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Expansion type chlorine liquefying method

A chlorine gas and liquefier technology, applied in the chemical industry, can solve the problems of environmental hazards on the earth, being susceptible to sulfuric acid pollution, reducing energy-saving effects, etc., so as to avoid sulfuric acid pollution of products, protect the living environment, and eliminate the danger of liquid chlorine explosion. Effect

Active Publication Date: 2013-11-27
杭州求是透平机制造有限公司
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  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The former is indirectly cooled by calcium chloride brine, but when liquid ammonia leaks into the system, nitrogen trichloride will be produced and when it accumulates to a certain level, it is easy to decompose and explode
The latter is a direct-cooling type, which is more energy-saving, but Freon will be banned globally in a few years, and production has been restricted at present, because Freon will destroy the ozone layer and cause harm to the living environment of the earth's organisms
The pressurization methods of the latter two methods mostly use sulfuric acid liquid ring compressors, the products are easily polluted by sulfuric acid, and the efficiency of liquid ring compressors is only 30%-40%, which reduces the energy saving effect

Method used

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  • Expansion type chlorine liquefying method

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Embodiment Construction

[0019] The present invention will be further described below in conjunction with the accompanying drawings and embodiments.

[0020] Such as figure 1 As shown, the equipment for an expansion chlorine liquefaction method includes a turbine chlorine compressor unit 1, a pressurized expansion unit 2, a brake cooler 3, a precooler 4, a chlorine liquefier 5, a gas-liquid separator 6, Liquid chlorine storage tank 7 and tail chlorine distribution platform 8.

[0021] The pressurized expansion unit 2 includes a pressurized braking fan 2-1, a main expander 2-2, a main shaft 2-3, a main shaft gear 2-4, an idler gear 2-5, a countershaft gear 2-6, and a countershaft 2 -7 and the tail chlorine expander 2-8; the supercharging brake fan 2-1 and the main expander 2-2 are connected through the main shaft 2-3, and the main shaft gear 2-4 is fixedly arranged on the main shaft 2-3, and the main shaft The gear meshes with the countershaft gear 2-6 through the idler gear 2-5, the countershaft gea...

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PUM

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Abstract

The invention discloses an expansion type chlorine liquefying method. A conventional chlorine liquefying device explodes and pollutes the environment easily. An output end of a turbine type chlorine compressor unit is connected with one end of a first cooling pipe through a pressurization braking fan; the other end of the first cooling pipe is connected with an input end of a precooler and an input end of a main expansion machine; an output end of the precooler is connected with an input end of a gas-liquid separator through a chlorine liquefier; an output end of the gas-liquid separator is connected with a tail chlorine distribution table through an tail chlorine expansion machine, a second cooling pipe and a third cooling pipe; and an output end of the main expansion machine is connected with an input end of the turbine type chlorine compressor unit through a fourth cooling pipe and a fifth cooling pipe. The method specifically comprises the steps as follows: the turbine type chlorine compressor unit and the tail chlorine distribution table pressurize raw material chlorine; a brake cooler, the precooler and the chlorine liquefier cool chlorine; and the gas-liquid separator separates a gas-liquid mixture. The method is safe, energy-saving and environment-friendly.

Description

technical field [0001] The invention belongs to the field of chemical industry, and in particular relates to an expansion type chlorine gas liquefaction method. Background technique [0002] At present, there are three commonly used methods for producing liquid chlorine in industrial production: the low-temperature and low-pressure method, the medium-temperature and medium-pressure method, and the high-temperature and high-pressure method. The safety degree of producing liquid chlorine in production decreases with the increase of pressure, but the energy consumption decreases accordingly. The cooling capacity required by the first two methods is provided by a refrigerator, and its refrigerants include liquid ammonia and Freon. The former is indirectly cooled by calcium chloride brine, but when liquid ammonia leaks into the system, nitrogen trichloride will be produced and when it accumulates to a certain level, it will easily decompose and explode. The latter is a direct-c...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): F25J1/02
Inventor 周国强杨金顺周音杨展彭振康朱荣声李啸
Owner 杭州求是透平机制造有限公司
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