Looking for breakthrough ideas for innovation challenges? Try Patsnap Eureka!

Separation method of cyclopentane and 2,2-dimethyl butane

A technology of dimethylbutane and separation method, applied in the field of separation of cyclopentane, can solve the problem that cyclopentane and 2,2-dimethylbutane cannot be separated, are not suitable for industrial production, have a narrow operating range, etc. problem, to achieve the effect of high selectivity, good stability and low solvent ratio

Active Publication Date: 2019-06-04
CHAMBROAD CHEM IND RES INST CO LTD
View PDF3 Cites 3 Cited by
  • 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

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
View more

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0014] The composition of the mixed material is: 5.2569%wt of 2,2-dimethylbutane and 94.7431%wt of cyclopentane.

[0015] Weigh a certain amount of the binary mixture and acetonitrile to carry out extractive distillation experiments, wherein the mass ratio of the mixture to acetonitrile is 1:6, the operating pressure of the extractive distillation column is controlled to be 102KPa, the reflux ratio is 70, and the temperature at the bottom of the column is 70°C. A rich solvent containing cyclopentane was obtained at the bottom; analysis experiments were carried out on the rich solvent, and the operating pressure of the analysis tower was controlled to be 110KPa, the reflux ratio was 3.5, and the temperature at the bottom of the tower was 75°C to obtain a refined cyclopentane product with a purity of 99.9%.

Embodiment 2

[0017] The composition of the mixed material is: 8.6571%wt of 2,2-dimethylbutane and 91.3429%wt of cyclopentane.

[0018] Weigh a certain amount of the mixture and acetonitrile to carry out extractive distillation experiments, wherein the mass ratio of the mixture to acetonitrile is 1:8, the operating pressure of the extractive distillation tower is controlled to be 115KPa, the reflux ratio is 55, the temperature at the bottom of the tower is 78°C, and the bottom of the tower is obtained A rich solvent containing cyclopentane; the analysis experiment was carried out on the rich solvent, and the operating pressure of the analysis tower was controlled at 115KPa, the reflux ratio was 5.5, and the temperature at the bottom of the tower was 78°C to obtain a refined cyclopentane product with a purity of 99.4%.

Embodiment 3

[0020] The composition of the mixed material is: 12.4598%wt of 2,2-dimethylbutane and 87.5402%wt of cyclopentane.

[0021] Take a certain amount of this mixture and acetonitrile to carry out extractive distillation experiment, wherein the mass ratio of the mixture to acetonitrile is 1:9, the operating pressure of the extractive distillation tower is controlled to be 120KPa, the reflux ratio is 45, the temperature at the bottom of the tower is 80°C, and the bottom of the tower is obtained A rich solvent containing cyclopentane; the analysis experiment was carried out on the rich solvent, and the operating pressure of the analysis tower was controlled to 102KPa, the reflux ratio was 6, and the temperature at the bottom of the tower was 70°C to obtain a refined cyclopentane product with a purity of 99.2%.

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
Login to View More

PUM

No PUM Login to View More

Abstract

The invention belongs to the technical field of chemical engineering. Efficient separation of cyclopentane and 2,2-dimethyl butane is realized by adopting an extractive distillation technology takingacetonitrile as an extracting agent. The cyclopentane / 2,2-dimethyl butane separation method adopts an extractive distillation process, which comprises an extractive distillation process and a desorption process; acetonitrile is used as an extraction agent, a cyclopentane / 2,2-dimethyl butane mixture is fed into the middle of an extractive distillation column in the extractive distillation process,the extraction agent is fed into the upper part of the extractive distillation column, the working pressure of the extractive distillation column is 102-120 kPa, the solvent ratio is 6-9, the reflux ratio is 45-70, and the column bottom temperature is 70-80 DEG C. The 2,2-dimethyl butane is obtained from the top of the column, and a rich solvent at the bottom of the column is subjected to desorption through a desorption column to obtain cyclopentane. The separation method is good in separation effect and high in cyclopentane purity (not less than 99%); the extraction agent is good in stability, high in selectivity, low in solvent ratio and low in boiling point. The method is simple in process flow, high in operation controllability and low in energy consumption; the extraction agent can berecycled, is low in pollution and is suitable for industrial production. The method is suitable for preparing high-quality cyclopentane.

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. The main substance that affects the purity of cyclopentane products is 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. In industry, the extraction method is commonly used to separate near-boiling systems. The extraction method requires experimental screening of extractants to improve the solubility of certain components in the system, while the solubility of other components is as low as possible. Extra...

Claims

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
Login to View More

Application Information

Patent Timeline
no application Login to View More
IPC IPC(8): C07C7/08C07C13/10C07C9/16
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
Features
  • Generate Ideas
  • Intellectual Property
  • Life Sciences
  • Materials
  • Tech Scout
Why Patsnap Eureka
  • Unparalleled Data Quality
  • Higher Quality Content
  • 60% Fewer Hallucinations
Social media
Patsnap Eureka Blog
Learn More