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:
Nov. 10, 2020

Filed:

Aug. 28, 2018
Applicants:

China Petroleum & Chemical Corporation, Beijing, CN;

Sinopec Catalyst Co., Ltd., Beijing, CN;

Inventors:

Xiping Yin, Beijing, CN;

Ye Li, Beijing, CN;

Songyuan Gu, Beijing, CN;

Zhijian Liu, Beijing, CN;

Tao Wang, Beijing, CN;

Jin'ai Gao, Shandong, CN;

Yuhua Chen, Shandong, CN;

Yan Zhou, Shandong, CN;

Ling Yang, Shandong, CN;

Zhiwei Yuan, Beijing, CN;

Hongliang Yi, Beijing, CN;

Tao An, Shandong, CN;

Fuzu Liu, Shandong, CN;

Zhimin Zhang, Shandong, CN;

Shupeng Xu, Shandong, CN;

Hongqi Guo, Shandong, CN;

Attorneys:
Primary Examiner:
Int. Cl.
CPC ...
C02F 9/00 (2006.01); C02F 1/22 (2006.01); C02F 1/66 (2006.01); C02F 1/52 (2006.01); C02F 1/38 (2006.01); C02F 101/12 (2006.01); C02F 101/10 (2006.01); C02F 103/34 (2006.01); C02F 1/04 (2006.01); C02F 101/16 (2006.01); C02F 1/00 (2006.01); C02F 1/06 (2006.01);
U.S. Cl.
CPC ...
C02F 9/00 (2013.01); C02F 1/004 (2013.01); C02F 1/041 (2013.01); C02F 1/048 (2013.01); C02F 1/06 (2013.01); C02F 1/22 (2013.01); C02F 1/385 (2013.01); C02F 1/66 (2013.01); C02F 2001/5218 (2013.01); C02F 2101/101 (2013.01); C02F 2101/12 (2013.01); C02F 2101/16 (2013.01); C02F 2103/34 (2013.01); C02F 2301/046 (2013.01); C02F 2301/08 (2013.01);
Abstract

In a method for treating waste water containing ammonium salts, sodium sulfate crystal is obtained by freezing crystallization, then the pH value of the waste water is adjusted to a specific range, and next sodium chloride crystal and ammonia water is obtained by evaporation. Alternatively, the pH value of the waste water is adjusted to a specific range, then sodium chloride crystal and ammonia water is obtained by evaporation, and next sodium sulfate crystal is obtained by freezing crystallization. This method can recover ammonia, sodium sulfate, and sodium chloride from the waste water.


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