Low-energy consumption nitrogen production method and apparatus

A low energy consumption, nitrogen technology, applied in refrigeration and liquefaction, nitrogen purification/separation, lighting and heating equipment, etc., can solve the problem of unsatisfactory energy consumption of air separation equipment, so as to avoid the increase of air humidity and reduce the humidity The effect of increasing the amount and improving the extraction rate

Active Publication Date: 2009-07-29
四川空分设备(集团)有限责任公司
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Problems solved by technology

With these methods and process organization, the energy consumption of the air separation plant cannot meet the user's requirements

Method used

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  • Low-energy consumption nitrogen production method and apparatus

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Embodiment Construction

[0023] The present invention will be described in further detail below in conjunction with the accompanying drawings and specific embodiments. However, it should not be construed that the scope of the above-mentioned subject matter of the present invention is limited to the following examples.

[0024] As shown in the figure, the nitrogen production process of the present invention is as follows:

[0025] a) The compressed and purified air is introduced into the heat exchanger E1, and is cooled to close to the liquefaction temperature by the return gas such as low-pressure oxygen-enriched, nitrogen and pressure-enriched oxygen in the heat exchanger through the pipeline;

[0026] b) The cooled air is sent to the rectification tower C1, where heat and mass transfer is carried out on the tray or packing from bottom to top in the rectification tower and the liquid from top to bottom. Different forms of rectification. Nitrogen is obtained at the top of the tower; oxygen-enriched ...

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Abstract

The invention relates to a method and a device for preparing nitrogen in low energy consumption. The method comprises that: the nitrogen is obtained on the top of a rectifying tower after the air is cooled, and one part of the nitrogen is condensed into liquid nitrogen, wherein one part of the liquid nitrogen is taken as a product liquid nitrogen and the rest liquid nitrogen is taken as a backflow liquid to return the top of the tower; the other part of the nitrogen enters a heat exchanger, is heated again to normal temperature and pressurized by a pressure-increasing end of an expander, and is sent into a user nitrogen conveying pipe network; the liquid air rich in oxygen is obtained on the bottom of the tower, enters the heat exchanger, is supercooled by cold fluid and throttled, and enters a condenser / evaporator as a cold source to carry out heat exchange with the nitrogen; the vaporized air rich in oxygen enters the heat exchanger, is heated again, and enters the expander for expansion refrigeration; and the low-pressure air rich in oxygen after the expansion enters the heat exchanger, and is heated again and led out. The method increases the pressure of the nitrogen through work outputted by the expansion of the air rich in oxygen, and reduces pressure discharge of a compressor so as to reduce energy consumption; the liquid air is subjected to heat exchanging and supercooling by various cold fluid such as the low-pressure air rich in oxygen, the nitrogen, the pressurized air rich in oxygen, and the like, so the humidity content of the air is reduced to improve extraction yield, the energy consumption is reduced by 15 to 23 percent, the water consumption is reduced by 14 to 22 percent, and the economic benefit is significant.

Description

technical field [0001] The invention relates to a method and device for producing nitrogen with greatly reduced energy consumption. Background technique [0002] With the rapid development of emerging photoelectric industry and special petrochemical industry, etc., the demand for nitrogen products is increasing. The air separation equipment for nitrogen production is a large energy consumer. Due to long-term operation, how to effectively reduce energy consumption is very important. . The nitrogen pressure is high, the oxygen-enriched amount is large, and the output power can be considerable when fully expanded and utilized. At present, the general practice is to partially expand and the rest to be throttled. Cold or subcooled by simple heat exchange with only part of the fluid. With these methods and process organization, the energy consumption of the air separation plant cannot meet the user's requirements. Contents of the invention [0003] The technical problem to be...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C01B21/04
CPCF25J3/0403F25J3/0423F25J3/04236F25J3/04284F25J3/04381F25J3/044F25J3/04769F25J2200/72
Inventor 黄震宇李传明杨斌刘厚荣
Owner 四川空分设备(集团)有限责任公司
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