NZ603075A - Method for treating wastewater - Google Patents

Method for treating wastewater

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Publication number
NZ603075A
NZ603075A NZ60307512A NZ60307512A NZ603075A NZ 603075 A NZ603075 A NZ 603075A NZ 60307512 A NZ60307512 A NZ 60307512A NZ 60307512 A NZ60307512 A NZ 60307512A NZ 603075 A NZ603075 A NZ 603075A
Authority
NZ
New Zealand
Prior art keywords
solution
degree
temperature
ammonium
wastewater
Prior art date
Application number
NZ60307512A
Other versions
NZ603075B (en
Inventor
Changlin Liu
Qianwen Li
Jinglei Zhang
Junhui Hong
Zhi Dong
Jinyang Zhang
Jianming Li
Deli Pu
Original Assignee
Pangang Group Res Inst Co Ltd
Pangang Group Co Ltd
Pangang Group Panzhihua Steel
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Pangang Group Res Inst Co Ltd, Pangang Group Co Ltd, Pangang Group Panzhihua Steel filed Critical Pangang Group Res Inst Co Ltd
Publication of NZ603075A publication Critical patent/NZ603075A/en
Publication of NZ603075B publication Critical patent/NZ603075B/en

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  • Heat Treatment Of Water, Waste Water Or Sewage (AREA)
  • Removal Of Specific Substances (AREA)

Abstract

Disclosed herein is a method for treating wastewater, the wastewater being produced by roasting a starting material in the presence of a sodium salt, leaching soluble sodium vanadate, and precipitating ammonium polyvanadate from an acidic leaching solution with an ammonium salt, the method comprising steps of: a) concentrating the wastewater having a pH value of 5.0~6.5 at a temperature of 90 degree C or higher to crystallize anhydrous sodium sulfate from the wastewater to obtain a first crystal suspension, and separating the anhydrous sodium sulfate from the first crystal suspension at a temperature of 90 degree C or higher to obtain a first solution; b) crystallizing a double salt of sodium sulfate and ammonium sulfate from the first solution at a temperature of 9~20 degree C, and separating the double salt to obtain a second solution; and c) concentrating the second solution by evaporation at a temperature of 70 degree C or higher, crystallising mixed ammonium salts including ammonium sulfate and ammonium chloride from the second solution at a temperature of 60~65 degree C to obtain a second crystal magma, and separating the mixed ammonium salts from the second crystal suspension at a temperature of 55 degree C or higher to obtain a third solution. Preferably wherein: a ratio of a volume of the wastewater before the concentrating in the step a) to a volume of the first crystal magma is 10:3~10:1, and a time during which the anhydrous sodium sulfate is crystallized is at least 40 minutes. the crystallizing in the step b) comprises crystallising the double salt of sodium sulfate and ammonium sulfate from the first solution at a temperature of 9~14 degree C for at least 3 hours. in the step c), a ratio of a volume of the second solution to a volume of the second crystal magma is 2~2.5:1, and a time during which the mixed ammonium salts are crystallized is at least 2 hours.
NZ603075A 2011-11-02 2012-10-17 Method for treating wastewater NZ603075B (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
CN 201110340963 CN102502900B (en) 2011-11-02 2011-11-02 Treatment method of sodium-roasted-leached-acid ammonium salt vanadium precipitation waste water
CN201110340963.2 2011-11-02

Publications (2)

Publication Number Publication Date
NZ603075A true NZ603075A (en) 2012-12-21
NZ603075B NZ603075B (en) 2013-03-22

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Also Published As

Publication number Publication date
JP2013094780A (en) 2013-05-20
CN102502900A (en) 2012-06-20
ZA201208219B (en) 2013-07-31
JP5466749B2 (en) 2014-04-09
CN102502900B (en) 2013-08-14

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