Process method and equipment for refining, extracting and distilling cyclopentane

A technology of extractive distillation and process method, which is applied in the field of cyclopentane refining extractive distillation process method and its equipment, which can solve the problems of low production performance of extraction equipment, large loss of cyclopentane, and inability to build too high, so as to improve market competitiveness and product added value, increase relative volatility, and ensure flexibility

Active Publication Date: 2012-03-28
BC P INC CHINA NAT PETROLEUM CORP +1
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  • Summary
  • Abstract
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  • Application Information

AI Technical Summary

Problems solved by technology

Solvent selection itself is not very difficult, because the polarity and molecular size of the cyclopentane / 2,2-dimethylbutane system are very similar, so it is difficult to find a high-efficiency extractant, and due to the cyclopentane / 2,2-dimethylbutane system The composition of pentane is already as high as 95.88%, so the amount of solvent used is extremely large, and the loss of cyclopentane product will also be large
At the same time, from the perspective of equipment efficiency, production experience and other operational aspects, the production performance of the extraction equipment is very low, and too tall towers cannot be built, so it is not suitable for the separation of the cyclopentane / 2,2-dimethylbutane system

Method used

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  • Process method and equipment for refining, extracting and distilling cyclopentane
  • Process method and equipment for refining, extracting and distilling cyclopentane
  • Process method and equipment for refining, extracting and distilling cyclopentane

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Embodiment 1

[0036] See Table 2 to Table 6.

[0037]The raw material 40°C crude cyclopentane (Table 1) enters the weight removal tower through the middle part of the feed pump, and after rectification, the gas phase cyclopentane at the top of the weight removal tower at about 58.6°C is condensed and cooled by the top condenser of the weight removal tower to 40°C enters the reflux tank at the top of the weight-removing tower; the liquid phase at 40°C in the reflux tank at the top of the weight-removing tower is pressurized to 0.2mpa by the reflux pump of the weight-removing tower, and then divided into two paths, one is returned to the reflux in the tower, and the other is used as the middle The product is sent to the extractive distillation tower; the liquid phase at the bottom of the de-weighting tower at about 70.3°C is drawn out and then heated to about 71.4°C by the reboiler of the de-weighting tower and then returned to the tower, and the heavy components of the liquid phase at the bot...

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Abstract

The invention relates to a process method and equipment for refining, extracting and distilling cyclopentane. The problem in the background art that the cyclopentane and a 2, 2-dimethylbutane system are difficult to effectively separate to influence the purity of a cyclopentane product is mainly solved. The equipment for refining, extracting and distilling the cyclopentane comprises an extracting and distilling tower (2) and a desorption tower (3), and a weight-removing tower (1) is additionally arranged in the front of the extracting and distilling tower (2). The process method for refining, extracting and distilling the cyclopentane adopts N, N-dimethyl formamide as an extracting agent in the extracting and distilling tower. By using the process method, two products, namely the cyclopentane and 2, 2-dimethylbutane can be effectively separated through an extractive distillation technique; the purity of a cyclopentane product is not less than 99.2% (mol percentage); the energy consumption of the towers is decreased; and the cyclopentane product with higher purity is produced.

Description

technical field [0001] The invention relates to an extractive distillation process and its equipment in the field of petrochemical industry, in particular to a cyclopentane refining extractive distillation process and its equipment. Background technique [0002] The purity of the cyclopentane produced by the cyclopentane plant of the fine chemical plant is low, which seriously restricts the market price of the product. The key component affecting the purity of cyclopentane product is 2,2-dimethylbutane. The atmospheric boiling points of cyclopentane (CP) and 2,2-dimethylbutane (22MB) are 49.25 and 49.74°C respectively, with a difference of 0.49°C, which belong to near-boiling systems. The linear relationship intersects at a temperature of 49.4°C and a composition of ~45 mol% to form an azeotrope. [0003] In industry, the extraction method is commonly used to separate the azeotropic system. The extraction method needs to screen the extractant experimentally to improve the ...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C07C13/10C07C7/08C07C7/00
Inventor 孙彦波胡刚黄泽娟高志茹陈光环冯桂权
Owner BC P INC CHINA NAT PETROLEUM CORP
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