CN1059762A - The novel process of V 2 O 5 production by chloric acid chlorination method - Google Patents

The novel process of V 2 O 5 production by chloric acid chlorination method Download PDF

Info

Publication number
CN1059762A
CN1059762A CN91108117A CN91108117A CN1059762A CN 1059762 A CN1059762 A CN 1059762A CN 91108117 A CN91108117 A CN 91108117A CN 91108117 A CN91108117 A CN 91108117A CN 1059762 A CN1059762 A CN 1059762A
Authority
CN
China
Prior art keywords
vanadium
novel process
raw materials
production
slag
Prior art date
Legal status (The legal status 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 status listed.)
Pending
Application number
CN91108117A
Other languages
Chinese (zh)
Inventor
郑志芳
丁中南
张渊玖
郑有娣
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Individual
Original Assignee
Individual
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 Individual filed Critical Individual
Priority to CN91108117A priority Critical patent/CN1059762A/en
Publication of CN1059762A publication Critical patent/CN1059762A/en
Pending legal-status Critical Current

Links

Images

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P10/00Technologies related to metal processing
    • Y02P10/20Recycling

Landscapes

  • Manufacture And Refinement Of Metals (AREA)

Abstract

The novel process of V 2 O 5 production by chloric acid chlorination method.The present invention utilizes aqueous hydrochloric acid to feed chlorine and changes the vanadium in the vanadium slag over to solution, adds alkali again and makes vanadium ion generate the vanadium hydroxide precipitation, thereby make V 2O 5Recovery rate reach more than 96%.It has solved the difficult problem of impurity such as removing silicon, calcium, magnesium from vanadium raw materials, makes process for extracting vanadium produce the major transformation that updates.

Description

The novel process of V 2 O 5 production by chloric acid chlorination method
The invention belongs to the extracting method of the compound of vanadium.
Known to the applicant, the technique for producing vanadium pentoxide of widespread usage is the Wet-smelting method of vanadium slag through the oxidation sodium roasting both at home and abroad at present.That is: vanadium slag → broken ball milling magnetic separation → oxidation sodium roasting → water logging → purification and impurity removal → many vanadium ammonium precipitation → oven dry → deamination oxidation → finished product.Contain the vanadium rate in order to improve in the raw material, the vanadium slag that often blew before steel-making makes the vanadium rate that contains of raw material be enriched to 10-20% from 1%.But because SiO 2Can not thoroughly remove with the compound of calcium, the recovery rate of vanadium is still not high, and general iron and steel enterprise's recovery rate is less than 70%, and best in the world recovery rate is 92%.
Want to have breakthrough on process for extracting vanadium, obtain high recovery rate high benefit, complicated current technology is become simply, key issue is how the SiO that is present in a large number in the vanadium raw materials 2, CaO, MgO etc. remove, this is the brainstorm project of listing China Ministry of Metallurgical Industry the enforcement period of the seventh five-year plan.The present invention has successfully solved this difficult problem.
The present invention is achieved in that vanadium raw materials (containing the high silicon steel slag of high calcium, coal gangue, vanadium slag, inferior vanadium slag of vanadium etc.) and admixes aqueous solution of hydrochloric acid after levigate, in reaction tower, carry out chemical reaction (being called for short the acidleach chlorination reaction), make the vanadium in the raw material all change acidic solution over to ionic species with the chlorine that feeds.Use the filtering separation method then and remove a large amount of SiO 2With other materials (as insoluble substances such as C in the coal gangue or intermediate product FeOCl) that do not participate in reacting on a small quantity.Again with acid dip solution NH 3H 2O or NaOH, Ca(OH) 2, Na 2CO 3Neutralize, make vanadium ion and OH -Effect generates V(OH) 3↓, V(OH) 4↓ precipitation.Here the pH value that needs strict control solution is between 6.5~.07, otherwise Ca 2+, Mg 2+Under the situation of PH>7, also can generate Ca(OH) 2, Mg(OH) 2Precipitation.With the filtering separation method insoluble vanadium hydroxide is separated again at last, promptly got thick vanadium product.This thick vanadium can be used as finished product and sells iron and steel enterprise and smelt the high vanadium pig iron, also can be with conventional oxidation sodium roasting method (being commonly called as pyrogenic process) or with " oxidation alkali solution technique " (being commonly called as water law) further processing high-purity high-quality Vanadium Pentoxide in FLAKES.Utilize the vanadium extraction of this novel process, V 2O 5Recovery rate can reach more than 96%.
This novel process Production Flow Chart signal as figure:
Compare with existing process for extracting vanadium, this novel process has following advantage: 1, this novel process vanadium slag that need not blow, can utilize the direct vanadium extraction of steel-making refuse-slag, and not only reduce the vanadium extraction cost greatly, simultaneously can improve iron and steel output, can the say so major reform of update of process for extracting vanadium of this law.2, this novel process is not only applicable to the raw material-vanadium slag of the oxidation sodium roasting method vanadium extraction of present widespread use, but also is applicable to the raw material such as slag, coal gangue, vanadium slag, inferior vanadium slag of high silicon high calcium, the source of having widened vanadium raw materials greatly.3, this law step is simple, and facility investment is few, has saved and has invested huge roasting kiln or vertical multiple hearth furnace.With 40 tons of V of current methods investment monthly output 2O 5Expense be 1600~1,700 ten thousand yuan, and with 4,000,000 yuan of the expense deficiencies of 40 tons of this novel process investment monthly outputs.4, the recovery rate of current methods coal gangue is 35~40%, and the recovery rate of this novel process coal gangue can reach 90%.Is 55~75% with current methods from the recovery rate of Leaching of Vanadium from Vanadium slag, adopts this novel process vanadium extraction recovery rate from vanadium slag to reach more than 96%.5, adopt this novel process not have waste substantially, intermediate product SiO 2Can make road-making material, filtered liquid can be used H 2SO 4Displace HCl and reuse CaSO 4System cement or sulfuric acid, residue CaO makes material of construction, but iron contamination production red iron oxide, Mn impurity can be made the additive of polynary fertilizer ... no toxic and harmful and dust produce in the production process, and is low in the pollution of the environment.
Produce embodiment for one below: aqueous solution of hydrochloric acid with being pumped into (5 meters of reaction tower heights penetrate pressure 0.5kg) in the tower, is adjusted solution with soft water and made PH=2, will contain V again 2O 5Be that 6 tons of (solid-to-liquid ratio is 1: 2) liftings of 4.8% slag (flush slags of Ma Gang company three steel) are gone in the reaction tower, the reinforced liquid adding hole of cat head is built.Cat head has an outlet pipe to feed gas trap interior (returning application in order to absorb sour gas).Open the chlorine valve, adjust air feed and press 0.6kg, violent chemical reaction takes place in the tower in this moment, and temperature is controlled at 60~70 ℃, and reaction was kept 4~8 hours.After treating that substance reaction fully in the tower, be chilled to room temperature, open the tower bottom valve, thing in the tower by filtering basin, is added slag in the water purge column from cat head again.The slag that filters out is most of to be SiO 2, can make road-making material.The logical ammoniacal liquor of leach liquor in settling tank stirs again, and control pH value 6.5~7.0 bleeds off the settling tank supernatant liquid, with lower floor's slurries suction drier, and dehydration, oven dry.The product that obtains be thick barium [V(OH) 3, V(OH) 4Deng] weight is 0.598 ton.Through sodium oxide roasting or the molten further refinement of alkali oxide, can get high-purity high-quality V again 2O 50.281 ton, recovery rate is 97.43%.

Claims (1)

1, a kind of novel process of extracting Vanadium Pentoxide in FLAKES from raw materials such as coal gangue or v-bearing steel slag is characterized in that earlier aqueous hydrochloric acid being mixed and stirred vanadium raw materials and feeds chlorine react insoluble SlO in the chlorination tower 2Deng being separated with the various vanadium ions that enter solution, calcium ion etc.; And then in leach liquor, add alkali lye [NH 3H 2O or Na 2CO 3, Ca (OH) 2, NaOH etc.] the control pH value is 6.5~7, vanadium ion generates insoluble precipitation of hydroxide, filters and separates out thick vanadium (vanadium hydroxide), uses oxidation sodium roasting method or oxidation alkali solution technique again, further processing can get high-quality V 2O 5Its principles of chemistry are:
CN91108117A 1991-07-18 1991-07-18 The novel process of V 2 O 5 production by chloric acid chlorination method Pending CN1059762A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN91108117A CN1059762A (en) 1991-07-18 1991-07-18 The novel process of V 2 O 5 production by chloric acid chlorination method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN91108117A CN1059762A (en) 1991-07-18 1991-07-18 The novel process of V 2 O 5 production by chloric acid chlorination method

Publications (1)

Publication Number Publication Date
CN1059762A true CN1059762A (en) 1992-03-25

Family

ID=4909041

Family Applications (1)

Application Number Title Priority Date Filing Date
CN91108117A Pending CN1059762A (en) 1991-07-18 1991-07-18 The novel process of V 2 O 5 production by chloric acid chlorination method

Country Status (1)

Country Link
CN (1) CN1059762A (en)

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1320142C (en) * 2005-10-24 2007-06-06 安徽工业大学 Method for enriching vanadium in vanadium containing steel slag
CN100587089C (en) * 2008-06-05 2010-02-03 贵州省地质矿产中心实验室 Method for cleanly extracting vanadium from vanadium-containing carbonaceous shale
CN101684525B (en) * 2009-08-12 2011-01-19 虹京环保有限公司 Method for extracting vanadium from vanadium-containing ferrophosphor
CN103147128A (en) * 2013-02-28 2013-06-12 安徽工业大学 Manganese vanadate nanoneedle structure and synthesis method thereof
CN106834749A (en) * 2017-02-09 2017-06-13 东北大学 The method of Vanadium Concentrationin from v-bearing steel slag
CN107555479A (en) * 2016-07-01 2018-01-09 中国科学院过程工程研究所 A kind of chloridising prepares the system and method for high-purity low price barium oxide
CN107663585A (en) * 2017-09-26 2018-02-06 东北大学 The method of low-quality vanadium slag upgrading
CN108217727A (en) * 2018-04-12 2018-06-29 四川星明能源环保科技有限公司 A phase hypovanadic oxides and preparation method thereof
CN109609775A (en) * 2018-12-31 2019-04-12 南京格洛特环境工程股份有限公司 A kind of Resource comprehensive utilization method of steel slag

Cited By (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1320142C (en) * 2005-10-24 2007-06-06 安徽工业大学 Method for enriching vanadium in vanadium containing steel slag
CN100587089C (en) * 2008-06-05 2010-02-03 贵州省地质矿产中心实验室 Method for cleanly extracting vanadium from vanadium-containing carbonaceous shale
CN101684525B (en) * 2009-08-12 2011-01-19 虹京环保有限公司 Method for extracting vanadium from vanadium-containing ferrophosphor
CN103147128A (en) * 2013-02-28 2013-06-12 安徽工业大学 Manganese vanadate nanoneedle structure and synthesis method thereof
CN103147128B (en) * 2013-02-28 2015-05-13 安徽工业大学 Manganese vanadate nanoneedle structure and synthesis method thereof
CN107555479A (en) * 2016-07-01 2018-01-09 中国科学院过程工程研究所 A kind of chloridising prepares the system and method for high-purity low price barium oxide
CN106834749A (en) * 2017-02-09 2017-06-13 东北大学 The method of Vanadium Concentrationin from v-bearing steel slag
CN106834749B (en) * 2017-02-09 2019-01-29 东北大学 The method of Vanadium Concentrationin from v-bearing steel slag
CN107663585A (en) * 2017-09-26 2018-02-06 东北大学 The method of low-quality vanadium slag upgrading
CN108217727A (en) * 2018-04-12 2018-06-29 四川星明能源环保科技有限公司 A phase hypovanadic oxides and preparation method thereof
CN109609775A (en) * 2018-12-31 2019-04-12 南京格洛特环境工程股份有限公司 A kind of Resource comprehensive utilization method of steel slag
CN109609775B (en) * 2018-12-31 2020-08-07 南京格洛特环境工程股份有限公司 Resource comprehensive utilization method of steel slag

Similar Documents

Publication Publication Date Title
CN100359025C (en) Method of extracting vanadium pentoxide from vanadium ore
CN102531056B (en) Method for cleaner production of sodium vanadate and sodium chromate by pressure leaching of vanadium slag
CN108975364B (en) Method for removing alkali and recovering sodium by Bayer process red mud acid treatment
CN103194611A (en) Method for producing vanadium oxide
CN104386720B (en) Method for acid-alkali combined extraction of alumina from high-silicon aluminum-containing mineral raw material
CN101723458B (en) Method for cleanly extracting vanadium pentexide from vanadium containing material
CN101624650B (en) Microwave irradiation-acid leaching vanadium-recovering process of stone coal containing vanadium
CN103276218B (en) Method for recycling vanadium from vanadium-containing electrolysis aluminum slag ash
CN103146930A (en) Method for preparing vanadium oxide
CN101363079A (en) Smelting method of iron rich mengite rare-earth mine
CN104016398B (en) A kind of method that dilute sulfuric acid utilized in industrial wastewater produces sulfate
CN102560086A (en) Method for extracting vanadium from vanadium slag clinker leached by ammonium carbonate
CN102534187A (en) Method for treating pyrite cinder by combining acidic leaching with alkaline dissolving
CN107954474A (en) A kind of method that vanadium product and chromium sulfate basic are produced using vanadium chromium solution
CN107043128B (en) A kind of method that iron salt solutions lixiviation process prepares synthetic rutile
CN110512095B (en) Method for extracting and stabilizing arsenic from tungsten metallurgy phosphorus arsenic slag
CN101585553B (en) Method for producing vanadium pentoxide by ore containing vanadium and intermediate material containing vanadium
CN110643838A (en) Method for roasting vanadium slag by adopting calcium sulfate
CN1059762A (en) The novel process of V 2 O 5 production by chloric acid chlorination method
CN110972479B (en) Method for producing zinc oxide by twice leaching method
CN103922423A (en) Method of improving vanadium slag grade by utilizing titanium white waste acid
CN110157927A (en) A kind of no ammonium precipitation vanadium method
CN104232940A (en) Technology for extracting vanadic anhydride from bone coal by wet method
CN108862370A (en) A method of nano zine oxide being produced under zinc ammonia complexing environment using containing zinc ore crude
CN108842053A (en) The method of comprehensive utilization of Low grade manganese ore and electrolytic manganese crystallization double salt

Legal Events

Date Code Title Description
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
C06 Publication
PB01 Publication