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:
Aug. 30, 2022

Filed:

Aug. 28, 2020
Applicant:

China University of Petroleum-beijing, Beijing, CN;

Inventors:

Chunmao Chen, Beijing, CN;

Zhichang Liu, Beijing, CN;

Zhongjin Yi, Beijing, CN;

Rui Zhang, Beijing, CN;

Jiahao Liang, Beijing, CN;

Xianghai Meng, Beijing, CN;

Haiyan Liu, Beijing, CN;

Chunming Xu, Beijing, CN;

Qinghong Wang, Beijing, CN;

Attorney:
Primary Examiner:
Int. Cl.
CPC ...
C02F 9/00 (2006.01); C02F 11/122 (2019.01); C04B 5/00 (2006.01); C02F 11/16 (2006.01); B01J 19/20 (2006.01); C02F 11/13 (2019.01); C10G 53/04 (2006.01); C02F 11/12 (2019.01); C02F 1/52 (2006.01); C02F 1/56 (2006.01); C02F 1/66 (2006.01); C02F 11/127 (2019.01); C02F 1/00 (2006.01); C02F 103/36 (2006.01); C02F 11/121 (2019.01);
U.S. Cl.
CPC ...
B01J 19/20 (2013.01); C02F 9/00 (2013.01); C02F 11/12 (2013.01); C02F 11/122 (2013.01); C02F 11/13 (2019.01); C04B 5/00 (2013.01); C10G 53/04 (2013.01); C02F 1/5281 (2013.01); C02F 1/56 (2013.01); C02F 1/66 (2013.01); C02F 11/121 (2013.01); C02F 11/127 (2013.01); C02F 11/16 (2013.01); C02F 2001/007 (2013.01); C02F 2103/365 (2013.01); C10G 2300/1003 (2013.01); C10G 2300/205 (2013.01); C10G 2300/701 (2013.01);
Abstract

A method and a system for treatment of a spent chloroaluminate ionic liquid catalyst and an alkaline wastewater, where the method includes: 1) mixing the catalyst with a concentrated brine for hydrolysis reaction until residual activity of the catalyst is completely eliminated, to obtain an acidic hydrolysate and an acid-soluble oil; 2) mixing the acidic hydrolysate with an alkaline solution containing the alkaline wastewater for neutralization reaction until this reaction system becomes weak alkaline, to obtain a neutralization solution; 3) fully mixing the neutralization solution with a flocculant, carrying out sedimentation and separation, collecting the concentrated brine at an upper layer for reuse in the hydrolysis reaction, and collecting concentrated flocs at a lower layer; 4) dehydrating the concentrated flocs to obtain concentrated brine for reuse into the hydrolysis reaction, and collecting a wet solid slag; and 5) drying the wet solid slag to obtain a dry solid slag.


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