Air separation system for generating liquid oxygen and liquid nitrogen

An air separation and vapor-liquid separator technology, applied in refrigeration and liquefaction, cold treatment separation, liquefaction and other directions, can solve the problems of large power consumption and increased energy consumption, and achieve the effect of large economic benefits and reduced energy consumption

Active Publication Date: 2007-09-12
HANGZHOU HANGYANG
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Problems solved by technology

However, the air separation process is usually carried out under low temperature conditions, and the low temperature environment (80 ~ 100K) is obtained by mechanical refrigeration driven by electricity. The generation of these cold quantities requires a large amount of electricity, especially when producing large amounts of liquid oxygen and liquid nitrogen. Energy consumption will increase significantly

Method used

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  • Air separation system for generating liquid oxygen and liquid nitrogen

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specific Embodiment approach

[0021] The present invention will be described in detail below in conjunction with accompanying drawing and specific embodiment:

[0022] Main heat exchanger (3), fractionation tower and liquid oxygen heat exchanger (10) are positioned at independent cold box I (1) inside, and fractionation tower is composed of fractionation lower tower (4), fractionation upper tower (6) and main condensation The evaporator (5) is connected to form.

[0023] The feed air (113) that removes carbon dioxide, water, acetylene and other hydrocarbon impurities is sent to the heat exchange channel (A1-A2) of the main heat exchanger (3) in the cold box I (1) to exchange heat with other The reflux gas in the channel exchanges heat, and after cooling down to a suitable fractionation temperature, it is sent to the bottom of the fractionation lower tower (4), and heat transfer occurs on the multi-layer tray with the reflux liquid flowing down from the top of the fractionation lower tower (4). and mass tr...

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Abstract

This kind of air separation system obtaining liquid oxygen and liquid nitrogen at least includes an air separator mainly consisting of a fractionating tower and at least includes an equipment for recovering cold energy of liquefied natural gas mainly consisting of an liquefied natural gas heat exchanger, which still includes main heat exchanger, liquid-oxygen heat exchanger and liquid-nitrogen liquid air subcooler; oxygen is drawn out from the underpart of the upper column on the fractionating tower, and cools and liquefied in the liquid-oxygen heat exchanger as the liquid oxygen products; after nitrogen from the top of the upper column passes through a liquid-nitrogen liquid air subcooler and is reheated by main heat exchanger, some nitrogen enters into liquefied-natural-gas heat exchanger to recool and exchange heat to become high pressure nitrogen through primary compression and pressurization at least. And through throttling expansion and air-liquid separator, nitrogen and liquid nitrogen participate in recycling and other nitrogen as liquid-nitrogen products; energy consumption is reduced notably after using actually, power consumption which produces liquid oxygen of 1kg is 0.39kwh, while the power consumption of the traditional equal air separator is 1.0 to 1.25kwh, which is 2.4 to 3 times than the separator. And it is easy to popularize and apply.

Description

technical field [0001] The invention relates to an air separation system for recovering the cooling capacity of liquefied natural gas to obtain liquid oxygen and liquid nitrogen, which is suitable for mass production of liquid oxygen, liquid nitrogen and argon fractions, and can greatly reduce the energy consumption of the air separation process. Background technique [0002] The main components of air are nitrogen and oxygen, and it is an inexhaustible source of industrial production of nitrogen and oxygen. Oxygen is mainly used as an oxidant in metallurgy, gas-supporting, medical treatment, wastewater treatment and chemical industry. Nitrogen is mainly used for ammonia synthesis, protective atmosphere for metal heat treatment, inert protective gas in chemical production (pipeline purge when starting and stopping, nitrogen seal for easily oxidized substances, pressing materials), grain storage, fruit preservation and electronic industry, etc. The traditional method of sepa...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): F25J3/04
CPCF25J1/0045F25J1/0015F25J1/0234F25J3/0406F25J2250/50F25J1/004F25J3/04351F25J3/04412F25J2250/42F25J1/0292F25J2210/62F25J1/0224F25J2230/60F25J2230/08F25J3/0423F25J3/04224F25J3/04272
Inventor 卢杰毛绍融朱朔元何晖
Owner HANGZHOU HANGYANG
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