JPH08104526A - Production of rhodium nitrate solution - Google Patents
Production of rhodium nitrate solutionInfo
- Publication number
- JPH08104526A JPH08104526A JP26111294A JP26111294A JPH08104526A JP H08104526 A JPH08104526 A JP H08104526A JP 26111294 A JP26111294 A JP 26111294A JP 26111294 A JP26111294 A JP 26111294A JP H08104526 A JPH08104526 A JP H08104526A
- Authority
- JP
- Japan
- Prior art keywords
- rhodium
- solution
- silver
- heating
- producing
- 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
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- Inorganic Compounds Of Heavy Metals (AREA)
Abstract
Description
【0001】[0001]
【産業上の利用分野】本発明は、ロジウムの持つ特性を
利用した触媒の原料、あるいはロジウム化合物の合成の
ための出発原料となる硝酸ロジウム溶液の製造方法に関
する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for producing a rhodium nitrate solution as a starting material for a catalyst or a starting material for synthesizing a rhodium compound by utilizing the characteristics of rhodium.
【0002】[0002]
【従来の技術】従来、硝酸ロジウム(Rh(NO3)3)溶
液の製造方法としては、塩化ロジウム(RhCl3)溶液
にアルカリ性溶液を加えて中和する工程と、生成した水
酸化ロジウム(Rh(OH)3) を傾斜法により分離して
洗浄する工程と、洗浄した水酸化ロジウムに硝酸(HN
O3)を加えて湯浴中で加熱溶解する工程と、加熱溶解後
に未溶解物をろ過分離する工程とからなる方法、あるい
は塩化ロジウム溶液の代わりに、上記方法によって得ら
れた硝酸ロジウム溶液を用いて上記方法を行う方法が知
られている。2. Description of the Related Art Conventionally, as a method of producing a rhodium nitrate (Rh (NO 3 ) 3 ) solution, a step of adding an alkaline solution to a rhodium chloride (RhCl 3 ) solution to neutralize it and a rhodium hydroxide (Rh (NO 3 ) 3 ) solution produced (OH) 3 ) is separated by a gradient method and washed, and nitric acid (HN 3 ) is added to the washed rhodium hydroxide.
O 3 ), and heating and dissolving in a hot water bath, and a step of filtering and separating undissolved substances after heating and dissolving, or instead of the rhodium chloride solution, the rhodium nitrate solution obtained by the above method is used. There are known methods of performing the above method using the same.
【0003】[0003]
【発明が解決しようとする課題】しかしながら、従来の
硝酸ロジウム溶液の製造方法では、歩留りが悪いと共
に、触媒性能の障害となる塩素イオンの濃度が高く、塩
素イオン濃度を下げるのに工数が多くなるという不具合
がある。However, in the conventional method for producing a rhodium nitrate solution, the yield is poor, and the concentration of chlorine ions, which hinders the catalyst performance, is high, and the number of steps for reducing the concentration of chlorine ions increases. There is a problem called.
【0004】[0004]
【課題を解決するための手段】前記課題を解決するた
め、本発明の硝酸ロジウム溶液の製造方法は、硝酸ロジ
ウム溶液を製造する方法において、塩化ロジウム溶液を
中和する工程と、生成した水酸化ロジウムをろ取した後
洗浄する工程と、洗浄した水酸化ロジウムに硝酸を加え
て加熱溶解する工程と、加熱溶解後に硝酸銀又は酸化銀
液を液中の塩素イオン当量分より過剰に添加して加熱す
る工程と、この加熱後に塩酸を液中に残存する銀イオン
のモル当量分添加して加熱する工程と、生成した塩化銀
をろ過分離する工程とからなることを特徴とする。In order to solve the above-mentioned problems, a method for producing a rhodium nitrate solution of the present invention comprises a step of neutralizing a rhodium chloride solution in the method for producing a rhodium nitrate solution, and a step of producing the generated hydroxide. After the rhodium is filtered off and washed, the nitric acid is added to the washed rhodium hydroxide to dissolve it by heating, and after heating and dissolving, the silver nitrate or silver oxide solution is added in excess of the chloride ion equivalent in the solution and heated. And a step of adding hydrochloric acid by a molar equivalent amount of silver ions remaining in the liquid after the heating and heating, and a step of separating the produced silver chloride by filtration.
【0005】前記各中和する工程は、水酸化カリウム溶
液を用いて行なわれることが好ましい。前記各洗浄する
工程は、中和後生成した水酸化ロジウムを静置した後デ
カンテーションする操作及び/又は純水を加えて静置し
た後デカンテーションする操作を2〜3回繰り返して行
われることが好ましい。又、前記各加熱溶解する工程
は、80℃以上の温度で行われることが好ましい。より好
ましくは、85〜95℃の温度である。一方、前記硝酸銀又
は酸化銀の添加量は、塩素イオンの 1.1〜2倍モル当量
分であることが好ましい。前記硝酸銀又は酸化銀液添加
後の加熱は、85℃以上の温度で行われることが好まし
い。又、前記塩酸添加後の加熱は90℃〜95℃の温度で行
われることが好ましい。Each of the neutralizing steps is preferably carried out using a potassium hydroxide solution. In each of the washing steps, the operation of decanting the rhodium hydroxide generated after neutralization after standing still and / or the operation of decanting after adding pure water and standing still is repeated 2-3 times. Is preferred. Further, it is preferable that each of the heating and melting steps is performed at a temperature of 80 ° C. or higher. More preferably, the temperature is 85 to 95 ° C. On the other hand, the amount of silver nitrate or silver oxide added is preferably 1.1 to 2 times the molar equivalent of chloride ion. The heating after the addition of the silver nitrate or silver oxide solution is preferably performed at a temperature of 85 ° C. or higher. The heating after the addition of hydrochloric acid is preferably performed at a temperature of 90 ° C to 95 ° C.
【0006】[0006]
【作用】本発明の硝酸ロジウム溶液の製造方法において
は、硝酸銀又は酸化銀を液中の塩素イオンのモル当量よ
り過剰に入れるため塩化銀の生成が完全に行なわれ、塩
素イオンが完全に除去できる。In the method for producing a rhodium nitrate solution of the present invention, since silver nitrate or silver oxide is added in excess of the molar equivalent of chloride ions in the solution, silver chloride is completely produced and chloride ions can be completely removed. .
【0007】前記各洗浄する工程が、1回では塩素イオ
ンの除去効果が充分発揮されない。前記各加熱溶解する
工程が、80℃未満の温度で行われると、反応速度が遅く
なる。一方、前記硝酸銀又は酸化銀液の添加量が、塩素
の 1.1倍モル当量分より少ないと、塩化銀の生成が完全
とならず塩素の除去が不完全となる一方、塩素が2倍モ
ル当量分より多いと、ムダになる硝酸銀又は酸化銀が多
くなり、不経済である。前記硝酸銀又は酸化銀液添加後
の加熱が、85℃未満の温度で行われると、反応速度が遅
くなり十分に塩素が除去できなくなる。又、前記塩酸添
加後の加熱を50℃以上とするのは、この範囲で加熱する
と塩化銀の凝集が促進され、その後のろ過性が良くなる
ためである。If each of the above-mentioned washing steps is performed once, the effect of removing chlorine ions is not sufficiently exerted. If the heating and melting steps are carried out at a temperature lower than 80 ° C., the reaction rate becomes slow. On the other hand, when the amount of the silver nitrate or silver oxide solution added is less than 1.1 times the molar equivalent of chlorine, the formation of silver chloride is not complete and the removal of chlorine is incomplete, while the amount of chlorine is twice the molar equivalent. If the amount is larger, wasteful silver nitrate or silver oxide is increased, which is uneconomical. If the heating after the addition of the silver nitrate or silver oxide solution is performed at a temperature lower than 85 ° C., the reaction rate becomes slow and chlorine cannot be sufficiently removed. The heating after the addition of hydrochloric acid is set to 50 ° C. or higher because the heating in this range promotes the aggregation of silver chloride and improves the filterability thereafter.
【0008】[0008]
【実施例】以下、本発明の実施例について比較例と共に
説明する。EXAMPLES Examples of the present invention will be described below together with comparative examples.
【0009】[0009]
【実施例1】塩化ロジウム溶液(Rhとして50g/l)
1lを撹拌しながら4N水酸化カリウム溶液を加え、p
H7まで中和して水酸化ロジウムを生成させた。次い
で、水酸化ロジウムをろ取し、この水酸化ロジウムを洗
浄して塩素イオンを除去した。洗浄は、ろ取した水酸化
ロジウムに純水を1000ml加え撹拌して静置し、デカンテ
ーションする操作を3回行った。次に、洗浄した水酸化
ロジウムに25%硝酸 850mlを加えて85〜95℃の温度の湯
浴中で撹拌しながら7時間加熱溶解した後、硝酸銀液を
液中の塩素イオンの1.1倍モル当量分添加して90〜95℃
の温度の湯浴中で撹拌しながら7時間加熱した。次い
で、上記加熱後に上澄み液中の銀濃度を測定し、塩酸を
液中の残存銀イオンのモル当量分添加して60℃の温度の
湯浴中で撹拌しながら30分間加熱した後、生成した塩化
銀をろ過分離して硝酸ロジウム溶液1000mlを得た。Example 1 Rhodium chloride solution (50 g / l as Rh)
While stirring 1 l, 4N potassium hydroxide solution was added, and p
It was neutralized to H7 to produce rhodium hydroxide. Then, the rhodium hydroxide was collected by filtration, and the rhodium hydroxide was washed to remove chlorine ions. For washing, 1000 ml of pure water was added to the rhodium hydroxide collected by filtration, and the mixture was stirred, allowed to stand, and decanted three times. Next, 850 ml of 25% nitric acid was added to the washed rhodium hydroxide, and the mixture was heated and dissolved in a hot water bath at a temperature of 85 to 95 ° C for 7 hours with stirring, and then the silver nitrate solution was added at 1.1 times the molar equivalent of chloride ion in the solution. 90-95 ℃
The mixture was heated in a water bath at the temperature of 7 hours with stirring. Next, after the above heating, the silver concentration in the supernatant was measured, hydrochloric acid was added in an amount equivalent to the molar equivalent of the remaining silver ions in the liquid, and the mixture was heated for 30 minutes while stirring in a water bath at a temperature of 60 ° C. Silver chloride was separated by filtration to obtain 1000 ml of a rhodium nitrate solution.
【0010】上記硝酸を加えた加熱溶解後の硝酸ロジウ
ム液中のロジウムは、48g/lとなり、歩留り98%以上
であった。又、得られた硝酸ロジウム溶液の塩素イオン
濃度は、Rh50g/lに対し、0.05g/l 以下であり、銀
イオン濃度は5ppm 以下であった。なお、硝酸銀に代え
て酸化銀を用いても同様の作用効果が得られた。The rhodium in the rhodium nitrate solution after heating and dissolution with the above nitric acid added was 48 g / l, and the yield was 98% or more. The rhodium nitrate solution thus obtained had a chloride ion concentration of 0.05 g / l or less and a silver ion concentration of 5 ppm or less with respect to Rh of 50 g / l. Similar effects were obtained even when silver oxide was used instead of silver nitrate.
【0011】[0011]
【比較例1】塩化ロジウム溶液(Rhとして20g/l)
1lを撹拌しながら14%アンモニア水を加え、50〜60℃
の温度でpH7まで中和して水酸化ロジウムを生成させ
た。次いで、デカンテーションにより分離した水酸化ロ
ジウムに実施例1と同様の洗浄を施して塩素イオンを除
去した。次に、洗浄した水酸化ロジウムに20%硝酸 500
mlを加えて 100℃の温度の湯浴中で撹拌しながら8時間
加熱溶解し、冷却した後未溶解物をメンブランフィルタ
ーを用いてろ過分離して硝酸ロジウム溶液 250mlを得
た。[Comparative Example 1] Rhodium chloride solution (Rh: 20 g / l)
While stirring 1 liter, add 14% aqueous ammonia, 50-60 ℃
Was neutralized to pH 7 at the temperature of 1 to produce rhodium hydroxide. Then, the rhodium hydroxide separated by decantation was washed in the same manner as in Example 1 to remove chlorine ions. Then, wash the rhodium hydroxide with 20% nitric acid 500
ml was added and dissolved by heating in a water bath at a temperature of 100 ° C. for 8 hours while stirring, and after cooling, the undissolved substance was separated by filtration using a membrane filter to obtain 250 ml of a rhodium nitrate solution.
【0012】上記硝酸を加えた加熱溶解後の硝酸ロジウ
ム溶液中のロジウムは、56g/lとなり、歩留り70%で
あった。又、得られた硝酸ロジウム溶液の塩素イオン濃
度は、Rh50g/lに対し、2g/l であった。The amount of rhodium in the rhodium nitrate solution after heating and dissolution with the above nitric acid added was 56 g / l, and the yield was 70%. The chloride ion concentration of the obtained rhodium nitrate solution was 2 g / l with respect to Rh 50 g / l.
【0013】[0013]
【発明の効果】以上説明したように、本発明の硝酸ロジ
ウム溶液の製造方法によれば、歩留りが高くなり、又硝
酸銀又は酸化銀液を塩素のモル当量分より過剰に添加す
ることによって、塩素がほぼ完全に除去されるので、硝
酸ロジウム溶液中の塩素イオン濃度をRh50g/lに対
して0.05g/l 以下とすることができる。従って、触媒の
原料に使用した場合、触媒活性の低下がおこらない硝酸
ロジウム溶液を得ることができる。As described above, according to the method for producing a rhodium nitrate solution of the present invention, the yield is high, and by adding silver nitrate or silver oxide solution in excess of the molar equivalent of chlorine, chlorine Is almost completely removed, the chloride ion concentration in the rhodium nitrate solution can be 0.05 g / l or less with respect to Rh 50 g / l. Therefore, when used as a catalyst raw material, a rhodium nitrate solution can be obtained in which the catalytic activity does not decrease.
Claims (7)
て、塩化ロジウム溶液を中和する工程と、生成した水酸
化ロジウムをろ取した後洗浄する工程と、洗浄した水酸
化ロジウムに硝酸を加えて加熱溶解する工程と、加熱溶
解後に硝酸銀又は酸化銀液を液中の塩素イオンのモル当
量分より過剰に添加して加熱する工程と、この加熱後に
塩酸を、液中に残存する銀イオンのモル当量分添加して
加熱する工程と、生成した塩化銀をろ過分離する工程と
からなることを特徴とする硝酸ロジウム溶液の製造方
法。1. A method for producing a rhodium nitrate solution, which comprises a step of neutralizing the rhodium chloride solution, a step of filtering the produced rhodium hydroxide and then washing, and heating the washed rhodium hydroxide with nitric acid. A step of dissolving, a step of heating after adding silver nitrate or silver oxide solution in excess of the molar equivalent of chloride ions in the solution after heating and dissolving, and hydrochloric acid after the heating, a molar equivalent of silver ions remaining in the solution A method for producing a rhodium nitrate solution, which comprises a step of adding and heating minute amounts and a step of separating the produced silver chloride by filtration.
化カリウム溶液を用いて行なうことを特徴とする請求項
1記載の硝酸ロジウム溶液の製造方法。2. The method for producing a rhodium nitrate solution according to claim 1, wherein the step of neutralizing the rhodium chloride is performed using a potassium hydroxide solution.
水酸化ロジウムを静置した後デカンテーションする操作
及び/又は純水を加えて静置した後デカンテーションす
る操作を2〜3回繰り返して行われることを特徴とする
請求項1又は請求項2記載の硝酸ロジウム溶液の製造方
法。3. Each of the washing steps includes an operation of decanting the rhodium hydroxide formed after neutralization after standing still and / or an operation of decanting after adding pure water and standing still 2-3 times. The method for producing a rhodium nitrate solution according to claim 1 or 2, wherein the method is repeated.
温度で行われることを特徴とする請求項1、請求項2又
は請求項3記載の硝酸ロジウム溶液の製造方法。4. The method for producing a rhodium nitrate solution according to claim 1, wherein the heating and melting step is performed at a temperature of 80 ° C. or higher.
中の塩素イオンの1.1乃至2倍モル当量分であることを
特徴とする請求項1、請求項2、請求項3又は請求項4
記載の硝酸ロジウム溶液の製造方法。5. The method according to claim 1, wherein the silver nitrate or silver oxide solution is added in an amount of 1.1 to 2 times the molar equivalent of chloride ion in the solution. Four
A method for producing the rhodium nitrate solution described.
が、85℃以上の温度で行われることを特徴とする請求項
1、請求項2、請求項3、請求項4又は請求項5記載の
硝酸ロジウム溶液の製造方法。6. The heating method after the addition of the silver nitrate or silver oxide solution is performed at a temperature of 85 ° C. or higher, claim 1, claim 2, claim 3, claim 4 or claim 5. Method for producing rhodium nitrate solution of.
度で行われることを特徴とする請求項1、請求項2、請
求項3、請求項4、請求項5又は請求項6記載の硝酸ロ
ジウム溶液の製造方法。7. The heating after the addition of hydrochloric acid is performed at a temperature of 50 ° C. or higher, claim 1, claim 2, claim 3, claim 4, claim 5, or claim 6. Method for producing rhodium nitrate solution of.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP26111294A JP3494485B2 (en) | 1994-09-30 | 1994-09-30 | Method for producing rhodium nitrate solution |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP26111294A JP3494485B2 (en) | 1994-09-30 | 1994-09-30 | Method for producing rhodium nitrate solution |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH08104526A true JPH08104526A (en) | 1996-04-23 |
JP3494485B2 JP3494485B2 (en) | 2004-02-09 |
Family
ID=17357262
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP26111294A Expired - Fee Related JP3494485B2 (en) | 1994-09-30 | 1994-09-30 | Method for producing rhodium nitrate solution |
Country Status (1)
Country | Link |
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JP (1) | JP3494485B2 (en) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101941739A (en) * | 2010-09-20 | 2011-01-12 | 中国海洋石油总公司 | Method for preparing high-purity hydrated rhodium trichloride |
CN103709205A (en) * | 2012-10-09 | 2014-04-09 | 中国石油化工股份有限公司 | Preparation method of acetylacetonatocarbonyltriphenylphosphine rhodium, and olefin hydroformylation method |
CN103709201A (en) * | 2012-10-09 | 2014-04-09 | 中国石油化工股份有限公司 | Preparation method of acetylacetonato dicarbonylrhodium, and olefin hydroformylation method |
CN104610369A (en) * | 2014-11-13 | 2015-05-13 | 昆明贵金属研究所 | Purifying method for acetylacetonatodicarbonyl rhodium |
-
1994
- 1994-09-30 JP JP26111294A patent/JP3494485B2/en not_active Expired - Fee Related
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101941739A (en) * | 2010-09-20 | 2011-01-12 | 中国海洋石油总公司 | Method for preparing high-purity hydrated rhodium trichloride |
CN103709205A (en) * | 2012-10-09 | 2014-04-09 | 中国石油化工股份有限公司 | Preparation method of acetylacetonatocarbonyltriphenylphosphine rhodium, and olefin hydroformylation method |
CN103709201A (en) * | 2012-10-09 | 2014-04-09 | 中国石油化工股份有限公司 | Preparation method of acetylacetonato dicarbonylrhodium, and olefin hydroformylation method |
CN104610369A (en) * | 2014-11-13 | 2015-05-13 | 昆明贵金属研究所 | Purifying method for acetylacetonatodicarbonyl rhodium |
Also Published As
Publication number | Publication date |
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