The patent badge is an abbreviated version of the USPTO patent document. The patent badge does contain a link to the full patent document.

The patent badge is an abbreviated version of the USPTO patent document. The patent badge covers the following: Patent number, Date patent was issued, Date patent was filed, Title of the patent, Applicant, Inventor, Assignee, Attorney firm, Primary examiner, Assistant examiner, CPCs, and Abstract. The patent badge does contain a link to the full patent document (in Adobe Acrobat format, aka pdf). To download or print any patent click here.

Date of Patent:
May. 02, 2017

Filed:

Nov. 06, 2012
Applicant:

Yingjin Yuan, Tianjin, CN;

Inventors:

Minhua Zhang, Tianjin, CN;

Xiuqin Dong, Tianjin, CN;

Cheng Liu, Tianjin, CN;

Minli Tao, Tianjin, CN;

Yonghui Li, Tianjin, CN;

Huisheng Lv, Tianjin, CN;

Yingzhe Yu, Tianjin, CN;

Zhongfeng Geng, Tianjin, CN;

Assignee:

Tianjin University, Tianjin, CN;

Attorneys:
Primary Examiner:
Assistant Examiner:
Int. Cl.
CPC ...
B01D 53/18 (2006.01); B01D 53/14 (2006.01); C07C 7/11 (2006.01);
U.S. Cl.
CPC ...
B01D 53/1406 (2013.01); B01D 53/1418 (2013.01); B01D 53/1487 (2013.01); B01D 53/1493 (2013.01); B01D 53/185 (2013.01); C07C 7/11 (2013.01); B01D 2252/103 (2013.01); B01D 2252/205 (2013.01); B01D 2252/50 (2013.01); B01D 2252/504 (2013.01); B01D 2256/24 (2013.01);
Abstract

The present invention discloses a method and a device for recovering ethylene during the process for producing vinyl acetate, wherein a double solvent absorption method composed of an absorbent solution and deionized water is adopted. The method is as follows: introducing an outlet stream as an absorbent solution from the upper section of the feeding plate in an acetic acid tower during the rectification stage of vinyl acetate production; delivering same to the top of the lower section of the ethylene recovery tower by a delivery pump; charging refined gas from the tower bottom of the ethylene recovery tower for contacting with the absorbent solution in a counter-current; delivering the absorption bottom solution to the rectification stage for treatment; the gas continuing to rise to the upper section of the ethylene recovery tower and contacting with the deionized water introduced from the top of the tower in a counter-current; absorbing and removing the acetic acid therein; and discharging the residual inert gas, such as N2, from the top of the ethylene recovery tower. The absorbent solution is a mixture of acetic acid, vinyl acetate and water, and comprises by weight percentage of 50-85% acetic acid, 5-30% vinyl acetate and 5-20% water.


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