Method and device for preparing liquid CO2 (carbon diode) by cold energy of LNG (liquefied natural gas)

A liquid carbon dioxide and dry ice technology, applied in refrigeration and liquefaction, liquefaction, lighting and heating equipment, etc., can solve the problems of low energy consumption of the system, not involving full utilization of LNG gasification cooling energy, etc., to achieve low energy consumption and utilization rate High and stable effect

Active Publication Date: 2014-12-24
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

AI Technical Summary

Problems solved by technology

[0005] None of the above prior art involves making full use of the cold energy of LNG gasification and liquid CO with low system energy consumption. 2 and dry ice preparation technology

Method used

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  • Method and device for preparing liquid CO2 (carbon diode) by cold energy of LNG (liquefied natural gas)
  • Method and device for preparing liquid CO2 (carbon diode) by cold energy of LNG (liquefied natural gas)

Examples

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Embodiment 1

[0032] Refer to attached figure 1 , a process for preparing liquid carbon dioxide and dry ice by using the cold energy of LNG, comprising the following steps: turn on the low-temperature LNG pump 2, LNG at 120kg / h and -162°C is output from the LNG storage tank 1, and enters the shell-and-tube exchange through the LNG pump 2 Heater 3 with 200 kg / h, -40°C, 0.6MPa of CO 2 Heat exchange, LNG through the tube, CO 2 On the shell side, LNG heats up and gasifies into low-temperature gaseous natural gas, then enters the low-temperature natural gas heating channel of the multi-flow plate-fin heat exchanger 4, heats up to a normal temperature of 25°C, and enters the downstream pipeline network to supply gas user. 150 kg / h 25℃, 0.1MPa CO 2 The raw material gas enters the CO of the multi-flow plate-fin heat exchanger 4 2 Raw material gas cooling channel, heat exchange and cooling to -40°C low-temperature CO 2 , into the first compressor 5 after being compressed, the temperature rises,...

Embodiment 2

[0038] Refer to attached figure 1 , a process for preparing liquid carbon dioxide and dry ice by using the cold energy of LNG, comprising the following steps: turn on the low-temperature LNG pump 2, LNG at 140kg / h and -162°C is output from the LNG storage tank 1, and enters the shell-and-tube type exchange through the LNG pump 2 Heater 3 with CO at 200 kg / h, -30°C, 1.0MPa 2 Heat exchange, LNG through the tube, CO 2 On the shell side, LNG heats up and gasifies into low-temperature gaseous natural gas, then enters the low-temperature natural gas heating channel of the multi-flow plate-fin heat exchanger 4, heats up to a normal temperature of 25°C, and enters the downstream pipeline network to supply gas user. 155 kg / h 25°C, 0.1MPa CO 2 The raw material gas enters the CO of the multi-flow plate-fin heat exchanger 4 2 Raw material gas cooling channel, heat exchange and cooling to -30°C low-temperature CO 2 , into the first compressor 5 after being compressed, the temperature ...

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Abstract

The invention discloses a method and a device for preparing liquid CO2 (carbon diode) by cold energy of LNG (liquefied natural gas). The method comprises the following steps of pumping the LNG into a tube of a shell-and-tube heat exchanger, releasing the potential heat of the LNG in the tube of the shell-and-tube heat exchanger, cooling and liquefying the lower-temperature gaseous CO2, sending the gasifying byproduct of the LNG as a cold source into a multi-strand flow plate fin type heat exchanger, cooling the raw CO2, then sending into a CO2 compressor, cooling the outputted high-pressure and high-temperature CO2, raising the temperature of the LNG, and gasifying the LNG into the normal-temperature natural gas with the temperature of 10-20 DEG C; sending the cooled CO2 into a shell of the shell-and-tube heat exchanger, dividing the liquid CO2 flowing from an outlet of the shell of the shell-and-tube heat exchanger into two branches, sending one branch into a liquid CO2 storage tank, and sending the other branch into a dry ice machine to prepare carbon dioxide ice. The method has the advantages that the gradient utilization of the cold energy of the LNG is realized, and the utilization rate of the cold energy of the LNG is high; the preparation pressure of the liquid CO2 and the carbon dioxide ice is decreased to 0.6-1.0MPa by the cold energy of the LNG, the gaseous CO2 at the inlet of the compressor is cooled to the temperature of -40 to -30 DEG C, and finally the effect of saving the energy by more than 58% is realized in comparison with the effect of the common low pressure method.

Description

technical field [0001] The invention relates to the field of preparation of liquid carbon dioxide and dry ice, in particular to a process and a device for preparing liquid carbon dioxide and dry ice by utilizing cold energy of LNG. Background technique [0002] In recent years, my country's liquefied natural gas (LNG) market has developed rapidly, and in 2013 it reached an annual LNG import volume of about 18 million tons. Usually, at the LNG receiving station or satellite station, it is necessary to convert LNG into gaseous natural gas (NG for short) through heat exchange and temperature rise. Aiming at the cold energy released during the gasification process of LNG, many researchers have carried out relevant research, such as the use of LNG cold energy in air separation, cold storage and ice making. Therefore, the development of new LNG cold energy application fields has positive significance for enhancing the flexibility of LNG cold energy utilization projects and reduci...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): F25J1/00F25J5/00
Inventor 徐文东赵建河程显弼袁丹
Owner 佛山市寰晟通新能源科技有限公司
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