-01
佛山市寰晟通新能源科技有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

The invention patent solves the above-mentioned problems such as high requirements for equipment, large floor space, large demand for refrigerant, and large investment in civil engineering. However, the circulation device is not sensitive to pressure and faces problems such as pressure leakage, detection and control difficulties, etc.

Method used

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Embodiment

[0042] LNG heavy-duty trucks are supplied with gas in the form of on-board LNG bottles. At present, when the cooling capacity is 3kW, it can meet the cooling needs of most heavy-duty LNG vehicles. It is known that the total liquefaction pressure of R404A at 0°C is about 6.4 bar, so the total system pressure P is set to 6.4 bar in this example; when the required cooling capacity is 3kW, the temperature of R404A during the heat exchange between R404A and LNG is given by During the change process from 10°C to 0°C, the mass flow rate of R404A calculated by Aspen simulation is about 62kg / h. in such as figure 2 As shown, the LNG storage tank 1, the heater 6, the surge tank 7, and the engine 8 together form the original LNG gasification zone. The overlapping heat exchanger 3 is composed of two heat exchangers, each of which is a single shell-side double-tube heat exchanger; the lower heat exchanger of the overlapping heat exchanger 3 in this embodiment is an evaporation device. ...

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Abstract

The invention discloses a heat exchanging method of liquid natural gas (LNG) cold energy used for a high-temperature-level cold energy user. According to the method, in the process of LNG entering tube passes of the upper portions of heat exchangers from an LNG storage tank, heat exchanging is achieved among the LNG, first refrigerant and nitrogen added into shell passes of the upper portions of the heat exchangers, and the temperature rises; the LNG passes through an air vaporizer and enters a natural gas pipeline network after the temperature rises; on the upper portions of the heat exchangers, the temperature of the first refrigerant and the nitrogen coming out of a refrigerant storage tank decreases to -40 DEG C-0 DEG C after heat exchanging is performed among the first refrigerant, the nitrogen and the LNG, and the first refrigerant and the nitrogen come into a liquid phase from a gas phase and enter the lower portions of the heat exchangers; the pressure PB of the nitrogen is determined through the formula (6) shown in the specification; the cooled first refrigerant achieves heat exchanging with second refrigerant on the lower portions of the heat exchangers, the temperature of the first refrigerant rises, the first refrigerant comes into a gas phase from the liquid phase and returns to the upper portions of the heat exchangers, and therefore a cycle is completed. Through using the usage amount of the nitrogen for changing the partial pressure of the refrigerant, the sensitivity of system operation is improved while the freezing point of the first refrigerant is lowered, and safety and stability in the heat exchanging process are guaranteed.

Description

technical field [0001] The invention relates to a heat exchange method, in particular to a heat exchange method in which liquefied natural gas cold energy is used for high-temperature cold energy users, and belongs to the technical field of cold energy utilization. Background technique [0002] Liquefied natural gas (LNG, liquid natural gas) is a low-temperature liquid mixture formed by natural gas deacidification, dehydration, and freezing and liquefaction in a low-temperature process. The production process consumes a lot of energy. According to calculations, the gasification process of each ton of LNG is equivalent to releasing 830-860 megajoules of cold energy. If this part of cold energy is recovered, energy can be saved and huge economic benefits can be generated. At the same time, because the pollutant discharge during the development and utilization of LNG cold energy is zero, it is a kind of green energy. The current LNG cold energy utilization methods include low-...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): F25D3/10
CPCF25D3/10
Inventor 徐文东李俊丽许欢欢陈仲潘季荣
Owner 佛山市寰晟通新能源科技有限公司
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