JPS5992045A - Flotation of nonsulfide mineral - Google Patents
Flotation of nonsulfide mineralInfo
- Publication number
- JPS5992045A JPS5992045A JP57203442A JP20344282A JPS5992045A JP S5992045 A JPS5992045 A JP S5992045A JP 57203442 A JP57203442 A JP 57203442A JP 20344282 A JP20344282 A JP 20344282A JP S5992045 A JPS5992045 A JP S5992045A
- Authority
- JP
- Japan
- Prior art keywords
- minerals
- flotation
- nonsulfide
- sulfide
- sulfide minerals
- 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
Landscapes
- Manufacture And Refinement Of Metals (AREA)
Abstract
Description
【発明の詳細な説明】
げ)技術分野
本発明は製錬含銅残渣物中の非硫化鉱物を選択的に浮遊
選鉱する方法に関するもので、特に浮選の条件剤として
チオ尿素をさらに必要により金属化合物あるいは両者の
錯化合物を使用することを特徴とするものである。[Detailed Description of the Invention] G) Technical Field The present invention relates to a method for selectively flotating non-sulfide minerals in a smelted copper-containing residue, and in particular, it relates to a method for selectively flotating non-sulfide minerals in a smelting copper-containing residue. It is characterized by using a metal compound or a complex compound of both.
(ロ)背景技術
一般に黒鉱の如き複雑鉱物においては、硫化鉱物と重晶
石の如き非硫化鉱物とが混在している。(B) Background Art In general, complex minerals such as black ore contain a mixture of sulfide minerals and non-sulfide minerals such as barite.
従来、この重晶石等の非硫化鉱物を浮遊選鉱法により採
取する場合には、硫化物浮選によって硫化鉱物を分離回
収した後の沈鉱、つまり重晶石等の非硫化鉱物が濃縮し
た沈鉱に対して、非硫化鉱物の浮遊選鉱(重晶石浮選)
を行なう方法が一般に行なわれ、また非硫化鉱物の品質
が強く望まれる場合には、硫化鉱物の浮選を強化するた
めに、過剰の捕収剤を用いて処理する方法等もある。Conventionally, when collecting non-sulfide minerals such as barite using the flotation method, the precipitate after the sulfide minerals are separated and recovered by sulfide flotation, that is, the non-sulfide minerals such as barite are concentrated. Flotation of non-sulfide minerals (barite flotation) for sedimentation
If the quality of non-sulfide minerals is strongly desired, there is also a method in which an excess amount of scavenger is used to enhance the flotation of the sulfide minerals.
さらに、本出願人の提案に係る特公昭!2−21.0/
号公報で詳細に説明しているように、硫化水素の存在下
で硫化鉱物の脱硫浮選を行ない、非硫化鉱物を採取する
方法もある。In addition, the applicant's proposal is based on the Tokukosho! 2-21.0/
As explained in detail in the publication, there is also a method of desulfurizing and flotating sulfide minerals in the presence of hydrogen sulfide to collect non-sulfide minerals.
しかしながら、これらの方法はいずれも第1図のフロー
シートに示すように、原料の浮選を行なって、まず硫化
鉱物を浮鉱とし、非硫化鉱物を沈鉱として分離し、その
復原沈鉱に対し上記諸方法により浮選を行なって非硫化
鉱物を浮鉱として脈石と分離するものであった。However, in all of these methods, as shown in the flow sheet of Figure 1, raw materials are flotated, sulfide minerals are first separated as floating ore, non-sulfide minerals are separated as settled ore, and then restored to the settled ore. On the other hand, by flotation using the above-mentioned methods, non-sulfide minerals were separated from gangue as floating ore.
(ハ)発明の開示
本発明者等は上記従来法に代り経済的かつ効率的な処理
方法を鋭意研究していたところ、チオ尿素と必要により
金属化合物(例えば硫酸亜鉛等の亜鉛塩や硫酸アルミニ
ウム等のアルミニウム塩)又は両者の錯化合物を用いて
浮選を行なうと、硫化鉱物は抑制されて非硫化金鉱物が
捕取剤で選択的に採取できることを見出した。(C) Disclosure of the Invention The present inventors were conducting intensive research into an economical and efficient treatment method in place of the conventional method described above, and discovered that thiourea and, if necessary, a metal compound (e.g., zinc salt such as zinc sulfate, aluminum sulfate, etc.) It has been found that when flotation is carried out using aluminum salts such as (aluminum salts, etc.) or a complex compound of both, sulfide minerals are suppressed and non-sulfide gold minerals can be selectively collected using a scavenger.
即ち、本発明は原料自体から直接浮選工程で目的物であ
る非硫化鉱物を浮鉱とし、硫化鉱物及び脈石を沈鉱とし
て分離することができる処理方法を提供するものである
。That is, the present invention provides a processing method that allows the target non-sulfide mineral to be converted into floating ore and the sulfide mineral and gangue to be separated as precipitate in a direct flotation process from the raw material itself.
チオ尿素と金属化合物又は両者の錯化合物を用いて浮選
する方法としては、本出願人の提案による特公昭!r7
−4!;♂3号公報ならびに特開昭j7−/3乙り57
号公報があるが、これらはいずれも硫化鉱物間の浮選分
離、特に方鉛鉱主体の鉛鉱物を優先的に浮遊させること
を目的とするものであり、本発明とはその機構及び対象
物が異なるものである。As a method of flotation using thiourea and a metal compound, or a complex compound of both, there is a method proposed by the present applicant called Tokkosho! r7
-4! ; ♂ Publication No. 3 and JP-A No. 7-3 Otsuri 57
However, all of these are aimed at flotation separation of sulfide minerals, especially preferentially floating lead minerals mainly composed of galena, and the present invention focuses on the mechanism and target object. are different.
に)比較例
原料としてA鉱山量の含銅残渣(パルプ濃度/j%)を
用い、捕取剤としてKL+、27≠(ジチオリン酸ソー
ダの商品名)7009−/lと起泡剤としてMIBC(
商品名)100y/lを添加し化鉱物を沈鉱として分離
し、浮鉱は銅精鉱として採取した。なお、この硫化鉱物
浮選に際しては、粗選→精選→清掃選が行なわれた。) Comparative Example: Copper-containing residue (pulp concentration/j%) of mine A was used as the raw material, KL+, 27≠ (trade name of sodium dithiophosphate) 7009-/l was used as the scavenger, and MIBC (
(trade name) 100 y/l was added to separate the fossil minerals as precipitated ore, and the floating ore was collected as copper concentrate. In addition, during this sulfide mineral flotation, rough selection → fine selection → cleaning selection was performed.
次に、上記清掃選尾鉱(沈鉱)に対し、非硫化鉱物(鉛
−ハライト鉱、即ちPb5o4とBa5o4の溶融鉱物
)の浮選を行ない、浮鉱側に鉛−バライト精鉱を、沈鉱
側に硅酸等を含んだ脈石とに分離した。このときの浮選
剤としては、捕取剤としてデュオミンT (N−アルキ
ルトリメチレンジアミン成分lr3%の商品名)!rO
f/lのみを用いた。Next, the cleaning tailings (precipitated ore) is subjected to flotation of non-sulfide minerals (lead-halite ore, that is, molten minerals of Pb5o4 and Ba5o4), and lead-barite concentrate is added to the floating ore side. It was separated into gangue containing silicic acid etc. on the ore side. At this time, the flotation agent used as a scavenger was Duomin T (trade name with 3% N-alkyl trimethylene diamine component)! rO
Only f/l was used.
この結果を第1表に示す。The results are shown in Table 1.
以下余白
(ホ)実施例
上記比較例と同じ原料に対し、第2図のフローシートの
如く直接条件剤(抑制剤)−としてチオ尿素l/L0θ
y−/lを添加し、硫化鉱物を抑制しつつ捕収剤デュオ
ミンT / 00 f / tを添加して、常温、 p
H/、、!S’で非硫化鉱物(鉛−パライト鉱)を浮鉱
として回収し、硫化鉱物と脈石を沈鉱として分離した。Below is a margin (e) Example Using the same raw materials as in the above comparative example, thiourea l/L0θ was used as a direct conditioning agent (inhibitor) as shown in the flow sheet of Figure 2.
At room temperature, p
H/,,! At S', non-sulfide minerals (lead-palite ore) were recovered as floating ore, and sulfide minerals and gangue were separated as sediment.
その結果を第2表に示す。The results are shown in Table 2.
以下余白
上記画表を比較して判るように、本発明法によって得ら
れた非硫化鉱物(鉛−パライト鉱)中のAu、Ag、C
u品位は低く、Pb品位が高い。As can be seen by comparing the diagrams in the margins above, Au, Ag, and C in the non-sulfide mineral (lead-palite ore) obtained by the method of the present invention.
The u grade is low and the Pb grade is high.
一般にCu鉱物の形態は、CuSあるいはCu2Sであ
り、Au * AgもCu鉱物に付随していることから
、従来法に比し本発明法は硫化鉱物と非硫化鉱物の分離
性が著しく改善されていることが判る。Generally, the form of Cu minerals is CuS or Cu2S, and since Au*Ag is also associated with Cu minerals, the method of the present invention significantly improves the separation of sulfide minerals and non-sulfide minerals compared to conventional methods. I know that there is.
(へ)発明の効果
以上の如く、本発明法は非硫化鉱物を直接浮鉱として浮
選回収するもので、従来の非硫化鉱物処理の概念を覆す
新規な方法であり、浮選分離性が向上し、処理系統の単
純化により操業コストの低減化を大きく図ることができ
る利点がある。(f) Effects of the Invention As described above, the method of the present invention is a method for flotation recovery of non-sulfide minerals directly as floating ore, and is a new method that overturns the concept of conventional non-sulfide mineral processing. This has the advantage that operating costs can be greatly reduced by simplifying the processing system.
第1図は従来法による非硫化鉱物浮選の70−シート、
第2図は本発明法による非硫化鉱物浮選の70−シート
である。
第1図
第214Figure 1 shows 70 sheets of non-sulfide mineral flotation using the conventional method.
FIG. 2 is a 70-sheet of non-sulfide mineral flotation according to the method of the present invention. Figure 1 214
Claims (1)
硫化鉱物の抑制剤として使用することを特徴とする非硫
化鉱物の浮選法。A method for flotation of non-sulfide minerals, characterized in that thiourea is used as an inhibitor of sulfide minerals in selectively flotating non-sulfide minerals.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP57203442A JPS5992045A (en) | 1982-11-19 | 1982-11-19 | Flotation of nonsulfide mineral |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP57203442A JPS5992045A (en) | 1982-11-19 | 1982-11-19 | Flotation of nonsulfide mineral |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS5992045A true JPS5992045A (en) | 1984-05-28 |
JPS6247417B2 JPS6247417B2 (en) | 1987-10-07 |
Family
ID=16474171
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP57203442A Granted JPS5992045A (en) | 1982-11-19 | 1982-11-19 | Flotation of nonsulfide mineral |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS5992045A (en) |
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5846407A (en) * | 1996-06-17 | 1998-12-08 | Fuerstenau; Douglas W. | Pyrite depressant useful in flotation separation |
US5853571A (en) * | 1996-06-17 | 1998-12-29 | Harris; Guy H. | Pyrite depressant useful in flotation separation |
US5855771A (en) * | 1996-06-17 | 1999-01-05 | Fuerstenau; Douglas W. | Pyrite depressant useful in floation separation |
CN102489406A (en) * | 2011-11-22 | 2012-06-13 | 中国铝业股份有限公司 | Method for treating sulfur bauxite |
CN103521504A (en) * | 2013-10-25 | 2014-01-22 | 赤峰中色锌业有限公司 | Method for comprehensively recovering gold and zinc from high leaching residue and recycling wastewater |
WO2023213100A1 (en) * | 2022-05-05 | 2023-11-09 | 广西华锡集团股份有限公司 | Marmatite and jamesonite flotation method |
Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5418204A (en) * | 1977-07-12 | 1979-02-10 | Agency Of Ind Science & Technol | Word voice identifying device |
-
1982
- 1982-11-19 JP JP57203442A patent/JPS5992045A/en active Granted
Patent Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5418204A (en) * | 1977-07-12 | 1979-02-10 | Agency Of Ind Science & Technol | Word voice identifying device |
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5846407A (en) * | 1996-06-17 | 1998-12-08 | Fuerstenau; Douglas W. | Pyrite depressant useful in flotation separation |
US5853571A (en) * | 1996-06-17 | 1998-12-29 | Harris; Guy H. | Pyrite depressant useful in flotation separation |
US5855771A (en) * | 1996-06-17 | 1999-01-05 | Fuerstenau; Douglas W. | Pyrite depressant useful in floation separation |
CN102489406A (en) * | 2011-11-22 | 2012-06-13 | 中国铝业股份有限公司 | Method for treating sulfur bauxite |
CN103521504A (en) * | 2013-10-25 | 2014-01-22 | 赤峰中色锌业有限公司 | Method for comprehensively recovering gold and zinc from high leaching residue and recycling wastewater |
WO2023213100A1 (en) * | 2022-05-05 | 2023-11-09 | 广西华锡集团股份有限公司 | Marmatite and jamesonite flotation method |
Also Published As
Publication number | Publication date |
---|---|
JPS6247417B2 (en) | 1987-10-07 |
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