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Separation of Methyl Chloride and Ethyl Chloride by Throttle Expansion

A throttling expansion and methyl chloride technology, which is applied in the disproportionation separation/purification of halogenated hydrocarbons, chemical instruments and methods, and the preparation of halogenated hydrocarbons, can solve the problems of large discharge of three wastes, low product purity, and complicated processes. Achieve the effect of reducing separation cost, short process flow and simple operation

Inactive Publication Date: 2016-11-30
HUAIYIN TEACHERS COLLEGE +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

However, due to the similar properties of the components of methyl chloride and ethyl chloride, the purity of the product obtained by the former adsorption separation method is not high, and the process is too complicated; the latter rectification separation method requires large investment in equipment, high energy consumption, and large discharge of three wastes

Method used

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  • Separation of Methyl Chloride and Ethyl Chloride by Throttle Expansion
  • Separation of Methyl Chloride and Ethyl Chloride by Throttle Expansion

Examples

Experimental program
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Effect test

Embodiment 1

[0025] Example 1: Take 100 kg of mixed gas raw material of methyl chloride and ethyl chloride for separation. The molar ratio of ethyl chloride to methyl chloride (based on methyl chloride-the following is abbreviated) is measured to be 0.001, and the raw materials enter the cooling and cooling device to be cooled to 0°C; the cooled mixture raw materials are sent to the first stage through the compressor Flow expansion device-sieve plate throttling expander (see figure 2 -The following is omitted), the cross-sectional area of ​​the selected sieve is 0.03 cm 2 The sieve plate 1 (the icon number is omitted below), the blind plate 2 (the icon number is omitted) is adjusted by the blind plate shift handle 3 (the icon number is omitted) to overlap the area covered by the sieve plate to control the flow in and out of the sieve plate. The pressure difference of the device is 0.1 MPa, and the collected liquid ethyl chloride is 0.12 kg and the gaseous methyl chloride is 98.1 kg. The yi...

Embodiment 2

[0026] Embodiment 2: Take 100 kg of mixed gas raw materials of methyl chloride and ethyl chloride for separation. It is determined that the molar ratio of ethyl chloride to methyl chloride is 0.01, and the raw material enters the cooling device to cool down to 5°C; the cooled mixture raw material is sent to the first-stage throttling expansion device-sieve plate throttling expander through the compressor , The cross-sectional area of ​​the selected sieve is 0.5cm 2 The sieve plate is adjusted by the blind plate shift handle to adjust the area of ​​the blind plate superimposed on the sieve plate, and the pressure difference between the fluid entering and leaving the sieve plate throttling expander is controlled to be 0.4 MPa. The collected liquid ethyl chloride and gaseous chlorine are 1.19 kg Methane was 96.9 kg, and the yields of the two were 94.4% and 98.1%, respectively; after testing, the purity of liquid ethyl chloride and gaseous methyl chloride were 99.9% and 99.8%, respe...

Embodiment 3

[0027] Embodiment 3: Take 100 kg of mixed gas raw material of methyl chloride and ethyl chloride for separation. It is determined that the molar ratio of ethyl chloride to methyl chloride is 0.1, and the raw material enters the cooling and cooling device to be cooled to 10°C; the cooled mixture raw material is sent to the first-stage throttling expansion device-sieve plate throttling expander through the compressor , The cross-sectional area of ​​the selected sieve is 3 cm 2 The sieve plate is adjusted by the blind plate shift handle to adjust the area of ​​the blind plate superimposed on the sieve plate, and the pressure difference between the fluid entering and exiting the sieve plate throttling expander is 0.8 MPa, and 10.9 kg of liquid ethyl chloride and 10.9 kg of gaseous chlorine are collected. The methane is 87.1 kg, and the yields of the two are 96.2% and 98.2% respectively; after testing, the purity of liquid ethyl chloride and gaseous methyl chloride are 99.8% and 99.7...

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Abstract

The invention relates to a technology for separation of a chloromethane and chloroethane mixture by a throttling expansion method. According to the technology, the process route is designed according to the properties of chloromethane and chloroethane, and separation is realized through coupling a low-temperature cooling system, a first-stage throttling expansion system and a second-stage throttling expansion system. The technology comprises the following specific steps: high-temperature chloromethane and chloroethane mixed gas serves as a raw material and is firstly subjected to cooling treatment, and then, a low-temperature gaseous mixture is subjected to a throttling expansion separating process; the separation of chloromethane and chloroethane is completed through first-stage throttling expansion or the separation of chloroethane and chloromethane is completed through first-stage throttling expansion separation and then second-stage throttling expansion according to the volumetric content ratio of gaseous chloroethane and chloromethane in the raw material. According to the technology, the process flow is brief, and the operation is simple; the obtained products, i.e., liquid-state chloroethane and gaseous chloromethane are high in purity; the processing equipment investment is small, the energy consumption is low, and the separating cost is greatly reduced, so that industrial application is facilitated; and the overall system is free of discharge of waste gases, waste water and waste residues, so that the requirements on environment-friendly sustainable development are met.

Description

Technical field [0001] The invention relates to a separation technology of a mixture of methyl chloride and ethyl chloride, in particular to a process technology for separating a mixture of methyl chloride and ethyl chloride by a throttling expansion method. Background technique [0002] Chloromethane is an important raw material for organic compounds such as methylchlorosilane, cellulose esters, quaternary ammonium compounds, herbicides, etc. It is also a polymerization solvent used in the production of butyl rubber. It is an important methylating agent with a boiling point of -23.7 °C, it is toxic, colorless, and has the smell of ether and volatile characteristics. Ethyl chloride is a widely used organic solvent. It can be used as anesthetics, insecticides, refrigerants, or used to make tetraethyl lead, ethyl cellulose, dye intermediates (hydroxydiethyl aniline) and dyes. It can be used as an inhibitor of ethylene oxide reaction, with low toxicity, boiling point of 12.5°C, and...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C07C19/03C07C19/043C07C17/38C07C17/389
Inventor 褚效中钱怀国赵宜江徐继明程志鹏徐睿张维光周守勇贝宗军郑学文吕宇
Owner HUAIYIN TEACHERS COLLEGE