Method for preparing cyclopentane refrigerant

A refrigerant and cyclopentane technology, applied in chemical instruments and methods, purification/separation of hydrocarbons, hydrocarbons, etc., can solve the problem that cyclopentane and 2,2-dimethylbutane cannot be separated and are not applicable Industrial production, narrow operating range, etc., to achieve the effect of high selectivity, good stability, and low solvent ratio

Active Publication Date: 2019-06-21
CHAMBROAD CHEM IND RES INST CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The extraction process requires a high ratio of solvent to oil, and the extraction agent is easy to deteriorate. The deteriorated extraction agent is not regenerated, resulting in a large waste of solvent, serious pollution, high environmental pressure, and high energy consumption.
[0004] Chinese patent CN201510532233.0 reports a method for separating cyclopentane and 2,2-dimethylbutane, which is realized by utilizing the azeotropic characteristics of 2,2-dimethylbutane and dichloromethane The separation of cyclopentane and 2,2-dimethylbutane does not consider that cyclopentane and dichloromethane will also form a binary azeotrope, so it is necessary to strictly control cyclopentane, 2,2-dimethylbutane The ratio of alkane and dichloromethane has a narrow operable range. If the composition of raw materials changes slightly, cyclopentane and 2,2-dimethylbutane may not be separated, which is not suitable for industrial production.

Method used

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  • Method for preparing cyclopentane refrigerant
  • Method for preparing cyclopentane refrigerant
  • Method for preparing cyclopentane refrigerant

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0018] The composition of raw materials is as follows:

[0019]

[0020] Weigh 1000g of raw oil to remove n-pentane and isopentane components under the conditions of operating pressure of 102KPa, reflux ratio of 4.5, and tower bottom temperature of 65°C, and then remove n-pentane and isopentane components at an operating pressure of 110KPa and a reflux ratio of 12 , under the condition that the temperature at the bottom of the tower is 78°C, the carbon six components are removed, and the main components are a mixture of cyclopentane and 2,2-dimethylbutane, and the purity of cyclopentane is 90.1%; controlled extractive distillation The operating pressure of the tower is 102KPa. Weigh a certain amount of the mixture and acetonitrile to carry out extractive distillation experiment, wherein the mass ratio of the mixture to acetonitrile is 1:6, the reflux ratio is 70, the temperature at the bottom of the tower is 70°C, and the mixture containing cyclopentane is obtained at the bo...

Embodiment 2

[0022] The composition of raw materials is as follows:

[0023]

[0024] Weigh 1000g of feedstock oil to remove n-pentane and isopentane components under the conditions of operating pressure of 110KPa, reflux ratio of 4, and tower bottom temperature of 68°C, and then remove n-pentane and isopentane components at an operating pressure of 102KPa and a reflux ratio of 9 , under the condition that the temperature at the bottom of the tower is 75°C, the C6 components are removed, and the main components are a mixture of cyclopentane and 2,2-dimethylbutane, and the purity of cyclopentane is 91.2%; controlled extractive distillation The operating pressure of the tower is 115KPa. Weigh a certain amount of the mixture and acetonitrile for extractive distillation experiment, wherein the mass ratio of the mixture to acetonitrile is 1:8, the reflux ratio is 55, the temperature at the bottom of the tower is 78°C, and the mixture containing cyclopentane is obtained at the bottom of the to...

Embodiment 3

[0026] The composition of raw materials is as follows:

[0027]

[0028] Weigh 1000g of raw oil to remove n-pentane and isopentane components under the conditions of operating pressure of 120KPa, reflux ratio of 5, and tower bottom temperature of 75°C, and then remove n-pentane and isopentane components at an operating pressure of 115KPa and a reflux ratio of 11 , under the condition that the temperature at the bottom of the tower is 80°C, the carbon six components are removed, and the main components are a mixture of cyclopentane and 2,2-dimethylbutane, and the purity of cyclopentane is 92.3%; controlled extractive distillation The operating pressure of the tower is 120KPa. Weigh a certain amount of the mixture and acetonitrile to carry out the extractive distillation experiment, wherein the mass ratio of the mixture to acetonitrile is 1:9, the reflux ratio is 45, the temperature at the bottom of the tower is 80°C, and the mixture containing cyclopentane is obtained at the ...

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Abstract

The invention belongs to the technical field of chemicals and discloses a method for preparing a cyclopentane refrigerant. Efficient separation of cyclopentane from 2,2-dimethyl butane is achieved byusing an extraction distillation technique with acetonitrile as an extraction agent. The method for preparing the cyclopentane refrigerant comprises the following steps: by taking a C5 mixture as a raw material, carrying out light component desorption, heavy component desorption, extraction distillation and desorption; by taking acetonitrile as an extraction agent, feeding a material from the topof a heavy component desorption tower into the middle part of an extraction distillation tower; feeding the extraction agent into the upper part of the extraction distillation tower, collecting 2,2-dimethyl butane from the top of the tower, and desorbing an enriched solvent at the bottom of the tower in a desorption tower, thereby obtaining the cyclopentane refrigerant. By adopting the method forpreparing the cyclopentane refrigerant, the obtained cyclopentane has purity not less than 99%, and is low in water content. The extraction agent is good in stability, high in selectivity, low in solvent ratio, low in boiling point, simple in process procedure, high in operation controllability, low in energy consumption, high in product purity, possible in extraction agent circulation, small in pollution and applicable to industrial production. The method is applicable to preparation of high-quality cyclopentane, and is particularly applicable to preparation of cyclopentane refrigerants of environmental-friendly refrigerators.

Description

technical field [0001] The invention belongs to the technical field of chemical industry and relates to material separation and purification technology, in particular to the separation technology of cyclopentane. Background technique [0002] Cyclopentane is an environmentally friendly refrigerant that can be used to replace chlorofluorocarbons. It is also an excellent polyurethane foaming agent with a good market prospect. In the C5 mixed raw material, the main substance that affects the purity of the cyclopentane product is 2,2-dimethylbutane, so the key point of the problem is the separation of cyclopentane and 2,2-dimethylbutane. The cyclopentane / 2,2-dimethylbutane system is a near-boiling system with a difference of only 0.4°C in boiling points. It is difficult to obtain more than 99% cyclopentane monomer through ordinary distillation. In industry, the extraction method is commonly used to separate near-boiling systems. The extraction method requires experimental scree...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C07C7/00C07C7/08C07C7/13C07C13/10
Inventor 杨颖张凤崎王启超吴文雷侯晓锋苏鹏飞史会兵
Owner CHAMBROAD CHEM IND RES INST CO LTD
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