CN106824550A - A kind of iron mineral inhibitor and preparation method thereof - Google Patents

A kind of iron mineral inhibitor and preparation method thereof Download PDF

Info

Publication number
CN106824550A
CN106824550A CN201710177011.0A CN201710177011A CN106824550A CN 106824550 A CN106824550 A CN 106824550A CN 201710177011 A CN201710177011 A CN 201710177011A CN 106824550 A CN106824550 A CN 106824550A
Authority
CN
China
Prior art keywords
parts
weight
mixture
conditions
high effective
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
CN201710177011.0A
Other languages
Chinese (zh)
Other versions
CN106824550B (en
Inventor
梅建庭
杨威
曹翠
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.)
Anshan Jinxiang Industrial Co ltd
Original Assignee
Liaoning Bao Xiang Technology 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 Liaoning Bao Xiang Technology Co Ltd filed Critical Liaoning Bao Xiang Technology Co Ltd
Priority to CN201710177011.0A priority Critical patent/CN106824550B/en
Publication of CN106824550A publication Critical patent/CN106824550A/en
Application granted granted Critical
Publication of CN106824550B publication Critical patent/CN106824550B/en
Withdrawn - After Issue legal-status Critical Current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
    • B03D1/018Mixtures of inorganic and organic compounds
    • 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
    • B03D2201/06Depressants
    • 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

  • Chemical & Material Sciences (AREA)
  • Inorganic Chemistry (AREA)
  • Epoxy Compounds (AREA)
  • Polysaccharides And Polysaccharide Derivatives (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Abstract

The invention discloses a kind of preparation method of iron mineral inhibitor:The first step is reacted 1~4h and obtains auxiliary agent (1) by following parts by weight of component mixture at 60 DEG C~90 DEG C:0.5~4.0 part of 100 parts of cornstarch, tapioca or wheaten starch, caustic alcohol or NaOH, 5~15 parts of sodium chloroacetate, second step react 3~6h and obtain auxiliary agent (2) by following parts by weight of component mixture at 50 DEG C~80 DEG C:0.2~1.0 part of (1) 100 part of the auxiliary agent obtained by the above-mentioned first step, 5~15 parts of oxirane, sodium carbonate or sodium acetate, the 3rd step are reacted at 30 DEG C~60 DEG C 1~3h by following parts by weight of component mixture and are inhibited agent finished product:(2) 100 parts of the auxiliary agent obtained by above-mentioned second step, sodium metaperiodate or 0.2~1.0 part of 1~12 part of hydrogen peroxide, ferrous sulfate or copper sulphate.

Description

A kind of iron mineral inhibitor and preparation method thereof
Technical field
The present invention relates to a kind of iron mineral inhibitor and preparation method thereof, belong to beneficiation reagent technical field.
Background technology
The inhibitor that floatation of iron mineral is used mainly has micromolecular inhibitor and the class of macromolecular inhibitor two.Little molecules in inhibiting Agent has waterglass, calgon, tartaric acid etc.;Macromolecular inhibitor has starch, carboxymethylcellulose calcium, sodium humate, dextrin With polyacrylamide etc..Most widely used in these inhibitor is cornstarch, when suppressing iron mineral using cornstarch, often There is mine tailing grade high not enough.Its reason is cornstarch weaker to the ability to function of fine grained iron mineral, causes fine grained iron ore Thing is easily accessible in mine tailing, causes Iron Grade of Tailings high, and iron recovery is low.
The content of the invention
It is an object of the invention to provide a kind of preparation method of iron mineral inhibitor, this inhibitor collection carboxyl, ethyoxyl With aldehyde radical in one, the group acted on fine grained iron mineral is increased, increases the length that group is acted on particulate iron mineral, Fine grained iron mineral can be suppressed in concentrate.Solve former cornstarch inhibitor weak to fine grained iron mineral ability to function, The problems such as rejection ability is not strong, improves concentrate grade and metal recovery rate, reduces tailings grade.
The purpose of the present invention is realized by following technical proposals:
The present invention provides a kind of preparation method of iron mineral inhibitor, comprises the steps:
The first step is reacted under the conditions of 60 DEG C~90 DEG C by the mixture of following parts by weight of component and obtained within 1~4 hour efficiently Auxiliary agent 1:
100 parts of starch
0.5~4.0 part of caustic alcohol or sodium hydroxide catalyst
5~15 parts of sodium chloroacetate
Second step is reacted under the conditions of 50 DEG C~80 DEG C by the mixture of following parts by weight of component and obtained within 3~6 hours efficiently Auxiliary agent 2:
1 100 parts of the high effective additives obtained by the above-mentioned first step
5~15 parts of oxirane
0.2~1.0 part of sodium carbonate or sodium acetate catalyst
3rd step is reacted under the conditions of 30 DEG C~60 DEG C by the mixture of following parts by weight of component and is inhibited for 1~3 hour Agent finished product:
2 100 parts of the high effective additives obtained by above-mentioned second step
1~12 part of sodium metaperiodate or hydrogen peroxide
0.2~1.0 part of ferrous sulfate or bluestone catalyst
Described starch is cornstarch, tapioca, wheaten starch.
The different preparation method of selection can obtain the inhibitor of different performance.
Further, in the above-mentioned technical solutions, a kind of preparation method of iron mineral inhibitor, it is preferable that including following steps Suddenly:
The first step is reacted under the conditions of 82 DEG C~85 DEG C by the mixture of following parts by weight of component and obtains high effective additives in 2 hours 1:
100 parts of cornstarch
0.6~1.0 part of ethanol sodium catalyst
7~10 parts of sodium chloroacetate
Second step is reacted under the conditions of 73 DEG C~75 DEG C by the mixture of following parts by weight of component and obtained within 4~5 hours efficiently Auxiliary agent 2:
1 100 parts of the high effective additives obtained by the above-mentioned first step
7~8 parts of oxirane
0.4~0.8 part of sodium acetate catalyst
3rd step is reacted under the conditions of 52 DEG C~55 DEG C by the mixture of following parts by weight of component and is inhibited for 2~3 hours Agent finished product:
2 100 parts of the high effective additives obtained by above-mentioned second step
2~3 parts of sodium metaperiodate
0.3~0.4 part of bluestone catalyst.
Further, in the above-mentioned technical solutions, a kind of preparation method of iron mineral inhibitor, it is preferable that including following steps Suddenly:
The first step is reacted under the conditions of 82 DEG C~85 DEG C by the mixture of following parts by weight of component and obtains high effective additives in 2 hours 1:
100 parts of tapioca
2.0~3.0 parts of sodium hydroxide catalyst
8~11 parts of sodium chloroacetate
Second step is reacted under the conditions of 72 DEG C~75 DEG C by the mixture of following parts by weight of component and obtained within 4~5 hours efficiently Auxiliary agent 2:
1 100 parts of the high effective additives obtained by the above-mentioned first step
7~8 parts of oxirane
0.4~0.8 part of sodium carbonate catalyst
3rd step is reacted under the conditions of 52 DEG C~55 DEG C by the mixture of following parts by weight of component and is inhibited for 2~3 hours Agent finished product:
2 100 parts of the high effective additives obtained by above-mentioned second step
7~10 parts of hydrogen peroxide
0.3~0.4 part of ferrous sulfate catalyst
Further, in the above-mentioned technical solutions, a kind of preparation method of iron mineral inhibitor, it is preferable that including following steps Suddenly:
The first step is reacted under the conditions of 82 DEG C~85 DEG C by the mixture of following parts by weight of component and obtains high effective additives in 2 hours 1:
100 parts of wheaten starch
2.0~3.0 parts of sodium hydroxide catalyst
8~11 parts of sodium chloroacetate
Second step is reacted under the conditions of 73 DEG C~75 DEG C by the mixture of following parts by weight of component and obtained within 4~5 hours efficiently Auxiliary agent 2:
1 100 parts of the high effective additives obtained by the above-mentioned first step
7~8 parts of oxirane
0.4~0.8 part of sodium carbonate catalyst
3rd step is reacted under the conditions of 53 DEG C~55 DEG C by the mixture of following parts by weight of component and is inhibited for 2~3 hours Agent finished product:
2 100 parts of the high effective additives obtained by above-mentioned second step
7~10 parts of hydrogen peroxide
0.3~0.4 part of ferrous sulfate catalyst
The present invention provides the iron mineral inhibitor that a kind of above-mentioned preparation method is obtained.
Invention beneficial effect
The present invention is pressed down by the iron mineral that three-step reaction forms carboxyl, ethyoxyl and carbonyl functional group on starch molecule Preparation, this inhibitor is a kind of iron mineral grade polymeric inhibitor wide.Strengthened by groups such as hydroxyl, ether and carbonyls With the useful effect of iron mineral, the selectivity acted on iron mineral is improve.Particularly significantly increase suppression fine grained iron ore The ability to function of stone, expands the scope for suppressing iron ore particle diameter, considerably reduces flotation tailing, realizes " carrying iron drop tail " Purpose.
Specific embodiment
Following non-limiting examples can make one of ordinary skill in the art be more fully understood the present invention, but not with Any mode limits the present invention.
Embodiment 1
The first step is reacted under the conditions of 82 DEG C~85 DEG C by the mixture of following parts by weight of component and obtains high effective additives in 2 hours 1:
100 parts of cornstarch
0.8 part of ethanol sodium catalyst
8 parts of sodium chloroacetate
Second step is reacted under the conditions of 73 DEG C~75 DEG C by the mixture of following parts by weight of component and obtained within 4~5 hours efficiently Auxiliary agent 2:
1 100 parts of the high effective additives obtained by the above-mentioned first step
8 parts of oxirane
0.6 part of sodium acetate catalyst
3rd step is reacted under the conditions of 52 DEG C~55 DEG C by the mixture of following parts by weight of component and is inhibited for 2~3 hours Agent finished product:
2 100 parts of the high effective additives obtained by above-mentioned second step
3 parts of sodium metaperiodate
0.4 part of bluestone catalyst
Properties of product:Compared with East Anshan industrial application causticization cornstarch inhibitor, 13 DEG C of floatation of iron ore temperature reduction, Iron concentrate grade improves 0.2%, Iron Grade of Tailings reduction by 2.4%, unit consumption of medicine raising 20%.
Embodiment 2
The first step is reacted under the conditions of 82 DEG C~85 DEG C by the mixture of following parts by weight of component and obtains high effective additives in 2 hours 1:
100 parts of tapioca
3.0 parts of sodium hydroxide catalyst
10 parts of sodium chloroacetate
Second step is reacted under the conditions of 72 DEG C~75 DEG C by the mixture of following parts by weight of component and obtained within 4~5 hours efficiently Auxiliary agent 2:
1 100 parts of the high effective additives obtained by the above-mentioned first step
8 parts of oxirane
0.6 part of sodium carbonate catalyst
3rd step is reacted under the conditions of 52 DEG C~55 DEG C by the mixture of following parts by weight of component and is inhibited for 2~3 hours Agent finished product:
2 100 parts of the high effective additives obtained by above-mentioned second step
9 parts of hydrogen peroxide
0.4 part of ferrous sulfate catalyst
Properties of product:Compared with East Anshan industrial application causticization cornstarch inhibitor, 15 DEG C of floatation of iron ore temperature reduction, Iron concentrate grade reduction by 0.15%, Iron Grade of Tailings reduction by 1.73, unit consumption of medicine improves 10%.
Embodiment 3
The first step is reacted under the conditions of 82 DEG C~85 DEG C by the mixture of following parts by weight of component and obtains high effective additives in 2 hours 1:
100 parts of wheaten starch
3.0 parts of sodium hydroxide catalyst
10 parts of sodium chloroacetate
Second step is reacted under the conditions of 73 DEG C~75 DEG C by the mixture of following parts by weight of component and obtained within 4~5 hours efficiently Auxiliary agent 2:
1 100 parts of the high effective additives obtained by the above-mentioned first step
8 parts of oxirane
0.8 part of sodium carbonate catalyst
3rd step is reacted under the conditions of 53 DEG C~55 DEG C by the mixture of following parts by weight of component and is inhibited for 2~3 hours Agent finished product:
2 100 parts of the high effective additives obtained by above-mentioned second step
9 parts of hydrogen peroxide
0.4 part of ferrous sulfate catalyst
Properties of product:Compared with East Anshan industrial application causticization cornstarch inhibitor, 14 DEG C of floatation of iron ore temperature reduction, Iron concentrate grade reduction by 0.08%, Iron Grade of Tailings reduction by 1.54, unit consumption of medicine improves 12%.
Embodiment 4
The first step is reacted under the conditions of 80 DEG C~82 DEG C by the mixture of following parts by weight of component and obtains high effective additives in 2 hours 1:
100 parts of cornstarch
2.5 parts of sodium hydroxide catalyst
10 parts of sodium chloroacetate
Second step is reacted under the conditions of 72 DEG C~74 DEG C by the mixture of following parts by weight of component and obtained within 4~5 hours efficiently Auxiliary agent 2:
1 100 parts of the high effective additives obtained by the above-mentioned first step
8 parts of oxirane
0.7 part of sodium carbonate catalyst
3rd step is reacted under the conditions of 53 DEG C~55 DEG C by the mixture of following parts by weight of component and is inhibited for 2~3 hours Agent finished product:
2 100 parts of the high effective additives obtained by above-mentioned second step
10 parts of hydrogen peroxide
0.3 part of ferrous sulfate catalyst
Properties of product:Compared with East Anshan industrial application causticization cornstarch inhibitor, 13 DEG C of floatation of iron ore temperature reduction, Iron concentrate grade improves 0.02%, Iron Grade of Tailings reduction by 2.04%, unit consumption of medicine raising 12%.
Embodiment 5
The first step is reacted under the conditions of 82 DEG C~84 DEG C by the mixture of following parts by weight of component and obtains high effective additives in 2 hours 1:
100 parts of cornstarch
1.8 parts of sodium hydroxide catalyst
13 parts of sodium chloroacetate
Second step is reacted under the conditions of 74 DEG C~75 DEG C by the mixture of following parts by weight of component and obtained within 4~5 hours efficiently Auxiliary agent 2:
1 100 parts of the high effective additives obtained by the above-mentioned first step
8 parts of oxirane
0.3 part of sodium carbonate catalyst
3rd step is reacted under the conditions of 53 DEG C~55 DEG C by the mixture of following parts by weight of component and is inhibited for 2~3 hours Agent finished product:
2 100 parts of the high effective additives obtained by above-mentioned second step
10 parts of hydrogen peroxide
0.3 part of ferrous sulfate catalyst
Properties of product:Compared with East Anshan industrial application causticization cornstarch inhibitor, 15 DEG C of floatation of iron ore temperature reduction, Iron concentrate grade draft 0.05%, Iron Grade of Tailings reduction by 2.43%, unit consumption of medicine improves 11%.

Claims (5)

1. a kind of preparation method of iron mineral inhibitor, it is characterised in that comprise the steps:
The first step is reacted under the conditions of 60 DEG C~90 DEG C by the mixture of following parts by weight of component and obtains high effective additives 1 in 1~4 hour:
100 parts of starch
0.5~4.0 part of caustic alcohol or sodium hydroxide catalyst
5~15 parts of sodium chloroacetate
Second step is reacted under the conditions of 50 DEG C~80 DEG C by the mixture of following parts by weight of component and obtains high effective additives 2 in 3~6 hours:
1 100 parts of the high effective additives obtained by the above-mentioned first step
5~15 parts of oxirane
0.2~1.0 part of sodium carbonate or sodium acetate catalyst
3rd step reacts the agent finished product that is inhibited for 1~3 hour by the mixture of following parts by weight of component under the conditions of 30 DEG C~60 DEG C:
2 100 parts of the high effective additives obtained by above-mentioned second step
1~12 part of sodium metaperiodate or hydrogen peroxide
0.2~1.0 part of ferrous sulfate or bluestone catalyst
Described starch is cornstarch, tapioca, wheaten starch.
2. the preparation method of a kind of iron mineral inhibitor according to claim 1, it is characterised in that:The described first step by The mixture of following parts by weight of component reacts under the conditions of 82 DEG C~85 DEG C and obtains high effective additives 1 in 2 hours:
100 parts of cornstarch
0.6~1.0 part of ethanol sodium catalyst
7~10 parts of sodium chloroacetate
Described second step is reacted under the conditions of 73 DEG C~75 DEG C by the mixture of following parts by weight of component and obtains height in 4~5 hours Effect auxiliary agent 2:
1 100 parts of the high effective additives obtained by the above-mentioned first step
7~8 parts of oxirane
0.4~0.8 part of sodium acetate catalyst
3rd step reacts the agent finished product that is inhibited for 2~3 hours by the mixture of following parts by weight of component under the conditions of 52 DEG C~55 DEG C:
2 100 parts of the high effective additives obtained by above-mentioned second step
2~3 parts of sodium metaperiodate
0.3~0.4 part of bluestone catalyst.
3. the preparation method of a kind of iron mineral inhibitor according to claim 1, it is characterised in that:The described first step by The mixture of following parts by weight of component reacts under the conditions of 82 DEG C~85 DEG C and obtains high effective additives 1 in 2 hours:
100 parts of tapioca
2.0~3.0 parts of sodium hydroxide catalyst
8~11 parts of sodium chloroacetate
Described second step is reacted under the conditions of 72 DEG C~75 DEG C by the mixture of following parts by weight of component and obtains height in 4~5 hours Effect auxiliary agent 2:
1 100 parts of the high effective additives obtained by the above-mentioned first step
7~8 parts of oxirane
0.4~0.8 part of sodium carbonate catalyst
3rd step reacts the agent finished product that is inhibited for 2~3 hours by the mixture of following parts by weight of component under the conditions of 52 DEG C~55 DEG C:
2 100 parts of the high effective additives obtained by above-mentioned second step
7~10 parts of hydrogen peroxide
0.3~0.4 part of ferrous sulfate catalyst.
4. the preparation method of a kind of iron mineral inhibitor according to claim 1, it is characterised in that:The described first step by The mixture of following parts by weight of component reacts under the conditions of 82 DEG C~85 DEG C and obtains high effective additives 1 in 2 hours:
100 parts of wheaten starch
2.0~3.0 parts of sodium hydroxide catalyst
8~11 parts of sodium chloroacetate
Described second step is reacted under the conditions of 73 DEG C~75 DEG C by the mixture of following parts by weight of component and obtains height in 4~5 hours Effect auxiliary agent 2:
1 100 parts of the high effective additives obtained by the above-mentioned first step
7~8 parts of oxirane
0.4~0.8 part of sodium carbonate catalyst
3rd step reacts the agent finished product that is inhibited for 2~3 hours by the mixture of following parts by weight of component under the conditions of 53 DEG C~55 DEG C:
2 100 parts of the high effective additives obtained by above-mentioned second step
7~10 parts of hydrogen peroxide
0.3~0.4 part of ferrous sulfate catalyst.
5. such as right wants the iron mineral inhibitor that 1~4 any one preparation method is obtained.
CN201710177011.0A 2017-03-22 2017-03-22 A kind of iron mineral inhibitor and preparation method thereof Withdrawn - After Issue CN106824550B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201710177011.0A CN106824550B (en) 2017-03-22 2017-03-22 A kind of iron mineral inhibitor and preparation method thereof

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201710177011.0A CN106824550B (en) 2017-03-22 2017-03-22 A kind of iron mineral inhibitor and preparation method thereof

Publications (2)

Publication Number Publication Date
CN106824550A true CN106824550A (en) 2017-06-13
CN106824550B CN106824550B (en) 2018-12-04

Family

ID=59130985

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201710177011.0A Withdrawn - After Issue CN106824550B (en) 2017-03-22 2017-03-22 A kind of iron mineral inhibitor and preparation method thereof

Country Status (1)

Country Link
CN (1) CN106824550B (en)

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107961902A (en) * 2017-11-22 2018-04-27 北京矿冶研究总院 Composite inhibitor for inhibiting gangue contained in copper minerals and use method and application thereof
CN108620240A (en) * 2018-05-22 2018-10-09 中南大学 A kind of sulfide mineral inhibitor of bismuth and its application
CN108787176A (en) * 2018-05-22 2018-11-13 中南大学 A kind of application of the based compound containing peroxide
CN112774869A (en) * 2020-12-25 2021-05-11 厦门紫金矿冶技术有限公司 Pyrite inhibitor, preparation thereof and application thereof in copper-lead-zinc multi-metal sulfide ores
CN114011581A (en) * 2021-11-09 2022-02-08 昆明理工大学 Preparation method and application of inhibitor for copper-sulfur separation under weak acidic condition
CN114011582A (en) * 2021-11-09 2022-02-08 昆明理工大学 Flotation method for improving beneficiation index of gold-bearing copper sulfide ore

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1231219A (en) * 1999-03-26 1999-10-13 清华大学 Process for preparing iron ore antifloating inhibitor
CN1356178A (en) * 2001-01-11 2002-07-03 徐井春 Reverse floatation depressant of iron ore and its preparing process
CN102443071A (en) * 2011-11-16 2012-05-09 广西大学 Composite modified starch as hematite reverse flotation inhibitor and preparation method thereof
CN103567078A (en) * 2013-11-13 2014-02-12 鞍钢集团矿业公司 Carboxymethyl starch inhibitor for reverse flotation of hematite
CN104190549A (en) * 2014-09-03 2014-12-10 鞍钢集团矿业公司 Composite inhibitor for reverse flotation of hematite
CN104437889A (en) * 2014-12-09 2015-03-25 鞍钢集团矿业公司 Hematite anti-floatation depressor

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1231219A (en) * 1999-03-26 1999-10-13 清华大学 Process for preparing iron ore antifloating inhibitor
CN1356178A (en) * 2001-01-11 2002-07-03 徐井春 Reverse floatation depressant of iron ore and its preparing process
CN102443071A (en) * 2011-11-16 2012-05-09 广西大学 Composite modified starch as hematite reverse flotation inhibitor and preparation method thereof
CN103567078A (en) * 2013-11-13 2014-02-12 鞍钢集团矿业公司 Carboxymethyl starch inhibitor for reverse flotation of hematite
CN104190549A (en) * 2014-09-03 2014-12-10 鞍钢集团矿业公司 Composite inhibitor for reverse flotation of hematite
CN104437889A (en) * 2014-12-09 2015-03-25 鞍钢集团矿业公司 Hematite anti-floatation depressor

Non-Patent Citations (2)

* Cited by examiner, † Cited by third party
Title
张可喜、汪志芬: "《淀粉的改性及其应用》", 30 June 2008, 南海出版公司 *
张泾生、阙煊兰: "《矿用药剂》", 30 November 2008, 冶金工业出版社 *

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107961902A (en) * 2017-11-22 2018-04-27 北京矿冶研究总院 Composite inhibitor for inhibiting gangue contained in copper minerals and use method and application thereof
CN107961902B (en) * 2017-11-22 2019-10-18 北京矿冶研究总院 Composite inhibitor for inhibiting gangue contained in copper minerals and use method and application thereof
CN108620240A (en) * 2018-05-22 2018-10-09 中南大学 A kind of sulfide mineral inhibitor of bismuth and its application
CN108787176A (en) * 2018-05-22 2018-11-13 中南大学 A kind of application of the based compound containing peroxide
CN108620240B (en) * 2018-05-22 2019-10-08 中南大学 A kind of sulfide mineral inhibitor of bismuth and its application
CN112774869A (en) * 2020-12-25 2021-05-11 厦门紫金矿冶技术有限公司 Pyrite inhibitor, preparation thereof and application thereof in copper-lead-zinc multi-metal sulfide ores
CN114011581A (en) * 2021-11-09 2022-02-08 昆明理工大学 Preparation method and application of inhibitor for copper-sulfur separation under weak acidic condition
CN114011582A (en) * 2021-11-09 2022-02-08 昆明理工大学 Flotation method for improving beneficiation index of gold-bearing copper sulfide ore

Also Published As

Publication number Publication date
CN106824550B (en) 2018-12-04

Similar Documents

Publication Publication Date Title
CN106824550B (en) A kind of iron mineral inhibitor and preparation method thereof
CN109530094B (en) Amido hydroxy carboxylic acid/hydroximic acid compound and application thereof in mineral flotation
CN109499773B (en) Use of amido polycarboxylic acids/hydroximic acids in mineral flotation
CN104117432B (en) Magnetic kind method for floating
CN110142143B (en) Collecting system prepared from W/O/W multiphase emulsion and preparation method and application thereof
CN103301953B (en) 6-aryl amido hexyl hydroximic acid collecting agent and preparation and application methods thereof
CN105107636A (en) Organic lead inhibitor and application thereof
WO2022160493A1 (en) Recovery method and use of crude ferro-nickel alloy
CN105251622A (en) Beneficiation inhibitor used in lepidolite flotation process
CN105772226A (en) Flotation activating agent for fine-grain cassiterite and preparing method of flotation activating agent
CN105170309A (en) Lead and zinc separation method for polymetal gold-bearing ores
CN109954590A (en) A method of the flotation recovery gold from low-grade gold
CN103447155B (en) Ore dressing method for blue chalcocite and pyrite and collecting agent used in ore dressing method
CN111330740B (en) Method for improving flotation separation efficiency of magnesium-containing layered silicate minerals and copper sulfide minerals
CN108499743B (en) Combined inhibitor for inhibiting pumice stone minerals and using method thereof
CN104001627A (en) Inhibiting agent capable of selectively inhibiting calcium-containing gangue minerals in scheelite ores
CN110013916B (en) Preparation method and application method of bismuth-lead sulfide ore flotation inhibitor
CN107983539A (en) Application of the hydrolysis of polymaleic anhydride in Scheelite Flotation
CN103041925A (en) Application method of combined reagent in copper and sulphur separation of ore beneficiation of covellite predominantly copper sulfide ore
CN101091935A (en) Combined capturing and collecting agent
CN101003029A (en) Method for floating inhibited iron sulfide minerals
CN109772592A (en) 2- hydroxyl arone oxime compound as collecting agent in oxide ore flotation application and method for floating
CN114904659B (en) Cascade strengthening inhibition method for talcum and molybdenite flotation separation combined inhibitor
CN104805285B (en) Method for leaching gold by virtue of thiosulfate utilizing ammonium alcohol polyvinyl phosphate as additive
CN102976410B (en) Comprehensive utilization method of gypsum containing tungsten and fluorine

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
TA01 Transfer of patent application right
TA01 Transfer of patent application right

Effective date of registration: 20181018

Address after: 300350 -1, building 25, Tianjin city Jinnan District Industrial Park.

Applicant after: TIANJIN TIANBAO XIANG TECHNOLOGY Co.,Ltd.

Applicant after: ANSHAN TIANXIANG INDUSTRIAL TECHNOLOGY Co.,Ltd.

Applicant after: LIAONING BAO XIANG TECHNOLOGY Co.,Ltd.

Address before: 116000 1-24-1, Zhongshan Road, Shahekou District, Dalian, Liaoning, 478

Applicant before: LIAONING BAO XIANG TECHNOLOGY Co.,Ltd.

GR01 Patent grant
GR01 Patent grant
TR01 Transfer of patent right

Effective date of registration: 20230414

Address after: 300350 -1, building 25, Tianjin city Jinnan District Industrial Park.

Patentee after: TIANJIN TIANBAO XIANG TECHNOLOGY Co.,Ltd.

Address before: 300350 -1, building 25, Tianjin city Jinnan District Industrial Park.

Patentee before: TIANJIN TIANBAO XIANG TECHNOLOGY Co.,Ltd.

Patentee before: ANSHAN TIANXIANG INDUSTRIAL TECHNOLOGY Co.,Ltd.

Patentee before: LIAONING BAO XIANG TECHNOLOGY Co.,Ltd.

TR01 Transfer of patent right
TR01 Transfer of patent right
TR01 Transfer of patent right

Effective date of registration: 20231101

Address after: No.7 Lingshan Hongqi Road, Lishan District, Anshan City, Liaoning Province, 114032

Patentee after: Anshan Jinxiang Industrial Co.,Ltd.

Address before: 300350 -1, building 25, Tianjin city Jinnan District Industrial Park.

Patentee before: TIANJIN TIANBAO XIANG TECHNOLOGY Co.,Ltd.

AV01 Patent right actively abandoned

Granted publication date: 20181204

Effective date of abandoning: 20240511

AV01 Patent right actively abandoned

Granted publication date: 20181204

Effective date of abandoning: 20240511