NZ603075A - Method for treating wastewater - Google Patents
Method for treating wastewaterInfo
- 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
Links
Landscapes
- 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.
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 |
Family
ID=
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 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
PL1807349T3 (en) | Method for crystallizing soluble salts of divalent anions from brine | |
IN2014CN03665A (en) | ||
US10072038B2 (en) | Crystal of ammonium N-acetylneuraminate anhydrate, and process for producing same | |
JP2019528230A5 (en) | ||
WO2012061460A3 (en) | Method for producing ammonium sulfate nitrate | |
NZ751256A (en) | Method for producing the crystalline form of modification a of calcobutrol | |
RU2017123112A (en) | METHOD FOR PRODUCING CRYSTALS OF DERIVATED DIAZABICYCLOOCTANE AND STABLE LYOPHILIZED DRUG | |
CN102992407B (en) | Ammonium rhenate solution crystallization method | |
CN106083673A (en) | A kind of preparation technology of carbocisteine | |
UA113204C2 (en) | SELECTIVE EXTRACTION OF POTASSIUM CHLORIDE FROM THE OUTSIDE SHENITA SOLUTION WITH THE USE OF TARTARIC ACID AS A SAFETY SOFT EXTRADENTS | |
JP2019529548A5 (en) | ||
TN2015000372A1 (en) | A method for concentrating rare-earth metals in phosphogypsum | |
CN104291360A (en) | Method for extracting reagent grade potassium chloride from potassium fertilizer | |
CN101475270A (en) | Denitration method by dilute salt solution membrane process | |
NZ603075A (en) | Method for treating wastewater | |
WO2012066547A4 (en) | Method for producing small size titanium oxide particles | |
CN108190921A (en) | A kind of preparation method of high-purity lithium salts | |
KR101395558B1 (en) | Refining method of quinolinic acid | |
US10005808B2 (en) | Crystal of alkali metal N-acetylneuraminate anhydrate, and process for producing same | |
WO2015084693A3 (en) | New process for preparing loratadine from a ketone intermediate | |
CN104276554B (en) | A kind of method preparing potassium dihydrogen phosphate coproduction walnut composite fertilizer special | |
CN104495878B (en) | A kind of from high calcium abandoned mine decalcification produce the method for food-grade potassium chloride | |
CN103923037B (en) | Method for reducing copper ions in methylene blue solution by using calcium phosphate | |
RU2013132528A (en) | METHOD FOR PRODUCING LACTATE | |
TW201720788A (en) | Crystals of monovalent cation salt of 3-hydroxyisovaleric acid, and method for producing said crystals |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
PSEA | Patent sealed | ||
RENW | Renewal (renewal fees accepted) |
Free format text: PATENT RENEWED FOR 3 YEARS UNTIL 17 OCT 2019 BY SHELSTON IP Effective date: 20140910 Free format text: PATENT RENEWED FOR 3 YEARS UNTIL 17 OCT 2022 BY SHELSTON IP Effective date: 20140910 Free format text: PATENT RENEWED FOR 7 YEARS UNTIL 17 OCT 2032 BY SHELSTON IP Effective date: 20140910 Free format text: PATENT RENEWED FOR 3 YEARS UNTIL 17 OCT 2025 BY SHELSTON IP Effective date: 20140910 |