CN101423203A - Water-saving and emission-reducing wet method phosphoric acid manufacture process - Google Patents
Water-saving and emission-reducing wet method phosphoric acid manufacture process Download PDFInfo
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- CN101423203A CN101423203A CNA2008100689875A CN200810068987A CN101423203A CN 101423203 A CN101423203 A CN 101423203A CN A2008100689875 A CNA2008100689875 A CN A2008100689875A CN 200810068987 A CN200810068987 A CN 200810068987A CN 101423203 A CN101423203 A CN 101423203A
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- phosphoric acid
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Claims (3)
- The wet method phosphoric acid manufacture process of 1 one kinds of water-saving and emission-reducings, it is characterized in that this technology is before the phosphorus ore slurry enters extraction tank, ore pulp is carried out following pre-treatment: the ore pulp that phosphorus ore and water form after wet wheeling machine grinds, separate through cyclone separator, underproof coarse particles is discharged from the swirler bottom and is reentered the grinding machine grinding, the qualified ore pulp for moisture 50% that discharge at the swirler top enters Hhigh-efficient thickener and carries out densely, pumps into filter then to filter; Breeze after the filtration, a part is transported to the breeze hopper through belt, is delivered to metering screw through disk feeder, and the metering back adds tempering tank; Another part breeze is then delivered to the breeze warehousing and is deposited, and when grinding system is shut down, to rotary conveyor, delivers to tempering tank with the driving grasping operation then; Enter the breeze of tempering tank and under the stirring action of tempering tank agitator, react,, extract, produce dilute phosphoric acid according to traditional method by pumping into phosphoric acid by wet process extractive reaction groove from rephosphorization acid, the washing water of phosphoric acid by wet process; The water that filter is separated is after collecting, and pump is mixed into grinding machine with phosphorus ore after metering and grinds to wet wheeling machine, reuses.
- 2 according to the described production technique of claim 1, it is characterized in that described filter is pottery or turntable type filter or band filter; One or more is set is arranged in parallel; Independent operating or many operations simultaneously.
- 3 according to the described production technique of claim 1, it is characterized in that used breeze granularity is-200 orders~60 orders; Breeze after the filtration is moisture less than 10%; The material that enters tempering tank is 60%~75% through the slip solid content that reaction forms.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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CN2008100689875A CN101423203B (en) | 2008-11-13 | 2008-11-13 | Water-saving and emission-reducing wet method phosphoric acid manufacture process |
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CN2008100689875A CN101423203B (en) | 2008-11-13 | 2008-11-13 | Water-saving and emission-reducing wet method phosphoric acid manufacture process |
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Publication Number | Publication Date |
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CN101423203A true CN101423203A (en) | 2009-05-06 |
CN101423203B CN101423203B (en) | 2011-12-07 |
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CN2008100689875A Expired - Fee Related CN101423203B (en) | 2008-11-13 | 2008-11-13 | Water-saving and emission-reducing wet method phosphoric acid manufacture process |
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Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102336428A (en) * | 2011-06-30 | 2012-02-01 | 云南云天化国际化工股份有限公司三环分公司 | Method for taking phosphogypsum under wet-process deslagging conditions |
CN104401959A (en) * | 2014-10-13 | 2015-03-11 | 云南红富化肥有限公司 | Method for filtering phosphogypsum with dilute phosphoric acid for circulating washing |
CN106395775A (en) * | 2016-08-31 | 2017-02-15 | 郝付勇 | Method for filtering phosphoric acid extraction slurry |
CN106904585A (en) * | 2017-03-08 | 2017-06-30 | 四川省汉源化工总厂 | A kind of diluted acid de-magging slurry processing method |
CN106914332A (en) * | 2017-04-18 | 2017-07-04 | 云南佳贝节能科技有限公司 | A kind of system of processing of rock phosphate in powder |
CN107628596A (en) * | 2017-11-13 | 2018-01-26 | 贵阳开磷化肥有限公司 | A kind of apparatus and method using waste water regulation phosphate ore pulp extraction production phosphoric acid |
CN110921642A (en) * | 2019-12-18 | 2020-03-27 | 瓮福(集团)有限责任公司 | Method and device for treating phosphoric acid slurry by wet process |
Family Cites Families (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3408161A (en) * | 1965-08-23 | 1968-10-29 | Armour Agricult Chem | Production of purified wet process phosphoric acid from phosphate rock |
CN1012166B (en) * | 1988-01-05 | 1991-03-27 | 江西工业大学 | Producing calcium superphosphat by activated ore pulp method |
CN101053853A (en) * | 2007-04-20 | 2007-10-17 | 云南云天化国际化工股份有限公司 | Phosphate rock single stage closed ore milling method |
-
2008
- 2008-11-13 CN CN2008100689875A patent/CN101423203B/en not_active Expired - Fee Related
Cited By (10)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102336428A (en) * | 2011-06-30 | 2012-02-01 | 云南云天化国际化工股份有限公司三环分公司 | Method for taking phosphogypsum under wet-process deslagging conditions |
CN102336428B (en) * | 2011-06-30 | 2013-07-24 | 云南云天化国际化工股份有限公司三环分公司 | Method for taking phosphogypsum under wet-process deslagging conditions |
CN104401959A (en) * | 2014-10-13 | 2015-03-11 | 云南红富化肥有限公司 | Method for filtering phosphogypsum with dilute phosphoric acid for circulating washing |
CN104401959B (en) * | 2014-10-13 | 2016-06-22 | 云南红富化肥有限公司 | A kind of method filtering ardealite employing light phosphoric acid circulation washing |
CN106395775A (en) * | 2016-08-31 | 2017-02-15 | 郝付勇 | Method for filtering phosphoric acid extraction slurry |
CN106904585A (en) * | 2017-03-08 | 2017-06-30 | 四川省汉源化工总厂 | A kind of diluted acid de-magging slurry processing method |
CN106914332A (en) * | 2017-04-18 | 2017-07-04 | 云南佳贝节能科技有限公司 | A kind of system of processing of rock phosphate in powder |
CN107628596A (en) * | 2017-11-13 | 2018-01-26 | 贵阳开磷化肥有限公司 | A kind of apparatus and method using waste water regulation phosphate ore pulp extraction production phosphoric acid |
CN110921642A (en) * | 2019-12-18 | 2020-03-27 | 瓮福(集团)有限责任公司 | Method and device for treating phosphoric acid slurry by wet process |
CN110921642B (en) * | 2019-12-18 | 2023-12-26 | 瓮福(集团)有限责任公司 | Wet-process phosphoric acid slurry treatment method and device |
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Publication number | Publication date |
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CN101423203B (en) | 2011-12-07 |
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SE01 | Entry into force of request for substantive examination | ||
C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
C53 | Correction of patent for invention or patent application | ||
CB03 | Change of inventor or designer information |
Inventor after: Yu Aimin Inventor after: Zhong Jin Inventor after: Li Long Inventor before: Yu Aimin Inventor before: Li Long Inventor before: Cheng Xuxin |
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COR | Change of bibliographic data |
Free format text: CORRECT: INVENTOR; FROM: YU AIMIN LI LONG CHENG XUXIN TO: YU AIMIN ZHONG JIN LI LONG |
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C56 | Change in the name or address of the patentee |
Owner name: GUIZHOU KAILIN GROUP CO., LTD. Free format text: FORMER NAME: KAILIN (GROUP) CO., LTD., GUIZHOU |
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CP03 | Change of name, title or address |
Address after: No. 237 Jinyang City Kailin Lake District Road 550009 Guizhou city of Guiyang Province Patentee after: Phosphorylcholine group limited-liability company is opened in Guizhou Address before: 550002, Haitian building, No. 203 Zhonghua South Road, Guizhou, Guiyang Patentee before: Guizhou Kailin (Group) Co.,Ltd. |
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CF01 | Termination of patent right due to non-payment of annual fee | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20111207 Termination date: 20181113 |