CN110947523A - Collecting agent for recovering copper, lead and zinc minerals from iron ore dressing tailings - Google Patents

Collecting agent for recovering copper, lead and zinc minerals from iron ore dressing tailings Download PDF

Info

Publication number
CN110947523A
CN110947523A CN201911158404.2A CN201911158404A CN110947523A CN 110947523 A CN110947523 A CN 110947523A CN 201911158404 A CN201911158404 A CN 201911158404A CN 110947523 A CN110947523 A CN 110947523A
Authority
CN
China
Prior art keywords
ester
copper
lead
tailings
zinc
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
Application number
CN201911158404.2A
Other languages
Chinese (zh)
Other versions
CN110947523B (en
Inventor
柏亚林
彭贵熊
王李鹏
胡保栓
郭海宁
包玺琳
巩明辉
王志丰
刘坤
任琳珠
杨俊龙
李健民
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.)
Northwest Research Institute of Mining and Metallurgy
Original Assignee
Northwest Research Institute of Mining and Metallurgy
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 Northwest Research Institute of Mining and Metallurgy filed Critical Northwest Research Institute of Mining and Metallurgy
Priority to CN201911158404.2A priority Critical patent/CN110947523B/en
Publication of CN110947523A publication Critical patent/CN110947523A/en
Application granted granted Critical
Publication of CN110947523B publication Critical patent/CN110947523B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B03SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
    • B03DFLOTATION; DIFFERENTIAL SEDIMENTATION
    • B03D1/00Flotation
    • B03D1/001Flotation agents
    • B03D1/004Organic compounds
    • B03D1/014Organic compounds containing phosphorus
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B03SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
    • B03DFLOTATION; DIFFERENTIAL SEDIMENTATION
    • B03D2201/00Specified effects produced by the flotation agents
    • B03D2201/02Collectors
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B03SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
    • B03DFLOTATION; DIFFERENTIAL SEDIMENTATION
    • B03D2203/00Specified materials treated by the flotation agents; Specified applications
    • B03D2203/02Ores

Landscapes

  • Manufacture And Refinement Of Metals (AREA)

Abstract

The invention belongs to the technical field of mineral flotation, and particularly relates to a collecting agent for comprehensively recovering copper, lead and zinc minerals from iron ore tailings, wherein the collecting agent is composition ester-215, and the ester-215 is prepared from the following raw materials: acrylonitrile diethyl dithiocarbamate, acrylonitrile n-butyl xanthate, ammonium dibutyl dithiophosphate and terpineol oil. Compared with the conventional collecting agent, the ester-215 has the advantages of stronger collecting capability, good selectivity, particularly good collecting effect on secondary sulfides and fine-grained copper-lead-zinc minerals with large mud content, and foaming property, effectively improves the flotation environment of the copper-lead-zinc minerals in iron tailings, improves the floatability, and can realize high-efficiency and quick flotation; meanwhile, the ester-215 has wider requirement on the medium range of ore pulp, the collector can be used in the pH range of 7-13, the effect is good, the capability of collecting pyrite is weaker, and the improvement of the concentrate grade is facilitated.

Description

Collecting agent for recovering copper, lead and zinc minerals from iron ore dressing tailings
Technical Field
The invention belongs to the technical field of mineral flotation, and particularly relates to a collecting agent for comprehensively recovering copper, lead and zinc minerals from iron ore tailings.
Background
Non-ferrous metal resources such as copper, lead and zinc in the nature are increasingly deficient along with the increase of mining intensity, and how to comprehensively recover the metals from secondary resources such as tailings and tailings is a great trend. Many iron ores contain a small amount of nonferrous metals such as copper, lead and zinc, and the like, and can not meet the recovery standard by separate separation, but after iron separation, the nonferrous metal minerals in the ores form secondary enrichment in iron separation tailings, and part of the nonferrous metal minerals meet the comprehensive recovery standard, but because the properties of the iron separation tailings are relatively complex, the conventional collecting agent is adopted, the recovery rate of the nonferrous metals is generally not high, even qualified concentrate products can not be produced, and the following problems mainly exist:
(1) the iron separation tailings have complex components, primary sulfides, secondary sulfides and oxides coexist, and the floatability of the non-ferrous metal minerals is changed to a certain extent under the action of ore grinding and a magnetic field and by adding a beneficiation reagent in the iron separation process;
(2) in the iron ore dressing tailings, because part of minerals are argillized due to early grinding, the floatability of non-ferrous metal minerals in the tailings is poor, and the floatability of part of easily floating gangue is similar, so that the separation is difficult.
Disclosure of Invention
Aiming at the problems and the defects in the prior art, the invention provides a collecting agent for recovering copper, lead and zinc from iron dressing tailings.
In order to achieve the purpose, the invention provides the following technical scheme:
a collector for recovering copper, lead and zinc from iron dressing tailings is a composition ester-215, wherein the ester-215 is prepared from the following raw materials: acrylonitrile diethyl dithiocarbamate, acrylonitrile n-butyl xanthate, ammonium dibutyl dithiophosphate and terpineol oil.
Further, the ester-215 is prepared from the following raw materials in parts by weight: 20-40 parts of diethyldithiocarbamate acrylonitrile ester, 20-40 parts of n-butyl xanthogen acrylonitrile ester, 10-25 parts of dibutyl ammonium dithiophosphate and 10-20 parts of terpineol oil. The raw materials are respectively added into a container and stirred for 30 to 60 minutes under normal temperature and pressure.
Compared with the prior art, the invention has the beneficial effects that:
compared with the conventional collecting agent, the ester-215 has the advantages of stronger collecting capability, good selectivity, particularly good collecting effect on secondary sulfides and fine-grained copper-lead-zinc minerals with large mud content, and foaming property, effectively improves the flotation environment of the copper-lead-zinc minerals in iron tailings, improves the floatability, and can realize high-efficiency and quick flotation; meanwhile, the ester-215 has wider requirement on the medium range of ore pulp, the collector can be used in the pH range of 7-13, the effect is good, the capability of collecting pyrite is weaker, and the improvement of the concentrate grade is facilitated.
Detailed Description
The present invention will be described in detail with reference to the following embodiments.
Example 1
Certain iron ore tailings contain 0.35% of copper and 4.17% of sulfur, and the copper is comprehensively recovered by adopting ester-215.
Step 1: 20 parts of diethyl dithiocarbamic acid acrylonitrile ester, 20 parts of n-butyl xanthogen acrylonitrile ester, 10 parts of dibutyl ammonium dithiophosphate and 20 parts of terpineol oil are added into a container and stirred for 30 minutes at normal temperature and normal pressure to prepare ester-215;
step 2: the tailings are adjusted to the pH value of 12, the ester-215 prepared in the step 1 is added, the mixture is stirred for two minutes to float copper, and copper concentrate can be obtained after two times of fine separation, wherein the technical indexes are shown in Table 1.
Comparative example 1
The iron ore tailings of example 1 are subjected to comprehensive recovery of copper by using butyl xanthate and 2# oil, and the technical indexes are shown in table 1.
Comparative example 2
The iron ore tailings of example 1 are subjected to comprehensive recovery of copper by using ethionamide and butyl xanthate, and the technical indexes are shown in table 1.
Comparative example 3
The iron ore dressing tailings of example 1 are used for comprehensively recovering copper by using azonitrile ester, and the technical indexes are shown in table 1.
Technical indexes of copper-containing iron tailings
Figure 725002DEST_PATH_IMAGE002
Example 2
Certain iron ore tailings contain 0.42% of copper and 1.05% of sulfur, and the copper is comprehensively recovered by adopting ester-215.
Step 1: adding 35 parts of diethyl dithiocarbamic acid acrylonitrile ester, 35 parts of n-butyl xanthogen acrylonitrile ester, 15 parts of dibutyl ammonium dithiophosphate and 15 parts of terpineol oil into a container, and stirring for 40 minutes at normal temperature and normal pressure to prepare ester-215;
step 2: and (3) regulating the pH value of the tailings to be 8, adding the ester-215 prepared in the step (1), stirring for two minutes, and performing flotation on copper, wherein copper concentrate can be obtained after two times of concentration, and the technical indexes are shown in Table 2.
Comparative example 4
The iron ore tailings of example 2 are subjected to comprehensive recovery of copper by using azonitrile ester and butyl xanthate, and the technical indexes are shown in table 2.
Comparative example 5
The iron ore tailings of example 2 are used for comprehensive recovery of copper by using propionitrile xanthate and butyl xanthate, and the technical indexes are shown in table 2.
Technical indexes of copper-containing iron tailings
Figure 173301DEST_PATH_IMAGE004
Example 3
Certain iron ore tailings contain 0.32% of copper, 0.92% of zinc and 1.74% of sulfur, and the copper and the zinc in the iron ore tailings are comprehensively recovered by adopting ester-215.
Step 1: adding 40 parts of diethyl dithiocarbamic acid acrylonitrile ester, 40 parts of n-butyl xanthogen acrylonitrile ester, 25 parts of dibutyl ammonium dithiophosphate and 20 parts of terpineol oil into a container, and stirring at normal temperature and normal pressure for 60 minutes to obtain ester-215;
step 2: the pH value of the tailings is adjusted to be 13, the ester-215 prepared in the step 1 is added, the mixture is stirred for two minutes to float copper and zinc, and copper concentrate and zinc concentrate can be obtained after separation after concentration, wherein the technical indexes are shown in Table 3.
Comparative example 6
The iron ore dressing tailings of example 3 are subjected to comprehensive recovery of copper and zinc by adopting ethidium and azote and 2# oil, and the technical indexes are shown in Table 3.
Comparative example 7
The iron ore tailings of example 3 are treated with ethionamide and butyl xanthate to comprehensively recover copper and zinc, and the technical indexes are shown in table 3.
Technical indexes of tailings of iron separation containing copper and zinc
Figure 484197DEST_PATH_IMAGE006
Example 4
Certain iron ore tailings contain 0.25% of copper, 0.72% of lead, 1.84% of zinc and 3.81% of sulfur, and the copper is comprehensively recovered by adopting ester-215.
Step 1: adding 25 parts of diethyl dithiocarbamic acid acrylonitrile ester, 40 parts of n-butyl xanthogen acrylonitrile ester, 20 parts of dibutyl ammonium dithiophosphate and 15 parts of terpineol oil into a container, and stirring at normal temperature and normal pressure for 35 minutes to obtain ester-215;
step 2: and (3) regulating the pH value of the tailings to 9, adding the ester-215 prepared in the step (1), stirring for two minutes, floating copper and lead and zinc, and separating after concentration to obtain copper concentrate and lead and zinc mixed concentrate, wherein the technical indexes are shown in Table 4.
Comparative example 8
The iron ore tailings of example 4 are treated with ethionamide and ethylxanthate to comprehensively recover copper, lead and zinc, and the technical indexes are shown in Table 4.
Comparative example 9
The iron ore dressing tailings of example 4 are used for comprehensively recovering copper, lead and zinc by using propionitrile xanthate and ethyl xanthate, and the technical indexes are shown in Table 4.
Technical indexes of tailings containing copper, lead and zinc for iron separation are shown in Table 4
Figure 676144DEST_PATH_IMAGE008
The above description is only for the purpose of illustrating the preferred embodiments of the present invention and is not to be construed as limiting the invention, so that any modification, equivalent replacement, or improvement made on the basis of the present invention should be included in the scope of the present invention.

Claims (2)

1. The collector for recovering copper, lead and zinc from iron dressing tailings is characterized in that the collector is composition ester-215, and the ester-215 is prepared from the following raw materials: acrylonitrile diethyl dithiocarbamate, acrylonitrile n-butyl xanthate, ammonium dibutyl dithiophosphate and terpineol oil.
2. The collector for recovering copper, lead and zinc from iron tailings as claimed in claim 1, wherein the ester-215 is prepared from the following raw materials in parts by weight: 20-40 parts of diethyldithiocarbamate acrylonitrile ester, 20-40 parts of n-butyl xanthogen acrylonitrile ester, 10-25 parts of ammonium dibutyldithiophosphate and 10-20 parts of terpineol, and the raw materials are respectively added into a container and stirred for 30-60 minutes at normal temperature and pressure.
CN201911158404.2A 2019-11-22 2019-11-22 Collecting agent for recovering copper, lead and zinc minerals from iron ore dressing tailings Active CN110947523B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201911158404.2A CN110947523B (en) 2019-11-22 2019-11-22 Collecting agent for recovering copper, lead and zinc minerals from iron ore dressing tailings

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201911158404.2A CN110947523B (en) 2019-11-22 2019-11-22 Collecting agent for recovering copper, lead and zinc minerals from iron ore dressing tailings

Publications (2)

Publication Number Publication Date
CN110947523A true CN110947523A (en) 2020-04-03
CN110947523B CN110947523B (en) 2022-05-03

Family

ID=69978277

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201911158404.2A Active CN110947523B (en) 2019-11-22 2019-11-22 Collecting agent for recovering copper, lead and zinc minerals from iron ore dressing tailings

Country Status (1)

Country Link
CN (1) CN110947523B (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN112973967A (en) * 2021-02-04 2021-06-18 中南大学 Composite collecting agent, composite reagent and method for selectively separating galena and chalcopyrite
CN113908995A (en) * 2021-10-13 2022-01-11 紫金矿业集团股份有限公司 High-sulfur gold copper lead ore collecting agent and preparation method thereof

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103350034A (en) * 2013-06-29 2013-10-16 西北矿冶研究院 Method for reducing freezing point of azothion ester collecting agent
CN103447155A (en) * 2013-08-23 2013-12-18 西北矿冶研究院 Ore dressing method for blue chalcocite and pyrite and collecting agent used in ore dressing method
CN104437818A (en) * 2014-11-24 2015-03-25 西北矿冶研究院 Beneficiation method for copper-lead-zinc polymetallic ore
CN109482354A (en) * 2018-11-16 2019-03-19 西北矿冶研究院 Novel combined collecting and foaming agent for sorting copper ores in alpine regions and application thereof

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103350034A (en) * 2013-06-29 2013-10-16 西北矿冶研究院 Method for reducing freezing point of azothion ester collecting agent
CN103447155A (en) * 2013-08-23 2013-12-18 西北矿冶研究院 Ore dressing method for blue chalcocite and pyrite and collecting agent used in ore dressing method
CN104437818A (en) * 2014-11-24 2015-03-25 西北矿冶研究院 Beneficiation method for copper-lead-zinc polymetallic ore
CN109482354A (en) * 2018-11-16 2019-03-19 西北矿冶研究院 Novel combined collecting and foaming agent for sorting copper ores in alpine regions and application thereof

Non-Patent Citations (3)

* Cited by examiner, † Cited by third party
Title
朱玉霜、朱建光: "《浮选药剂的化学原理》", 28 February 1987 *
程秦豫: "N,N-二乙基二硫代氨基甲酸酯衍生物的合成与性能", 《工程科技Ⅰ辑》 *
黄真瑞等: "黄铜矿浮选工艺及捕收剂研究进展 ", 《应用化工》 *

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN112973967A (en) * 2021-02-04 2021-06-18 中南大学 Composite collecting agent, composite reagent and method for selectively separating galena and chalcopyrite
CN113908995A (en) * 2021-10-13 2022-01-11 紫金矿业集团股份有限公司 High-sulfur gold copper lead ore collecting agent and preparation method thereof
CN113908995B (en) * 2021-10-13 2022-11-25 紫金矿业集团股份有限公司 High-sulfur gold copper lead ore collecting agent and preparation method thereof

Also Published As

Publication number Publication date
CN110947523B (en) 2022-05-03

Similar Documents

Publication Publication Date Title
CN109174459B (en) Beneficiation method for high-sulfur lead-zinc ore in high-temperature environment
AU2017101078A4 (en) Beneficiation method for high-clay mixed lead-zinc oxide-sulfide ore
US9475067B2 (en) Chalcopyrite ore beneficiation process and method
CN103433149B (en) Polymetallic sulphide ore flotation process capable of increasing zinc index
CN102896037B (en) Method for beneficiating ion-state copper/cobalt/nickel mine of ore
CN110292984A (en) The embedding cloth type copper sulfide ore substep grinding flotation method of coarse grain containing vitreous copper
CN107362899B (en) Heavy flotation ore combination process for treating complex tungsten-molybdenum-copper-lead-zinc polymetallic ore
CN102513215A (en) Method for separating gold, silver and other metals and sulfur from waste cyanide tailings by floatation
CN102441482A (en) Mineral separation method for scheelite containing rich pyrrhotite
CN109127115B (en) Method for recovering lead-zinc mineral from high-sulfur lead-zinc ore tailings
CN102806148A (en) High-sulfur copper ore collecting agent
CN110947523B (en) Collecting agent for recovering copper, lead and zinc minerals from iron ore dressing tailings
CN110947518A (en) Flotation separation process for high-sulfur low-grade lead-zinc ore
CN1017686B (en) Method for floating copper concentrate from copper, lead and zinc-containing multi-metal complex sulfide ore
CN111632756A (en) Beneficiation method of associated copper-lead-zinc-pyrite
CN105170339B (en) The method for floating of sulphur oxygen mixed mineral in a kind of recovery mine tailing
JP2013212478A (en) Method for dressing ore containing fine mineral
CN110026293B (en) Flotation method for secondary copper-containing high-sulfur copper lead zinc ore
CN117046613A (en) Mineral separation method for efficiently recovering low-grade molybdenum bismuth sulfur polymetallic ore through floatation
CN115007309B (en) Step separation method for antimony and arsenic in high-arsenic complex antimony gold ore
CN113333169B (en) Flotation separation method for copper-lead-zinc mixed flotation concentrate pulp
AU2021101525A4 (en) A Preparation Method of Lead-zinc-Sulphur Mixing, Floating and Separating Inhibitor
CN1242851C (en) Technique for fast selecting plumbum and zinc for sulphidic ore of plumbum-zinc
CN113304888B (en) Speed-division flotation process for sphalerite
CN105689151B (en) A kind of technique that lead, zinc and sulphur are reclaimed from the Gold Concentrate under Normal Pressure phase analysis of high content argillization gangue

Legal Events

Date Code Title Description
PB01 Publication
PB01 Publication
SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination
GR01 Patent grant
GR01 Patent grant