Freezing expansion type chlorine liquefying method

A technology of chlorine gas and liquefier, which is applied in the chemical industry, can solve the problems of the earth's biological living environment hazards, susceptibility to sulfuric acid pollution, and lower energy-saving effects, and achieve the effects of avoiding sulfuric acid pollution of products, protecting the living environment, and reducing the risk of explosions

Active Publication Date: 2013-11-27
杭州求是透平机制造有限公司
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  • Claims
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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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  • Freezing expansion type chlorine liquefying method

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Embodiment Construction

[0022] The present invention will be further described below in conjunction with the accompanying drawings and embodiments.

[0023] like figure 1 As shown, the equipment used in a freeze-expansion chlorine gas liquefaction method includes a turbine chlorine gas compressor unit 1, a pressurized expansion unit 2, a first cooling pipe 3, a brake cooler 4, a precooler 5, and a main chlorine gas liquefaction unit. Device 6, main gas-liquid separator 7, liquid chlorine storage tank 8, auxiliary chlorine gas liquefier 9, auxiliary gas-liquid separator 10, second cooling pipe 11, third cooling pipe 12, tail chlorine distribution table 13, fourth cooling Pipe 14 and refrigerating unit 15.

[0024] The booster expansion unit 2 includes a booster brake fan 2-1, an expander 2-2 and a drive shaft 2-3, and the drive shaft 2-3 passes between the booster brake fan 2-1 and the expander 2-2 connect.

[0025] The input end of the turbine-type chlorine gas compressor unit 1 is open, and the o...

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Abstract

The invention discloses a freezing expansion type chlorine liquefying method. A conventional chlorine liquefying device can explode or pollute the environment easily. An output end of a turbine type chlorine compression unit is connected with an input end of a main gas-liquid separator through a pressurization brake fan, a brake cooler, a precooler and a main chlorine liquefier; an output end of the main gas-liquid separator is connected with an input end of an auxiliary gas-liquid separator through an auxiliary chlorine liquefier; and an output end of the auxiliary chlorine liquefier is connected with an input end of a tail chlorine distribution platform through an expansion machine, a second cooling pipe and a third cooling pipe. The method specifically comprises the steps as follows: the turbine type chlorine compression unit and the pressurization brake fan pressurize a chlorine raw material; the brake cooler, the precooler and the main chlorine liquefier cool chlorine; the main gas-liquid separator separates a gas-liquid mixture; the auxiliary chlorine liquefier performs secondary cooling of the chlorine; and the auxiliary gas-liquid separator performs secondary separation of the gas-liquid mixture. The freezing expansion type chlorine liquefying 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 a freeze-expansion 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-...

Claims

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Application Information

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