CN1413912A - Process for preparing thiomolybdate for molybdenum separated from sodium tungstate solution containing molybdenum - Google Patents
Process for preparing thiomolybdate for molybdenum separated from sodium tungstate solution containing molybdenum Download PDFInfo
- Publication number
- CN1413912A CN1413912A CN01128681A CN01128681A CN1413912A CN 1413912 A CN1413912 A CN 1413912A CN 01128681 A CN01128681 A CN 01128681A CN 01128681 A CN01128681 A CN 01128681A CN 1413912 A CN1413912 A CN 1413912A
- Authority
- CN
- China
- Prior art keywords
- molybdenum
- thiomolybdate
- sodium tungstate
- sulphur
- tungstate solution
- 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.)
- Granted
Links
Classifications
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P10/00—Technologies related to metal processing
- Y02P10/20—Recycling
Landscapes
- Inorganic Compounds Of Heavy Metals (AREA)
- Catalysts (AREA)
Abstract
A process for preparing thiomolybdate for separating Mo from the sodium tungstate solution countaining NaOH, WO3 and Mo includes such steps as adding S to the said solution, stirring, heating to 40-110 deg.C, reaction for 1-4 hr, cooling to 40 deg.C, regulating pH to 7.5-9.0 in sealed condition, heating to 50-80 deg.C, stirring and reaction for 1-4 hr. It can decrease cost by 90-98%.
Description
Technical field:
The invention belongs to chemical industry metallurgical inorganics purification field.The present invention relates to a kind ofly carry out tungsten, the isolating process for preparing thiomolybdate of molybdenum, particularly adopt vulcanizing agent: sulphur, i.e. sulphur based on generating the thiomolybdate ion.
Background technology:
Under the certain condition, the molybdenum acid ion in the tungstate can carry out thioated and generate thiomolybdate.Utilize the thiomolybdate ion can realize that with the difference of tungstate ion character in weak alkaline medium tungsten separates, this is a kind of industry application method thereof that has practical significance most, its prerequisite is to make molybdenum acid ion be converted into the thiomolybdate ion, promptly must make molybdate be converted into Thiomolybdate.The existing employed vulcanizing agent of method for preparing Thiomolybdate from tungstate solution has Na
2S, NaHS, (NH
4)
2S when adopting these vulcanizing agents to prepare Thiomolybdate, because their prices are higher, makes that the cost of preparation Thiomolybdate is higher, causes tungsten, molybdenum separation industries production cost height.
Summary of the invention:
The object of the present invention is to provide the cheap vulcanizing agent of a kind of usefulness to prepare the method for Thiomolybdate, thus from sodium tungstate solution Separation of Molybdenum at lower cost.
1. technical solution of the present invention is the process for preparing thiomolybdate that Separation of Molybdenum is used in a kind of sodium tungstate solution that contains molybdenum, and it is to contain in the sodium tungstate solution of molybdenum a kind of vulcanizing agent is added, and generates Thiomolybdate.Thereafter, by the thiomolybdate ion in ion exchange method, extraction process or the precipitator method separation solution, thereby realize that tungsten, molybdenum separate, the feature of present method is:
(1). used vulcanizing agent is a sulphur, i.e. sulphur, chemical molecular formula is: S
(2). the step of preparation Thiomolybdate is as follows:
A) feed liquid is the sodium tungstate solution that contains molybdenum, and feed liquid contains Mo:0.2-3.5g/L, WO
3: 40-280g/L, NaOH:0.5-20g/L is with a certain amount of Q
1Feed liquid and a certain amount of Q
2Vulcanizing agent in container, mix Q
2Amount is Q
1The 7-15 that contains the molybdenum gross weight in the amount doubly stirs, heating, and Heating temperature is 40 ℃-110 ℃, reacts after 1-4 hour, is cooled to about 40 ℃
B) under airtight and stirring state, the acidity of regulating mixed solution with acid makes the pH value in the 7.5-9.0 scope, is heated to 50 ℃-80 ℃ then, stirring reaction 1-4 hour.
Above-mentioned A), B) these two steps can be carried out continuously, can be carried out also can carrying out continuously in two reaction vessels in same reaction vessel.
Used vulcanizing agent sulphur is that sulphur can be powdery, also can be block, if blocky, can use after suitable fragmentation, and effect same can be arranged.
Regulate acidity and can use mineral acid and CO such as sulfuric acid, hydrochloric acid
2Gas; Organic acids such as also available formic acid, acetate.
Embodiment:
The present invention further specifies as follows in conjunction with specific embodiments, in described below all specific embodiments of the present invention, vulcanizing agent all is to adopt sulphur, be sulphur, feed liquid all is the sodium tungstate solution that contains molybdenum, the method for preparing Thiomolybdate is all by top described A), B) two steps carry out, reaction is carried out under agitation condition.The common conditions that these are identical, following each specific embodiment is not given unnecessary details one by one.
Embodiment 1, and vulcanizing agent is a powdery sulphur, i.e. powdery sulphur, and the preparation Thiomolybdate carries out by the following step:
Feed liquid is industrial sodium tungstate solution, and feed liquid contains Mo:1.457g/L; WO
3: 120.257g/L; NaOH:0.5g/L.
A) get the 200ml feed liquid, in reaction vessel, add 2.0g (weight ratio of molybdenum and vulcanizing agent is 1: 7) powdery sulphur and be sulphur in feed liquid, stir, mix, heating, being heated to temperature is 106 ℃ of reactions 1 hour, is chilled to then about 40 ℃.
B) mixed solution changes over to encloses container, is 8.0 with the pH value of 1: 1 hydrochloric acid conditioning solution, stirs, is heated to 70 ℃, reacts 2 hours.
With extraction process check thioated rate, the composition of used organic phase (V%) is: 3%N
263+ 15%TBP+82% kerosene mixes with the feed liquid of own thioated by comparing 1: 1, and vibration is 5 minutes on the Kang Shi vibrator, makes the thiomolybdate ion be extracted to organic phase, behind the standing demix, tells water.Detect the molybdenum of aqueous phase then with colorimetry, calculate the thioated rate with minusing.
Detected result, the molybdenum rate of removing of present embodiment is 81.88%.Embodiment 2, vulcanizing agent powdery sulphur, and the step of the feed liquid of preparation Thiomolybdate and preparation Thiomolybdate is identical with embodiment 1.The vulcanizing agent consumption is 2.0g, but A) step is to be heated to 110 ℃, reaction is 4 hours; B) step is to regulate acidity to pH=7.5 with 1: 1 formic acid, and 70 ℃ were reacted 2 hours.
The method of pressing embodiment 1 detects, detected result, and removing the molybdenum rate is 96.49%.Embodiment 3, and feed liquid is for containing WO
3: 40.356g/L; Mo:0.205g/L; The sodium tungstate solution of NaOH:4.460g/L.Vulcanizing agent powdery sulphur, the step of preparation Thiomolybdate is identical with embodiment 1.The vulcanizing agent consumption is 2.0g, but A) step is to be heated to 106 ℃ of reactions 2 hours; B) step is to regulate acidity to pH=9.0 with 1: 1 acetate, is heated to 50 ℃, reacts 4 hours.
The method of pressing embodiment 1 detects, and after testing, removing the molybdenum rate is 97.31% embodiment 4, and feed liquid is for containing WO
3: 160.125g/L; Mo:0.205g/L, the sodium tungstate solution of NaOH:14.460g/L.Get the 200ml feed liquid, vulcanizing agent and preparation Thiomolybdate A), B) step is identical with embodiment 1.Adding sulfuration dosage is 3.2g.A) step is that B) step was with 1: 1 rare H 106 ℃ of reactions 1 hour
2SO
4Regulate acidity to pH=8.0,80 ℃ of reactions 4 hours.The method of inspection is: with rare H of 1mol/L
2SO
4In and the feed liquid after the thioated to pH ≈ 2.3, boiled 1.5 hours, filter, remove MoS
2Precipitation with the molybdenum of colorimetry detection aqueous phase, is calculated the molybdenum rate of removing with minusing then.
After testing, removing the molybdenum rate is 93.85%.Embodiment 5, and feed liquid is for containing WO
3: 180.215g/L; Mo:1.457g/L; The sodium tungstate solution of NaOH:14.460g/L.Get the 200ml feed liquid, vulcanizing agent and preparation Thiomolybdate A), B) two steps are identical with embodiment 4.Add vulcanizing agent 3.2g, A) step is reflected at 100 ℃ of reactions 2.5 hours, and B) step is to regulate acidity to pH=7.8 with 1: 1 formic acid, and 50 ℃ of reactions 4 hours.Press embodiment 4 and detect the molybdenum rate of removing.
After testing, remove the molybdenum rate and be 96.92% embodiment 6, substantially the same manner as Example 5, but different be that the sulfo-agent is to be crushed to 80 orders with block sulphur and with it, the vulcanizing agent consumption is 3.2g.Detection method is: adopt ion exchange method to detect, the feed liquid that is about to own thioated is collected the solution after exchanging by the ion exchange column of D290 resin is housed, and detects molybdenum with colorimetry then, calculates the molybdenum rate of removing with minusing.
After testing, removing the molybdenum rate is 99.03%.Embodiment 7, and is substantially the same manner as Example 6.Different is that B) step is to use CO
2Regulate acidity to pH=7.8.
The method of pressing embodiment 6 detects, and detected result is removed the molybdenum rate and is 99.28% embodiment 8, and is substantially the same manner as Example 7.Different is that A) going on foot temperature of reaction is 40 ℃, 4 hours; B) step is to regulate acidity to pH=8.5 with 1: 1 hydrochloric acid, and at 80 ℃, reacts 1 hour.
The method of pressing embodiment 4 detects, detected result, and removing the molybdenum rate is 81.66%.Embodiment 9, and feed liquid is for containing Mo:1.467g/L; WO
3: 273.965g/L; The sodium tungstate solution of NaOH:20.012g/L, get the 200ml feed liquid, heavily add powdery sulphur 4.4 g by 15 times that contain the molybdenum gross weight in the feed liquid and make vulcanizing agent, stir, heat, 106 ℃ of reactions 2.5 hours, be chilled to about 40 ℃, finish A) step, use formic acid acid adjustment in 1: 1 then, making the pH value is 8.0,70 ℃, stirring reaction 2 hours.Detection method: feed liquid after the thioated is diluted to contains WO
3Be 145g/L, add the CaCl of d=1.23 again
2Solution makes tungsten with CaWO
4The form precipitation, thiomolybdate stays in mother liquor of precipitation of ammonium, realizes that tungsten separates, and detects the molybdenum of aqueous phase then with colorimetry, calculates the molybdenum rate of removing by following formula.
Detected result, removing the molybdenum rate is 98.32% embodiment 10, feed liquid is for containing WO
3: 80.457g/L; Mo:3.506g/L; The sodium tungstate solution of NaOH:3.457g/L.Get feed liquid 200ml, vulcanizing agent consumption, preparation Thiomolybdate A), B) two steps are identical with embodiment 9.Press
The method of embodiment 9 detects.
Detected result, removing the molybdenum rate is 78.20%.
Advantage of the present invention is: adopt method of the present invention, with sulphur, be sulphur, chemical molecular formula is: S, as vulcanizing agent, the preparation Thiomolybdate has reduced the cost of Separation of Molybdenum from sodium tungstate solution significantly, and uses Na
2S, NaHS, (NH
4)
2The method that these several vulcanizing agents of S prepare Thiomolybdate is made comparisons, and has remarkable advantages.For example, handle 1 cubic metre and contain WO
3: 120.257g/L; The actual feed liquid of Mo:1.457g/L is used Na respectively
2S, NaHS and (NH
4)
2S makes vulcanizing agent, reaches the thioated rate of the desired molybdenum acid ion of industrial production, reaches the required molybdenum rate of removing, and the cost of required vulcanizing agent is respectively 36.56 yuan, 40.93 yuan and 222.54 yuan, and makes vulcanizing agent with sulphur (sulphur), only needs 4.37 yuan.Compare as seen, the inventive method of making vulcanizing agent with sulphur can reduce expense 90-98%, and expense reduces very remarkable.
In addition, also can find out the vulcanizing agent sulphur that the present invention is used from the unit sulphur valency (unit/ton sulphur) of the listed various different vulcanizing agents of following table, promptly sulphur is in the employed vulcanizing agent, and unit sulphur valency is minimum.
| The vulcanizing agent title | ??Na 2S | ??NaHS | ??(NH 4) 2S | ????S |
| Unit sulphur valency (unit/ton sulphur) | ??6700 | ??7500 | ??40780 | ????800 |
Claims (4)
1. the process for preparing thiomolybdate that Separation of Molybdenum is used in the sodium tungstate solution that contains molybdenum, it is to contain in the sodium tungstate solution of molybdenum a kind of vulcanizing agent is added, and generates Thiomolybdate.Thereafter, by the thiomolybdate ion in ion exchange method, extraction process or the precipitator method separation solution, thereby realize that tungsten, molybdenum separate, the feature of present method is:
(1). used vulcanizing agent is a sulphur, i.e. sulphur, chemical molecular formula is: S
(2). the step of preparation Thiomolybdate is as follows:
A) feed liquid is the sodium tungstate solution that contains molybdenum, and feed liquid contains Mo:0.2-3.5g/L, WO
3: 40-280g/L, NaOH:0.5-20g/L is with a certain amount of Q
1Feed liquid and a certain amount of Q
2Vulcanizing agent in container, mix Q
2Amount is Q
1The 7-15 that contains the molybdenum gross weight in the amount doubly stirs, heating, and Heating temperature is 40 ℃-110 ℃, reacts after 1-4 hour, is cooled to about 40 ℃
B) under airtight and stirring state, the acidity of regulating mixed solution with acid makes the pH value in the 7.5-9.0 scope, is heated to 50 ℃-80 ℃ then, stirring reaction 1-4 hour.
2. the process for preparing thiomolybdate that Separation of Molybdenum is used in the sodium tungstate solution that contains molybdenum according to claim 1, used vulcanizing agent is sulphur, i.e. sulphur, chemical molecular formula is: S, and it can be a powdery, also can be block, if blocky, can after suitable fragmentation, use.
3. the process for preparing thiomolybdate that Separation of Molybdenum is used in the sodium tungstate solution that contains molybdenum according to claim 1, the process of preparation Thiomolybdate is a successive, can carry out in two reaction vessels, also can carry out in same reaction vessel.
4. the process for preparing thiomolybdate that Separation of Molybdenum is used in the sodium tungstate solution that contains molybdenum according to claim 1 is regulated acidity and can be used mineral acid and CO such as sulfuric acid, hydrochloric acid
2Gas; Organic acids such as also available formic acid, acetate.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB011286814A CN1166565C (en) | 2001-10-16 | 2001-10-16 | Process for preparing thiomolybdate for molybdenum separated from sodium tungstate solution containing molybdenum |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB011286814A CN1166565C (en) | 2001-10-16 | 2001-10-16 | Process for preparing thiomolybdate for molybdenum separated from sodium tungstate solution containing molybdenum |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN1413912A true CN1413912A (en) | 2003-04-30 |
| CN1166565C CN1166565C (en) | 2004-09-15 |
Family
ID=4668521
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNB011286814A Expired - Fee Related CN1166565C (en) | 2001-10-16 | 2001-10-16 | Process for preparing thiomolybdate for molybdenum separated from sodium tungstate solution containing molybdenum |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN1166565C (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104402054A (en) * | 2014-10-27 | 2015-03-11 | 中南大学 | Method for deeply removing molybdenum from tungstate solution through ion exchange process |
| CN107986333A (en) * | 2017-12-13 | 2018-05-04 | 中南大学 | A kind of molybdate solution or tungstate solution containing molybdenum and trithiocyanuric acid（Salt）The method of reaction synthesis Thiomolybdate |
| CN108396143A (en) * | 2018-06-07 | 2018-08-14 | 江西理工大学 | A method of removing molybdenum from tungstate solution extraction |
| CN108642309A (en) * | 2018-06-07 | 2018-10-12 | 江西理工大学 | A kind of technique that ion-exchange removes molybdenum from tungstate solution |
| CN114855000A (en) * | 2022-04-28 | 2022-08-05 | 湖北绿钨资源循环有限公司 | Method for separating and removing tungsten and molybdenum in tungsten smelting process |
-
2001
- 2001-10-16 CN CNB011286814A patent/CN1166565C/en not_active Expired - Fee Related
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104402054A (en) * | 2014-10-27 | 2015-03-11 | 中南大学 | Method for deeply removing molybdenum from tungstate solution through ion exchange process |
| CN107986333A (en) * | 2017-12-13 | 2018-05-04 | 中南大学 | A kind of molybdate solution or tungstate solution containing molybdenum and trithiocyanuric acid（Salt）The method of reaction synthesis Thiomolybdate |
| CN108396143A (en) * | 2018-06-07 | 2018-08-14 | 江西理工大学 | A method of removing molybdenum from tungstate solution extraction |
| CN108642309A (en) * | 2018-06-07 | 2018-10-12 | 江西理工大学 | A kind of technique that ion-exchange removes molybdenum from tungstate solution |
| CN108396143B (en) * | 2018-06-07 | 2019-08-20 | 江西理工大学 | A method of molybdenum is removed from tungstate solution extraction |
| CN114855000A (en) * | 2022-04-28 | 2022-08-05 | 湖北绿钨资源循环有限公司 | Method for separating and removing tungsten and molybdenum in tungsten smelting process |
| CN114855000B (en) * | 2022-04-28 | 2023-08-22 | 湖北绿钨资源循环有限公司 | Method for separating and removing impurities from tungsten and molybdenum in tungsten smelting process |
Also Published As
| Publication number | Publication date |
|---|---|
| CN1166565C (en) | 2004-09-15 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| US3800024A (en) | Process for neutralization and regeneration of aqueous solutions of acids and dissolved metals | |
| CN1255560C (en) | Process for recovering rare earth from neodymium-ion-boron waste materials | |
| CN108298581A (en) | A kind of vanadium extraction from the leachate of containing vanadium and chromium silicon and the system and its processing method for preparing vanadic anhydride | |
| EP3243799B1 (en) | Vanadium pentoxide purifying system and method | |
| CN101012501A (en) | Method for separating highly-pure rare-earth oxide from yttrium-rich rare earth mine | |
| CN101932526B (en) | Methods and compositions for the removal of impurities and water from the bayer process | |
| EP3243798A1 (en) | System and method for preparing high-purity divanadium pentoxide powder | |
| EP3252012A1 (en) | System and method for producing high-purity divanadium pentoxide powder | |
| CN103421964A (en) | Method for leaching vanadium from stone coal containing vanadium | |
| CN107417576A (en) | A kind of urea for vehicle preparation method | |
| CN1413912A (en) | Process for preparing thiomolybdate for molybdenum separated from sodium tungstate solution containing molybdenum | |
| CN103482650A (en) | Equipment for preparing ammonium fluoride or ammonium bifluoride by adopting fluosilicic acid and liquid ammonia and production method | |
| CN100467671C (en) | Method for recovering hydrochloric acid and copper sulfate from acidic etching liquid | |
| US4083925A (en) | Method for removing ferrous iron from alkali metal aluminate liquor | |
| CN111206150B (en) | Dissolved state high-similarity rare and precious metal enrichment and separation method based on floating extraction | |
| CN107118138A (en) | A kind of method that sulfosalicylic acid is reclaimed in the alkalization mother liquor from fortimicin | |
| CN108706844A (en) | Iron, chromium, the separation and recovery method of aluminium and its application in more metal hazardous wastes | |
| CN1259242C (en) | Method for simultaneously producing sodium aluminofluoride and silica white | |
| CN104610043A (en) | Method for recycling oxalic acid from rear-earth industrial wastewater | |
| CN1453381A (en) | Scheelite decomposing process | |
| CN1194897C (en) | Method for producing cryolite | |
| CN1506474A (en) | Phosphorus-eliminating purification process of vanadium-containing chamotte leachate | |
| CN1044634A (en) | The method of hydrothermal producting solution of solidum silicate at high ratio of Si: Na | |
| CN220573434U (en) | Device for preparing potassium sulfate by extraction method | |
| CN1056091A (en) | Producing sand like synthetic cryolite by clay bittern method |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C19 | Lapse of patent right due to non-payment of the annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |