JPS61223139A - Method for removing tellurium - Google Patents

Method for removing tellurium

Info

Publication number
JPS61223139A
JPS61223139A JP6329985A JP6329985A JPS61223139A JP S61223139 A JPS61223139 A JP S61223139A JP 6329985 A JP6329985 A JP 6329985A JP 6329985 A JP6329985 A JP 6329985A JP S61223139 A JPS61223139 A JP S61223139A
Authority
JP
Japan
Prior art keywords
copper
tellurium
arsenic
soln
reducing agent
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
JP6329985A
Other languages
Japanese (ja)
Inventor
Takashi Ogata
緒方 俊
Yoichi Chiba
千葉 養一
Shunichi Kasai
笠井 俊一
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.)
Eneos Corp
Original Assignee
Nippon Mining Co Ltd
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 Nippon Mining Co Ltd filed Critical Nippon Mining Co Ltd
Priority to JP6329985A priority Critical patent/JPS61223139A/en
Publication of JPS61223139A publication Critical patent/JPS61223139A/en
Pending legal-status Critical Current

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  • Removal Of Specific Substances (AREA)
  • Manufacture And Refinement Of Metals (AREA)

Abstract

PURPOSE:To remove easily and effectively Te from an acidic aqueous soln. contg. copper and/or arsenic as well as Te even in case of a high concn. of Te by adding copper to the soln. in the presence of a reducing agent. CONSTITUTION:When Te is removed from an acidic aqueous soln. contg. copper and/or arsenic as well as Te such as a copper electrolytic soln. or a soln. obtd. by the oxidation leaching of anode sludge, solid copper and/or deposited copper is added to the soln. in the presence of a reducing agent by an amount >=4 times the amount (gram ion) of the dissolved Te to remove the Te as a Cu-Te compound. The preferred reducing agent is gaseous SO2 and granular, wiry or powdery copper of <=about 10mm diameter and/or length is used as the solid copper.

Description

【発明の詳細な説明】 m口り蝮 本発明は、銅及び又は砒素を含む酸性水溶液中に溶存す
るテルル、例えば狭義には銅製錬工程にて取り扱われる
溶液中に溶存するテルルの除去方法に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for removing tellurium dissolved in an acidic aqueous solution containing copper and/or arsenic, for example, in a narrow sense, tellurium dissolved in a solution handled in a copper smelting process. .

従来立挟権 例えば銅電解工程において、陽極中に含まれるテルルは
殆どが陽極泥中に混入する。この陽極泥中の銅及びまた
は、砒素を除去する目的で酸化浸出すると、テルルの1
0〜15%が浸出される。
Conventionally, in copper electrolysis processes, for example, most of the tellurium contained in the anode is mixed into the anode mud. When oxidized leaching is performed to remove copper and/or arsenic from this anode mud, one of the tellurium
0-15% is leached.

また1条件によっては、前述の銅電解の場合でさえテル
ルが浸出されることがある。
Also, depending on one condition, tellurium may be leached even in the case of copper electrolysis as described above.

しかしながら、これらの液中のテルルの除去には、一般
的に有効とみなされている技術がなく、殆ど黙認されて
いるか又は単に銅粉添加や電解採取等によりわずかに除
去されているにすぎない。
However, there is no technology that is generally considered effective for removing tellurium from these liquids, and it is mostly ignored or only slightly removed by adding copper powder, electrowinning, etc. .

■が  しようとしているシ屯 即ち、銅及び又は砒素を含む酸性水溶液の場合、銅粉を
添加するのみでは、その効果は極めて小さく、電解採取
に至っては除去効果が悪いのみならず多量の銅や砒素も
析出するため処理コストが嵩くなり好ましくない。
In the case of the acid aqueous solution containing copper and/or arsenic, the effect of adding copper powder alone is extremely small, and electrowinning not only has a poor removal effect but also removes a large amount of copper and arsenic. Since arsenic is also precipitated, the processing cost increases, which is not preferable.

そこで、本発明者等が鋭意研究した結果、以下の発明を
なした。
Therefore, as a result of intensive research, the present inventors have made the following invention.

。 占を  するための手 本発明は、銅及び又は砒素を含む酸性水溶液中のテルル
を、溶存しているテルルのグラムイオン量の4倍以上、
還元剤の存在下で固体の銅を加え。
. A method for telling fortune-telling The present invention is based on the present invention, in which tellurium in an acidic aqueous solution containing copper and/or arsenic is at least four times the amount of dissolved tellurium gram ions.
Add solid copper in the presence of a reducing agent.

及び又は、析出した銅を使用し、銅との化合物としてテ
ルルを除去する方法に関する。
And/or relates to a method of removing tellurium as a compound with copper using precipitated copper.

また、その好ましい実施態様としては、還元剤が亜硫酸
ガスであるテルルの除去方法を提供する。
In a preferred embodiment, a method for removing tellurium is provided in which the reducing agent is sulfur dioxide gas.

さらに他の実施態様としては、固体の銅が直径及び又は
長さが、1101I以下の粒状、線状又は粉状であるテ
ルルの除去方法を提供する。
Yet another embodiment provides a method for removing tellurium in which the solid copper is in the form of granules, lines, or powder having a diameter and/or length of 1101I or less.

月11i轟遵]劃1朋− 以下本発明について詳細に述べる。Month 11i Todorojun] Chapter 1 - The present invention will be described in detail below.

本発明において処理対象となる溶液は、銅及び又は砒素
を含む酸性水溶液であり、その例としては、銅電解液や
、陽極泥を酸化浸出した浸出液である。
The solution to be treated in the present invention is an acidic aqueous solution containing copper and/or arsenic, and examples thereof include a copper electrolyte and a leachate obtained by oxidizing and leaching anode mud.

酸性水溶液中のテルルは銅を添加することによリテルル
化銅等の化合物として除去されることは以前から知られ
ている。
It has long been known that tellurium in an acidic aqueous solution can be removed as a compound such as copper litelluride by adding copper.

しかしながら、銅電解液等の各種のイオン種が溶存する
溶液では殆どその効果がない。
However, this effect is almost ineffective in solutions in which various ionic species are dissolved, such as a copper electrolyte.

本発明者等は種々検討した結果、その原因が銅イオン及
び砒素イオンさらには1価の砒素イオンにあることをつ
きとめ、ついで銅及び砒素イオンが存在する条件下でも
テルルを有効に除去する方法を見出した。
As a result of various studies, the inventors of the present invention found that the cause of the problem was copper ions, arsenic ions, and even monovalent arsenic ions, and then devised a method to effectively remove tellurium even under conditions where copper and arsenic ions are present. I found it.

即ち、テルルを還元し、さらには沈殿物として除去する
役割をなす物質は、銅であるが、この反応を可能ならし
むるために還元剤の添加が、不可欠であるということで
ある。
That is, copper is the substance that reduces tellurium and further removes it as a precipitate, but in order to make this reaction possible, it is essential to add a reducing agent.

添加する銅量は、テルルのグラムイオン量の4倍以上を
必要とする。 銅・の形状は、細かいほど少なくて良い
、また銅の直径および又は、長さは、10mm以下であ
ることが好ましい。
The amount of copper added needs to be four times or more the amount of gram ions of tellurium. The finer the shape of the copper, the less the need for it, and the diameter and/or length of the copper is preferably 10 mm or less.

また、オートクレーブ等を用いる場合は、水素を使用す
ることも可能であり、これにより銅粉を析出させる場合
は銅の添加は省くことができる。
Further, when using an autoclave or the like, it is also possible to use hydrogen, and when copper powder is precipitated using hydrogen, addition of copper can be omitted.

還元剤には亜硫酸ガス、亜硫酸ナトリ゛ウム及びチオ硫
酸ナトリウム等がある。いづれも使用できるが、液中の
ナトリウムイオンの増加をきらう場合は、亜硫酸ガスが
好ましい、これらの還元剤の使用量は酸、砒素イオンや
銅イオンの濃度により影響を受けるため一義的には決め
られない、ただ、テルルを除去する際に液中に余剰の還
元剤が存在していることが不可欠である。また、砒素が
1価である場合は、予め三価に還元しておくことが好ま
しい。
Reducing agents include sulfur dioxide gas, sodium sulfite, and sodium thiosulfate. Any of these can be used, but if an increase in sodium ions in the liquid is not desired, sulfur dioxide gas is preferable.The amount of these reducing agents to be used is affected by the concentration of acid, arsenic ions, and copper ions, so it cannot be determined However, it is essential that an excess of reducing agent be present in the solution when removing tellurium. Moreover, when arsenic is monovalent, it is preferable to reduce it to trivalent arsenic in advance.

温度は高い方が好ましいが1通常の操業温度(50〜6
0℃)でも充分である。
A higher temperature is preferable, but 1 normal operating temperature (50 to 6
0°C) is also sufficient.

反応時間は銅、砒素、テルル及び酸の濃度により異なる
が、2時間以上とれば充−分である。
The reaction time varies depending on the concentrations of copper, arsenic, tellurium and acid, but 2 hours or more is sufficient.

i+υ1呆 以上のように本発明を実施することにより、以下の効果
が得られる。
By implementing the present invention as described above, the following effects can be obtained.

(1)銅及び又は砒素を含みかつテルルの高い液であっ
ても、容易にテルルの除去が可能である。
(1) Even if the solution contains copper and/or arsenic and is high in tellurium, tellurium can be easily removed.

(2)この発明により銅電解におけるスライム中のテル
ルが高いものであっても容易にテルルの除去が可能であ
り、好ましい処理が行える。
(2) According to the present invention, tellurium can be easily removed even if the slime in copper electrolysis contains a high amount of tellurium, and a preferable treatment can be performed.

失凰貫よ   ・ (a) Te (VI)とCu (n)を夫々0.55
g/lと40g/l含む水溶液、(b)さらにAs(V
)をLog/l加えたもの、(0)又はAs(II)を
Log/l加えた夫々の水溶液IQに、夫々200メツ
シユ以下の銅粉をテルルのグラムイオン量の8倍加え、
ガラス製反応容器内で60℃に保温しながら攪拌した。
・ (a) Te (VI) and Cu (n) are each 0.55
g/l and an aqueous solution containing 40 g/l, (b) further As(V
), (0) or As(II) (Log/l) was added to each aqueous solution IQ, and 200 mesh or less of copper powder was added to each solution, which was 8 times the gram ion amount of tellurium.
The mixture was stirred in a glass reaction container while being kept at 60°C.

気相の雰囲気は、SO□ガスであった。液中の硫酸濃度
は100〜200g/lの範囲で行ったが影響は小さか
った。
The gas phase atmosphere was SO□ gas. Although the concentration of sulfuric acid in the liquid was in the range of 100 to 200 g/l, the influence was small.

結果を表2に示す、還元剤の添加が非常に有効であるこ
とが判る。
The results are shown in Table 2, and it can be seen that the addition of a reducing agent is very effective.

実施例1に示した(b)の液をオートクレーブに入れ、
150℃で水素分圧が8XIO″Paとなる様に保持し
、1時間反応させた。その結果、液中のテルルは0.0
01g/1未満となり、テルル化銅と銅粉の混合物が得
られた。
Put the solution (b) shown in Example 1 into an autoclave,
The hydrogen partial pressure was maintained at 150°C to be 8XIO''Pa, and the reaction was carried out for 1 hour.As a result, the tellurium in the liquid was 0.0
The ratio was less than 0.01 g/1, and a mixture of copper telluride and copper powder was obtained.

共」1匹 硫酸200g/lを含む水溶液に、(d)Te (■)
を0.53g/l加えたもの、(e)さらにCu(■)
を40g/l加えたもの、(f)さらにAs(■)をL
ogハ加えた夫々の水溶液IQをガラス製反応容器に入
れ、60℃に保温し、200メツシユ以下の銅粉をテル
ルのグラムイオン量の8倍を加え、窒素雰囲気下で攪拌
した0表1に結果を示す。
(d) Te (■) in an aqueous solution containing 200 g/l of sulfuric acid.
(e) plus Cu (■)
40 g/l of (f) and As(■) added to L
Each of the aqueous solutions IQ and IQ added was placed in a glass reaction container, kept at 60°C, and copper powder of 200 mesh or less was added in an amount 8 times the amount of gram ions of tellurium, and stirred under a nitrogen atmosphere. Show the results.

表−l テルルのみの場合(d)は、テルルは銅粉の添加により
速やかに除去されうるが、銅イオンや砒素イオンが存在
すると(e)又は(f)テルルの除去が極めて困難にな
ることがわかる。
Table 1 In the case of tellurium only (d), tellurium can be quickly removed by adding copper powder, but if copper ions or arsenic ions are present (e) or (f) it becomes extremely difficult to remove tellurium. I understand.

Claims (3)

【特許請求の範囲】[Claims] (1)銅及び又は砒素を含む酸性水溶液中のテルルを、
溶存しているテルルのグラムイオン量の4倍以上、還元
剤の存在下で固体の銅を加え、及び又は、析出した銅を
使用し、銅との化合物としてテルルを除去することを特
徴とするテルルの除去方法。
(1) Tellurium in an acidic aqueous solution containing copper and or arsenic,
It is characterized by adding solid copper in the presence of a reducing agent and/or using precipitated copper to remove tellurium as a compound with copper at least four times the amount of dissolved tellurium gram ions. How to remove tellurium.
(2)還元剤が亜硫酸ガスであることを特徴とする特許
請求の範囲第一項記載のテルルの除去方法。
(2) The method for removing tellurium according to claim 1, wherein the reducing agent is sulfur dioxide gas.
(3)固体の銅が直径及び又は長さが、10mm以下の
粒状、線状又は粉状であることを特徴とする特許請求の
範囲第一項記載のテルルの除去方法。
(3) The method for removing tellurium according to claim 1, wherein the solid copper is in the form of particles, lines, or powder with a diameter and/or length of 10 mm or less.
JP6329985A 1985-03-29 1985-03-29 Method for removing tellurium Pending JPS61223139A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP6329985A JPS61223139A (en) 1985-03-29 1985-03-29 Method for removing tellurium

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP6329985A JPS61223139A (en) 1985-03-29 1985-03-29 Method for removing tellurium

Publications (1)

Publication Number Publication Date
JPS61223139A true JPS61223139A (en) 1986-10-03

Family

ID=13225293

Family Applications (1)

Application Number Title Priority Date Filing Date
JP6329985A Pending JPS61223139A (en) 1985-03-29 1985-03-29 Method for removing tellurium

Country Status (1)

Country Link
JP (1) JPS61223139A (en)

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5792147A (en) * 1980-09-30 1982-06-08 Inco Ltd Wet metallurgy treatment of noble metal containing substance

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5792147A (en) * 1980-09-30 1982-06-08 Inco Ltd Wet metallurgy treatment of noble metal containing substance

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