JPH0236533B2 - MORIBUDENSANENGANJUSUIYOEKIKARAMORIBUDENSANENOKAISHUSURUHOHO - Google Patents
MORIBUDENSANENGANJUSUIYOEKIKARAMORIBUDENSANENOKAISHUSURUHOHOInfo
- Publication number
- JPH0236533B2 JPH0236533B2 JP6539386A JP6539386A JPH0236533B2 JP H0236533 B2 JPH0236533 B2 JP H0236533B2 JP 6539386 A JP6539386 A JP 6539386A JP 6539386 A JP6539386 A JP 6539386A JP H0236533 B2 JPH0236533 B2 JP H0236533B2
- Authority
- JP
- Japan
- Prior art keywords
- molybdate
- solution
- methanol
- aqueous solution
- moo
- 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.)
- Expired - Lifetime
Links
- MEFBJEMVZONFCJ-UHFFFAOYSA-N molybdate Chemical compound [O-][Mo]([O-])(=O)=O MEFBJEMVZONFCJ-UHFFFAOYSA-N 0.000 claims description 33
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims description 15
- 239000007864 aqueous solution Substances 0.000 claims description 13
- CSCPPACGZOOCGX-UHFFFAOYSA-N Acetone Chemical compound CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 claims description 10
- 239000002244 precipitate Substances 0.000 claims description 8
- 238000000034 method Methods 0.000 claims description 6
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 33
- 239000000243 solution Substances 0.000 description 14
- 238000001556 precipitation Methods 0.000 description 9
- 239000003960 organic solvent Substances 0.000 description 8
- LRHPLDYGYMQRHN-UHFFFAOYSA-N N-Butanol Chemical compound CCCCO LRHPLDYGYMQRHN-UHFFFAOYSA-N 0.000 description 7
- 238000011084 recovery Methods 0.000 description 5
- ZOKXTWBITQBERF-UHFFFAOYSA-N Molybdenum Chemical compound [Mo] ZOKXTWBITQBERF-UHFFFAOYSA-N 0.000 description 4
- 229910052750 molybdenum Inorganic materials 0.000 description 4
- 239000011733 molybdenum Substances 0.000 description 4
- 239000011734 sodium Substances 0.000 description 4
- KFZMGEQAYNKOFK-UHFFFAOYSA-N Isopropanol Chemical compound CC(C)O KFZMGEQAYNKOFK-UHFFFAOYSA-N 0.000 description 3
- 150000003839 salts Chemical class 0.000 description 3
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 2
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 description 2
- 239000002253 acid Substances 0.000 description 2
- APUPEJJSWDHEBO-UHFFFAOYSA-P ammonium molybdate Chemical compound [NH4+].[NH4+].[O-][Mo]([O-])(=O)=O APUPEJJSWDHEBO-UHFFFAOYSA-P 0.000 description 2
- 235000018660 ammonium molybdate Nutrition 0.000 description 2
- 239000011609 ammonium molybdate Substances 0.000 description 2
- 229940010552 ammonium molybdate Drugs 0.000 description 2
- 150000003863 ammonium salts Chemical class 0.000 description 2
- 239000012141 concentrate Substances 0.000 description 2
- 230000003247 decreasing effect Effects 0.000 description 2
- 239000000706 filtrate Substances 0.000 description 2
- 238000001914 filtration Methods 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- JKQOBWVOAYFWKG-UHFFFAOYSA-N molybdenum trioxide Chemical compound O=[Mo](=O)=O JKQOBWVOAYFWKG-UHFFFAOYSA-N 0.000 description 2
- VLAPMBHFAWRUQP-UHFFFAOYSA-L molybdic acid Chemical compound O[Mo](O)(=O)=O VLAPMBHFAWRUQP-UHFFFAOYSA-L 0.000 description 2
- BDERNNFJNOPAEC-UHFFFAOYSA-N propan-1-ol Chemical compound CCCO BDERNNFJNOPAEC-UHFFFAOYSA-N 0.000 description 2
- 238000000926 separation method Methods 0.000 description 2
- 235000015393 sodium molybdate Nutrition 0.000 description 2
- 239000011684 sodium molybdate Substances 0.000 description 2
- TVXXNOYZHKPKGW-UHFFFAOYSA-N sodium molybdate (anhydrous) Chemical compound [Na+].[Na+].[O-][Mo]([O-])(=O)=O TVXXNOYZHKPKGW-UHFFFAOYSA-N 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- GRYLNZFGIOXLOG-UHFFFAOYSA-N Nitric acid Chemical compound O[N+]([O-])=O GRYLNZFGIOXLOG-UHFFFAOYSA-N 0.000 description 1
- 238000003916 acid precipitation Methods 0.000 description 1
- 150000001298 alcohols Chemical class 0.000 description 1
- 238000005119 centrifugation Methods 0.000 description 1
- 239000013078 crystal Substances 0.000 description 1
- 238000002425 crystallisation Methods 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 238000004090 dissolution Methods 0.000 description 1
- 239000003792 electrolyte Substances 0.000 description 1
- 229910017604 nitric acid Inorganic materials 0.000 description 1
- 239000011780 sodium chloride Substances 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- LSGOVYNHVSXFFJ-UHFFFAOYSA-N vanadate(3-) Chemical compound [O-][V]([O-])([O-])=O LSGOVYNHVSXFFJ-UHFFFAOYSA-N 0.000 description 1
- 229910052720 vanadium Inorganic materials 0.000 description 1
- LEONUFNNVUYDNQ-UHFFFAOYSA-N vanadium atom Chemical compound [V] LEONUFNNVUYDNQ-UHFFFAOYSA-N 0.000 description 1
Landscapes
- Inorganic Compounds Of Heavy Metals (AREA)
Description
本発明は、モリブデン酸塩含有水溶液からモリ
ブデン酸塩を回収する方法に関するものである。
モリブデン酸塩含有水溶液からモリブデンの回
収は、工業的には、モリブデン精鉱を焙焼して得
られる三酸化モリブデンをアルカリ水溶液に溶解
してモリブデン酸塩水溶液とし、これを減圧濃縮
により、モリブデン酸塩{Na2MoO7・2H2Oあ
るいは(NH4)6Mo7O24・4H2O}として晶析する
か、塩酸あるいは硝酸で酸分解してモリブデン酸
(H2MoO4)として回収する方法が行なわれてい
る。
しかしながら、晶析法では溶液の蒸発濃縮に多
大なエネルギーと時間を要する。又、酸沈法では
溶液中に含まれる塩化ナトリウムなどの電解質及
び添加する酸の量によりモリブデン酸の析出は大
きく影響されるなどの欠点がある。
本発明者は、モリブデンとバナジウムを含有す
る水溶液にアンモニウム塩を添加してバナジン酸
塩を析出させ、ろ過により固液分離したとき、析
出塩の洗浄に水洗浄では析出物塩の溶解が大きい
ため、エタノールで洗浄したところ、ろ液が白濁
すると同時に白色の沈澱が析出することを見出す
と共に、この白濁はモリブデン酸塩からなるもの
であることが分析された。本発明者は、このモリ
ブデン酸塩含有水溶液にアルコールを添加すると
モリブデン酸塩が析出する点に着目して、鋭意研
究を行い、本発明をするに至つた。
本発明の方法に従えば、モリブデン含有水溶液
に水と任意の割合で溶解する低級アルコール又は
アセトンを添加することによりモリブデン酸塩を
析出させ回収することができる。
本発明においてモリブデン酸塩析出用に用いる
有機溶媒は、メタノール、エタノール、プロパノ
ール、ブタノールなどの低級アルコール及びアセ
トンである。又、本発明が対象とするモリブデン
酸塩含有水溶液は、モリブデン酸アンモニウム及
びモリブデン酸ナトリウム溶液等である。
モリブデン酸塩含有水溶液に、撹拌しながら前
記有機溶媒を添加すると直ちに白色の粉末状の結
晶が析出し、短時間でモリブデン酸塩の析出は完
了する。モリブデン酸塩の析出物率はモリブデン
酸塩濃度及び有機溶媒添加量が増加するに従つて
高くなる。又、有機溶媒とモリブデン酸塩の析出
率の関係はメタノール<エタノール<プロパノー
ル<ブタノール<アセトンの順であつた。溶液の
PHとモリブデン酸塩の析出率の関係については、
PH5.5から10の範囲ではPHが高くなるに従つてモ
リブデン酸塩の析出率は低下したが、その差は2
%以下であつた。析出温度5℃から40℃の範囲で
は、温度が高くなるに従つてモリブデン酸塩の析
出率はわずかに低下したが、析出温度は常温で十
分である。なお、有機溶媒添加のみではモリブデ
ン酸塩が析出しない低濃度のモリブデン酸塩溶液
でも、アンモニウム塩を添加することによつてモ
リブデン酸塩を析出することができる。このよう
にしてモリブデン酸塩含有水溶液から有機溶媒添
加により析出したモリブデン酸塩はろ過又は遠心
分離などの固液分離法により分離した後、乾燥し
てモリブデン酸塩として回収することがでる。
モリブデン酸アンモニウム水溶液からの析出物
は(NH4)6Mo7O24・4H2O、モリブデン酸ナトリ
ウム溶液からの析出物はNa2MoO4・2H2OがX
線回折により固定された。又、ろ液中に含まれる
有機溶媒は公知の方法により回収し、再利用する
ことができる。
実施例
次に本発明の実施例を示す。
実施例 1
Mo濃度110g/、PH8の(NH4)2MoO4溶液
に有機溶媒を(NH4)2MoO4溶液に対して5倍量
添加し、モリブデン酸塩を析出させたときのMo
としての回収率は、メタノール96.4%、エタノー
ル98.2%、2−プロパノール、98.6%、1−ブタ
ノール98.7%及びアセトン99.8%であつた。
実施例 2
Mo濃度100g/、PH7.6のNa2MoO4溶液にメ
タノール及びエタノールをNa2MoO4溶液に対し
て5倍量添加し、モリブデン酸塩を析出させたと
きのMoとしての回収率は、メタノール91.0%及
びエタノール99.1%であつた。
実施例 3
Mo濃度100g/、PH5.5の(NH4)2MoO4溶
液にメタノールを添加し、モリブデン酸塩を析出
さたときのメタノール添加量比とモリブデン酸塩
のMoとしての回収率との関係を表1に示す。
The present invention relates to a method for recovering molybdate from an aqueous solution containing molybdate. Industrially, molybdenum can be recovered from a molybdate-containing aqueous solution by dissolving molybdenum trioxide obtained by roasting molybdenum concentrate in an alkaline aqueous solution to obtain a molybdate aqueous solution, and then concentrating the molybdate solution under reduced pressure. It can be crystallized as a salt {Na 2 MoO 7・2H 2 O or (NH 4 ) 6 Mo 7 O 24・4H 2 O} or recovered as molybdic acid (H 2 MoO 4 ) by acid decomposition with hydrochloric acid or nitric acid. method is being carried out. However, the crystallization method requires a great deal of energy and time to evaporate and concentrate the solution. Furthermore, the acid precipitation method has the disadvantage that the precipitation of molybdic acid is greatly affected by the electrolyte such as sodium chloride contained in the solution and the amount of acid added. The present inventor added ammonium salt to an aqueous solution containing molybdenum and vanadium to precipitate vanadate, and when solid-liquid separation was performed by filtration, the precipitated salt was washed with water, which caused a large dissolution of the precipitated salt. When washed with ethanol, it was found that the filtrate became cloudy and at the same time a white precipitate was deposited, and it was analyzed that this cloudiness was composed of molybdate. The present inventor focused on the fact that molybdate precipitates when alcohol is added to this molybdate-containing aqueous solution, conducted extensive research, and came up with the present invention. According to the method of the present invention, molybdate can be precipitated and recovered by adding a lower alcohol or acetone that dissolves in an arbitrary ratio with water to a molybdenum-containing aqueous solution. In the present invention, organic solvents used for molybdate precipitation are lower alcohols such as methanol, ethanol, propanol, butanol, and acetone. Further, molybdate-containing aqueous solutions targeted by the present invention include ammonium molybdate and sodium molybdate solutions. When the organic solvent is added to the molybdate-containing aqueous solution while stirring, white powdery crystals are immediately precipitated, and the precipitation of the molybdate is completed in a short time. The molybdate precipitate rate increases as the molybdate concentration and the amount of organic solvent added increase. Furthermore, the relationship between the organic solvent and the precipitation rate of molybdate was in the following order: methanol < ethanol < propanol < butanol < acetone. of solution
Regarding the relationship between pH and molybdate precipitation rate,
In the pH range from 5.5 to 10, the precipitation rate of molybdate decreased as the pH increased, but the difference was 2.
% or less. In the precipitation temperature range of 5°C to 40°C, the precipitation rate of molybdate slightly decreased as the temperature increased, but a room temperature precipitation temperature is sufficient. Note that even in a low-concentration molybdate solution in which molybdate does not precipitate only by adding an organic solvent, molybdate can be precipitated by adding an ammonium salt. The molybdate precipitated from the molybdate-containing aqueous solution by adding an organic solvent in this manner can be separated by a solid-liquid separation method such as filtration or centrifugation, and then dried and recovered as a molybdate. The precipitate from the ammonium molybdate aqueous solution is (NH 4 ) 6 Mo 7 O 24・4H 2 O, and the precipitate from the sodium molybdate solution is Na 2 MoO 4・2H 2 O.
Fixed by line diffraction. Further, the organic solvent contained in the filtrate can be recovered and reused by a known method. Examples Next, examples of the present invention will be shown. Example 1 An organic solvent was added to a (NH 4 ) 2 MoO 4 solution with a Mo concentration of 110 g/, pH 8 in an amount 5 times the amount of the (NH 4 ) 2 MoO 4 solution, and molybdate was precipitated.
The recovery rates were 96.4% for methanol, 98.2% for ethanol, 98.6% for 2-propanol, 98.7% for 1-butanol, and 99.8% for acetone. Example 2 Recovery rate as Mo when molybdate was precipitated by adding methanol and ethanol 5 times the amount of the Na 2 MoO 4 solution to a Na 2 MoO 4 solution with a Mo concentration of 100 g/pH 7.6 was 91.0% methanol and 99.1% ethanol. Example 3 Methanol was added to a (NH 4 ) 2 MoO 4 solution with a Mo concentration of 100 g/PH 5.5 to precipitate molybdate, and the methanol addition amount ratio and the recovery rate of molybdate as Mo The relationship is shown in Table 1.
【表】
実施例 4
種々のMo濃度に調整した(NH4)2MoO4溶液
にメタノールを10倍量添加したときのMo濃度と
Mo回収率の関係を表2に示す。[Table] Example 4 Mo concentration when 10 times the amount of methanol was added to the (NH 4 ) 2 MoO 4 solution adjusted to various Mo concentrations.
Table 2 shows the relationship between Mo recovery rates.
【表】
実施例 5
メタノール添加のみではMoが析出しないMo
濃度6.5g/の(NH4)2MoO4溶液にNH4Clを
加えて、メタノールを10倍量添加したときの
NH4Cl濃度とMo回収率の関係を表3に示す。[Table] Example 5 Mo does not precipitate only by adding methanol
When NH 4 Cl is added to a (NH 4 ) 2 MoO 4 solution with a concentration of 6.5 g/methanol and 10 times the amount of methanol is added,
Table 3 shows the relationship between NH 4 Cl concentration and Mo recovery rate.
Claims (1)
又はアセトンを添加することにより、モリブデン
酸塩を析出させ、この析出物を分離することを特
徴とするモリブデン酸塩含有水溶液からモリブデ
ン酸塩を回収する方法。1. A method for recovering molybdate from a molybdate-containing aqueous solution, which comprises adding a lower alcohol or acetone to the molybdate-containing aqueous solution to precipitate the molybdate and separating the precipitate.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP6539386A JPH0236533B2 (en) | 1986-03-24 | 1986-03-24 | MORIBUDENSANENGANJUSUIYOEKIKARAMORIBUDENSANENOKAISHUSURUHOHO |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP6539386A JPH0236533B2 (en) | 1986-03-24 | 1986-03-24 | MORIBUDENSANENGANJUSUIYOEKIKARAMORIBUDENSANENOKAISHUSURUHOHO |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS62223021A JPS62223021A (en) | 1987-10-01 |
| JPH0236533B2 true JPH0236533B2 (en) | 1990-08-17 |
Family
ID=13285711
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP6539386A Expired - Lifetime JPH0236533B2 (en) | 1986-03-24 | 1986-03-24 | MORIBUDENSANENGANJUSUIYOEKIKARAMORIBUDENSANENOKAISHUSURUHOHO |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0236533B2 (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH02137424U (en) * | 1989-04-19 | 1990-11-16 |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103387264B (en) * | 2013-07-24 | 2017-02-22 | 高立新 | Comprehensive utilization method of molybdenum in waste molybdenum |
| CN109626432A (en) * | 2019-02-21 | 2019-04-16 | 合众思(北京)环境工程有限公司 | A kind of sodium molybdate and sodium chloride waste water recovery process |
-
1986
- 1986-03-24 JP JP6539386A patent/JPH0236533B2/en not_active Expired - Lifetime
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH02137424U (en) * | 1989-04-19 | 1990-11-16 |
Also Published As
| Publication number | Publication date |
|---|---|
| JPS62223021A (en) | 1987-10-01 |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| EXPY | Cancellation because of completion of term |