JPH0313531A - Method for solubilizing ruthenium - Google Patents
Method for solubilizing rutheniumInfo
- Publication number
- JPH0313531A JPH0313531A JP1145602A JP14560289A JPH0313531A JP H0313531 A JPH0313531 A JP H0313531A JP 1145602 A JP1145602 A JP 1145602A JP 14560289 A JP14560289 A JP 14560289A JP H0313531 A JPH0313531 A JP H0313531A
- Authority
- JP
- Japan
- Prior art keywords
- ruthenium
- tube
- chloride
- oxide
- ruo4
- 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
Links
- KJTLSVCANCCWHF-UHFFFAOYSA-N Ruthenium Chemical compound [Ru] KJTLSVCANCCWHF-UHFFFAOYSA-N 0.000 title claims description 22
- 229910052707 ruthenium Inorganic materials 0.000 title claims description 22
- 238000000034 method Methods 0.000 title claims description 14
- 230000003381 solubilizing effect Effects 0.000 title claims description 4
- 238000006243 chemical reaction Methods 0.000 claims abstract description 11
- VEXZGXHMUGYJMC-UHFFFAOYSA-M Chloride anion Chemical compound [Cl-] VEXZGXHMUGYJMC-UHFFFAOYSA-M 0.000 claims abstract description 10
- 239000003795 chemical substances by application Substances 0.000 claims abstract description 9
- 238000010438 heat treatment Methods 0.000 claims abstract description 8
- 150000003839 salts Chemical class 0.000 claims description 9
- KZBUYRJDOAKODT-UHFFFAOYSA-N Chlorine Chemical compound ClCl KZBUYRJDOAKODT-UHFFFAOYSA-N 0.000 claims description 7
- YBCAZPLXEGKKFM-UHFFFAOYSA-K ruthenium(iii) chloride Chemical compound [Cl-].[Cl-].[Cl-].[Ru+3] YBCAZPLXEGKKFM-UHFFFAOYSA-K 0.000 claims description 7
- 150000001805 chlorine compounds Chemical class 0.000 claims 1
- 239000003039 volatile agent Substances 0.000 claims 1
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 abstract description 7
- 239000000919 ceramic Substances 0.000 abstract description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract description 4
- 239000004576 sand Substances 0.000 abstract description 3
- 239000000377 silicon dioxide Substances 0.000 abstract description 2
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 abstract 3
- 229910052801 chlorine Inorganic materials 0.000 abstract 3
- 239000000460 chlorine Substances 0.000 abstract 3
- 229910001927 ruthenium tetroxide Inorganic materials 0.000 abstract 3
- WCUXLLCKKVVCTQ-UHFFFAOYSA-M Potassium chloride Chemical compound [Cl-].[K+] WCUXLLCKKVVCTQ-UHFFFAOYSA-M 0.000 abstract 2
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 abstract 2
- UXVMQQNJUSDDNG-UHFFFAOYSA-L Calcium chloride Chemical compound [Cl-].[Cl-].[Ca+2] UXVMQQNJUSDDNG-UHFFFAOYSA-L 0.000 abstract 1
- 229910001626 barium chloride Inorganic materials 0.000 abstract 1
- WDIHJSXYQDMJHN-UHFFFAOYSA-L barium chloride Chemical compound [Cl-].[Cl-].[Ba+2] WDIHJSXYQDMJHN-UHFFFAOYSA-L 0.000 abstract 1
- 239000001110 calcium chloride Substances 0.000 abstract 1
- 229910001628 calcium chloride Inorganic materials 0.000 abstract 1
- 235000011148 calcium chloride Nutrition 0.000 abstract 1
- 239000001103 potassium chloride Substances 0.000 abstract 1
- 239000011780 sodium chloride Substances 0.000 abstract 1
- 230000007928 solubilization Effects 0.000 description 5
- 238000005063 solubilization Methods 0.000 description 5
- 238000005660 chlorination reaction Methods 0.000 description 4
- 239000000843 powder Substances 0.000 description 3
- 239000002516 radical scavenger Substances 0.000 description 3
- 239000000243 solution Substances 0.000 description 3
- 239000007864 aqueous solution Substances 0.000 description 2
- 238000007664 blowing Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 239000002244 precipitate Substances 0.000 description 2
- 239000012495 reaction gas Substances 0.000 description 2
- 229910001925 ruthenium oxide Inorganic materials 0.000 description 2
- WOCIAKWEIIZHES-UHFFFAOYSA-N ruthenium(iv) oxide Chemical compound O=[Ru]=O WOCIAKWEIIZHES-UHFFFAOYSA-N 0.000 description 2
- HEMHJVSKTPXQMS-UHFFFAOYSA-M sodium hydroxide Inorganic materials [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- 238000007740 vapor deposition Methods 0.000 description 2
- 235000014676 Phragmites communis Nutrition 0.000 description 1
- 239000012327 Ruthenium complex Substances 0.000 description 1
- 239000003513 alkali Substances 0.000 description 1
- 230000006835 compression Effects 0.000 description 1
- 238000007906 compression Methods 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 239000006185 dispersion Substances 0.000 description 1
- 238000004090 dissolution Methods 0.000 description 1
- 238000011978 dissolution method Methods 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
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
- Manufacture And Refinement Of Metals (AREA)
Abstract
Description
【発明の詳細な説明】
(産業上の利用分野)
本発明は、ルテニウムおよび/又はその酸化物の塩化反
応と、塩化物の錯塩形成剤との錯塩形成反応とを行い、
可溶性のルテニウム錯塩を作ることを特徴とするルテニ
ウムの可溶化方法に係る。Detailed Description of the Invention (Industrial Application Field) The present invention involves carrying out a chlorination reaction of ruthenium and/or its oxide, and a complex salt-forming reaction of the chloride with a complex salt-forming agent.
The present invention relates to a method for solubilizing ruthenium, which is characterized by producing a soluble ruthenium complex salt.
(従来技術とその問題点)
従来より、リードスイッチ等の接点材料を作る際の蒸着
用ターゲットや、抵抗用材料としてルテニウムが大量に
使用されており、ターゲットの使用残や製造工程で発生
する不良等を回収精製し有効利用する必要がある。(Prior art and its problems) Ruthenium has traditionally been used in large quantities as a vapor deposition target for making contact materials such as reed switches, and as a resistor material. It is necessary to collect, purify, and use them effectively.
一般的にルテニウムの精製は、−旦溶液とした後、その
酸化物であるRub、の揮発性を利用した方法で他と容
易に分離され、精製できるがルテニウムの性質上、溶液
化が難しくNa(10−NaOH混合液を用いて溶解す
る通常の方法では、金属状態の固体は溶解が困難であり
、酸化物に至ってはこの方法での溶解は困難である。Generally, ruthenium can be purified by a method that takes advantage of the volatility of its oxide, Rub, after it is first made into a solution.However, due to the nature of ruthenium, it is difficult to make it into a solution. (By the usual method of dissolving using a 10-NaOH mixture, it is difficult to dissolve metallic solids, and it is difficult to dissolve oxides using this method.
酸化物粉末などは還元を行い金属状粉末とした後上記方
法により溶解する。Oxide powders and the like are reduced into metallic powders and then dissolved by the above method.
またKNO,−KOHなどのアルカリ溶融塩を用いた溶
解法も行われるが、金属状固体に至ってはその溶解速度
が遅く工業的には不適な方法であった。Dissolution methods using alkali molten salts such as KNO and -KOH have also been carried out, but the dissolution rate of metallic solids is slow and is not suitable for industrial use.
(発明の目的)
本発明は、上記の問題を解決すべくなされたものであり
、その目的はルテニウムおよび/又はその酸化物を簡便
かつ効率良く可溶化する方法を提供せんとするものであ
る。(Objective of the Invention) The present invention was made to solve the above problems, and its object is to provide a method for easily and efficiently solubilizing ruthenium and/or its oxide.
(問題点を解決するための手段)
上記問題を解決するための本発明のルテニウム可溶化方
法は、ルテニウムおよび/又はその酸化物を加熱しなが
ら塩素ガスを流すことによりルテニウムおよび/又はそ
の酸化物を塩化物にし揮発させ、その揮発物を塩化物の
錯塩形成剤層を通すことによりルテニウム塩化物と錯塩
形成剤との錯塩形成反応により可溶性のルテニウム塩化
物錯塩を作らせることを特徴とするものである。(Means for Solving the Problems) In order to solve the above problems, the ruthenium solubilization method of the present invention includes heating ruthenium and/or its oxides while flowing chlorine gas. is converted into chloride and volatilized, and the volatile product is passed through a chloride complex salt forming agent layer to form a soluble ruthenium chloride complex salt through a complex salt forming reaction between ruthenium chloride and the complex salt forming agent. It is.
この際の加熱温度は700〜1200℃が好ましい。The heating temperature at this time is preferably 700 to 1200°C.
図1にルテニウムおよびその酸化物の塩化揮発量と温度
との関係を示す。図に示すように700℃以下ではルテ
ニウムの塩化反応は起こるが、揮発に充分な蒸気圧が得
られない。FIG. 1 shows the relationship between the amount of chloride volatilization of ruthenium and its oxides and temperature. As shown in the figure, the chlorination reaction of ruthenium occurs below 700°C, but sufficient vapor pressure for volatilization cannot be obtained.
また850〜950℃に揮発量のピークがあり高温にな
る程効率は低下して行き、1200℃以上では揮発量が
少なくなるばかりでなく加熱にエネルギーを必要とし効
率的でない。Further, there is a peak in the amount of volatilization at 850 to 950°C, and the higher the temperature, the lower the efficiency is. At 1200°C or higher, not only the amount of volatilization decreases, but also energy is required for heating, which is not efficient.
また酸化物の場合も同様であり、酸化物の場合は800
℃以上を必要とする。塩化物の捕集剤には以下のものが
適している。The same applies to oxides, and in the case of oxides, 800
Requires temperature above ℃. Suitable chloride scavengers are:
B a Cj22
K(I
aCjI
Ca C12
M g C12
rc12
(実施例1)
本発明のルテニウム可溶化方法の実施例と従来例を説明
する。B a Cj22 K(I aCjI Ca C12 M g C12 rc12 (Example 1) Examples and conventional examples of the ruthenium solubilization method of the present invention will be described.
先ず本発明のルテニウム可溶化方法の実施例について説
明すると、蒸着用ルテニウムボタン113.62g(ボ
タン24ケ)1を第2図に示す如く反応管(内管)2に
セットした。First, an example of the ruthenium solubilization method of the present invention will be described. 113.62 g of ruthenium buttons (24 buttons) 1 for vapor deposition were set in a reaction tube (inner tube) 2 as shown in FIG.
反応管(内管)2には、塩素ガス加熱用シリカサンド5
およびその上方にガス分散の為の多孔質セラミック4と
セラミックフィルター3を有する機構になっている。そ
の後反応管(外管)10を装填した。In the reaction tube (inner tube) 2, there is a silica sand 5 for heating chlorine gas.
The mechanism has a porous ceramic 4 and a ceramic filter 3 above it for gas dispersion. Thereafter, a reaction tube (outer tube) 10 was loaded.
反応管(外管)10は上部に捕集剤層を有しており、こ
こにBaCj!2を充填した。電気炉(A)7により9
00℃に加熱しながら塩素ガス吹込管6より塩素ガスを
101/min流し塩化反応を行わせた。The reaction tube (outer tube) 10 has a scavenger layer on the top, and BaCj! 2 was filled. Electric furnace (A) 7 by 9
While heating to 00° C., chlorine gas was flowed through the chlorine gas blowing pipe 6 at a rate of 10 1/min to carry out a chlorination reaction.
反応ガスは電気炉(B)8により830℃に加熱された
捕集剤9に充填した13 a C12層を通し、ルテニ
ウム塩化物の捕集を行った。The reaction gas was passed through a 13 a C12 layer packed in a collector 9 heated to 830° C. in an electric furnace (B) 8 to collect ruthenium chloride.
この反応を4時間30分行った後、捕集剤層に充填した
Ba(1!2を取り出し氷で溶かしたところ、沈澱物も
なく (BaRuCj!sの)水溶液となった。After this reaction was carried out for 4 hours and 30 minutes, Ba (1!2) filled in the scavenger layer was taken out and melted with ice, resulting in an aqueous solution (of BaRuCj!s) without any precipitate.
(実施例2)
抵抗ペースト用酸化ルテニウム11粉末180gを圧縮
成形し、第3図に示す如く反応管12にセットした。(Example 2) 180 g of ruthenium oxide 11 powder for resistance paste was compression molded and set in a reaction tube 12 as shown in FIG.
また捕集剤13にはK(lを充填した。Further, the collecting agent 13 was filled with K(l).
電気炉(A)14により酸化ルテニウムを1000℃に
加熱しながら塩素ガス吹込管15より塩素ガスを2f/
min流して塩化反応を行わせた。While heating the ruthenium oxide to 1000°C in the electric furnace (A) 14, chlorine gas is supplied at 2f/2f/2 from the chlorine gas blowing pipe 15.
The chlorination reaction was carried out at a flow rate of min.
反応ガスは電気炉(B)16により750℃に加熱され
た捕集剤13に充填したKCl層を通しルテニウム塩化
物の捕集を行った。The reaction gas was passed through a KCl layer filled in a collector 13 heated to 750° C. in an electric furnace (B) 16 to collect ruthenium chloride.
この反応を7時間行った後、捕集剤層に充填したKCl
を取り出し水で溶かしたところ、沈澱物もなく (K
JuCβ、の)水溶液となった。After carrying out this reaction for 7 hours, the KCl packed in the scavenger layer
When I took it out and dissolved it in water, there was no precipitate (K
It became an aqueous solution of JuCβ.
(従来例)
ルテニウムボタン151g1OをNaCl0 :Na0
H=8 : 1の溶液51に入れ60℃に加熱し、撹拌
しながら溶解を行った。(Conventional example) Ruthenium button 151g1O NaCl0:Na0
The mixture was placed in a solution 51 of H=8:1 and heated to 60° C., and dissolved while stirring.
これを10時間続けたところ、溶解したルテニウムは2
8.30 gであった。When this continued for 10 hours, the amount of dissolved ruthenium was 2
It was 8.30 g.
(発明の効果)
以上の説明で判るように本発明の方法によれば、ルテニ
ウムを効率良く簡便に短時間に可溶化できるというすぐ
れた効果がある。(Effects of the Invention) As can be seen from the above explanation, the method of the present invention has the excellent effect of being able to solubilize ruthenium efficiently, easily, and in a short time.
第1図はルテニウムの塩化揮発量と温度との関係を示す
グラフ、第2図は本発明のルテニウムの可溶化法の一実
施例を示す図、
第3図は本発明の
ルテニウムの可溶化方法の他の実施例を示す図である。Figure 1 is a graph showing the relationship between the amount of ruthenium chloride volatilization and temperature, Figure 2 is a diagram showing an example of the ruthenium solubilization method of the present invention, and Figure 3 is the ruthenium solubilization method of the present invention. It is a figure showing other examples of.
Claims (1)
00℃に加熱しながら塩素ガスを流し、ルテニウムおよ
び/又はその酸化物を塩化物に変えて揮発させ、その揮
発物を塩化物の錯塩形成剤層を通すことによりルテニウ
ム塩化物と塩化物の錯塩形成剤との錯塩形成反応により
、可溶性のルテニウム塩化物錯塩を作ることを特徴とす
るルテニウムの可溶化方法。1. Ruthenium and/or its oxide 700-12
Ruthenium and/or its oxides are converted into chlorides and volatilized by flowing chlorine gas while heating to 00°C, and the volatiles are passed through a chloride complex salt forming agent layer to form a complex salt of ruthenium chloride and chloride. A method for solubilizing ruthenium, which comprises producing a soluble ruthenium chloride complex salt through a complex salt-forming reaction with a forming agent.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP1145602A JPH0313531A (en) | 1989-06-08 | 1989-06-08 | Method for solubilizing ruthenium |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP1145602A JPH0313531A (en) | 1989-06-08 | 1989-06-08 | Method for solubilizing ruthenium |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH0313531A true JPH0313531A (en) | 1991-01-22 |
Family
ID=15388852
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP1145602A Pending JPH0313531A (en) | 1989-06-08 | 1989-06-08 | Method for solubilizing ruthenium |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH0313531A (en) |
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2001073043A (en) * | 1999-07-27 | 2001-03-21 | Anglo American Platinum Corp Ltd | Improvement in refining |
EP2157198A1 (en) | 2008-08-22 | 2010-02-24 | Bayer MaterialScience AG | Method for generating metallic ruthenium or ruthenium compounds from solids containing ruthenium |
US7704469B2 (en) | 2005-12-23 | 2010-04-27 | Basf Aktiengesellschaft | Method for the recovery of ruthenium from used ruthenium oxide-containing catalysts |
WO2010076297A2 (en) | 2008-12-30 | 2010-07-08 | Basf Se | Method for recovering ruthenium from spent catalysts containing ruthenium oxide |
US10316388B2 (en) * | 2011-12-02 | 2019-06-11 | Stillwater Mining Company | Precious metals recovery |
WO2023106244A1 (en) * | 2021-12-06 | 2023-06-15 | セントラル硝子株式会社 | Platinum group element resource recovery device, film formation system, platinum group element resource recovery tube, and platinum group element resource recovery method |
Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH01142040A (en) * | 1987-11-30 | 1989-06-02 | Tanaka Kikinzoku Kogyo Kk | Method for recovering ru |
JPH01142036A (en) * | 1987-11-30 | 1989-06-02 | Tanaka Kikinzoku Kogyo Kk | Method for recovering platinum metal |
JPH01142037A (en) * | 1987-11-30 | 1989-06-02 | Tanaka Kikinzoku Kogyo Kk | Method for recovering platinum metal |
-
1989
- 1989-06-08 JP JP1145602A patent/JPH0313531A/en active Pending
Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH01142040A (en) * | 1987-11-30 | 1989-06-02 | Tanaka Kikinzoku Kogyo Kk | Method for recovering ru |
JPH01142036A (en) * | 1987-11-30 | 1989-06-02 | Tanaka Kikinzoku Kogyo Kk | Method for recovering platinum metal |
JPH01142037A (en) * | 1987-11-30 | 1989-06-02 | Tanaka Kikinzoku Kogyo Kk | Method for recovering platinum metal |
Cited By (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2001073043A (en) * | 1999-07-27 | 2001-03-21 | Anglo American Platinum Corp Ltd | Improvement in refining |
US7704469B2 (en) | 2005-12-23 | 2010-04-27 | Basf Aktiengesellschaft | Method for the recovery of ruthenium from used ruthenium oxide-containing catalysts |
EP2157198A1 (en) | 2008-08-22 | 2010-02-24 | Bayer MaterialScience AG | Method for generating metallic ruthenium or ruthenium compounds from solids containing ruthenium |
DE102008039278A1 (en) | 2008-08-22 | 2010-02-25 | Bayer Materialscience Ag | Process for recovering metallic ruthenium or ruthenium compounds from ruthenium-containing solids |
WO2010076297A2 (en) | 2008-12-30 | 2010-07-08 | Basf Se | Method for recovering ruthenium from spent catalysts containing ruthenium oxide |
US8252253B2 (en) | 2008-12-30 | 2012-08-28 | Basf Se | Process for recovering ruthenium from used ruthenium oxide-comprising catalysts |
US10316388B2 (en) * | 2011-12-02 | 2019-06-11 | Stillwater Mining Company | Precious metals recovery |
US11788170B2 (en) | 2011-12-02 | 2023-10-17 | Stillwater Mining Company | Precious metals recovery |
WO2023106244A1 (en) * | 2021-12-06 | 2023-06-15 | セントラル硝子株式会社 | Platinum group element resource recovery device, film formation system, platinum group element resource recovery tube, and platinum group element resource recovery method |
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