CN106824550B - A kind of iron mineral inhibitor and preparation method thereof - Google Patents

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

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Publication number
CN106824550B
CN106824550B CN201710177011.0A CN201710177011A CN106824550B CN 106824550 B CN106824550 B CN 106824550B CN 201710177011 A CN201710177011 A CN 201710177011A CN 106824550 B CN106824550 B CN 106824550B
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parts
weight
sodium
mixture
conditions
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CN201710177011.0A
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CN106824550A (en
Inventor
梅建庭
杨威
曹翠
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Anshan Jinxiang Industrial Co ltd
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Anshan Tianxiang Industrial Technology Co Ltd
Liaoning Bao Xiang Technology Co Ltd
Tianjin Tianbao Xiang Technology Co Ltd
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    • 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

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

Abstract

The invention discloses a kind of production methods of iron mineral inhibitor: the first step reacts 1~4h by following parts by weight of component mixture at 60 DEG C~90 DEG C and obtains auxiliary agent (1): cornstarch, tapioca or 100 parts of wheaten starch, sodium ethoxide or 0.5~4.0 part of sodium hydroxide, 5~15 parts of sodium chloroacetate, second step reacts 3~6h by following parts by weight of component mixture at 50 DEG C~80 DEG C and obtains auxiliary agent (2): (1) 100 part of auxiliary agent obtained by the above-mentioned first step, 5~15 parts of ethylene oxide, sodium carbonate or 0.2~1.0 part of sodium acetate, third step is reacted 1~3h by following parts by weight of component mixture at 30 DEG C~60 DEG C to be inhibited agent finished product: (2) 100 parts of auxiliary agent obtained by above-mentioned second step, sodium metaperiodate or 1~12 part of hydrogen peroxide, sulphur It is sour ferrous or 0.2~1.0 part of 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 technique
The inhibitor that floatation of iron mineral uses mainly has two class of micromolecular inhibitor and macromolecular inhibitor.Little molecules in inhibiting Agent has waterglass, calgon, tartaric acid etc.;Macromolecular inhibitor has starch, carboxymethyl cellulose, sodium humate, dextrin With polyacrylamide etc..Most widely used in these inhibitor is cornstarch, when inhibiting iron mineral using cornstarch, often The deficiencies of high there are tailing.The reason is that cornstarch is weaker to the ability to function of fine grained iron mineral, cause fine grained iron ore Object is easily accessible in tailing, causes Iron Grade of Tailings high, iron recovery is low.
Summary of the invention
The object of the present invention is to provide a kind of production method of iron mineral inhibitor, this inhibitor collection carboxyl, ethyoxyl With aldehyde radical in one, the group with the effect of fine grained iron mineral is increased, increases the length with particulate iron mineral effect group, Fine grained iron mineral can be inhibited in concentrate.It is weak to fine grained iron mineral ability to function to solve former cornstarch inhibitor, 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 what is realized by following technical proposals:
The present invention provides a kind of production method of iron mineral inhibitor, includes the following 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 to be obtained efficiently for 1~4 hour Auxiliary agent 1:
100 parts of starch
Sodium ethoxide or 0.5~4.0 part of 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 to be obtained efficiently for 3~6 hours Auxiliary agent 2:
1 100 parts of high effective additives obtained by the above-mentioned first step
5~15 parts of ethylene oxide
Sodium carbonate or 0.2~1.0 part of sodium acetate catalyst
Third step is reacted 1~3 hour under the conditions of 30 DEG C~60 DEG C by the mixture of following parts by weight of component to be inhibited Agent finished product:
2 100 parts of high effective additives obtained by above-mentioned second step
Sodium metaperiodate or 1~12 part of hydrogen peroxide
Ferrous sulfate or 0.2~1.0 part of bluestone catalyst
The starch is cornstarch, tapioca, wheaten starch.
Select the inhibitor of the available different performance of different production methods.
Further, in the above-mentioned technical solutions, a kind of production method of iron mineral inhibitor, it is preferable that including following steps It is rapid:
The first step is reacted 2 hours under the conditions of 82 DEG C~85 DEG C by the mixture of following parts by weight of component obtains high effective additives 1:
100 parts of cornstarch
0.6~1.0 part of ethyl alcohol 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 to be obtained efficiently for 4~5 hours Auxiliary agent 2:
1 100 parts of high effective additives obtained by the above-mentioned first step
7~8 parts of ethylene oxide
0.4~0.8 part of sodium acetate catalyst
Third step is reacted 2~3 hours under the conditions of 52 DEG C~55 DEG C by the mixture of following parts by weight of component to be inhibited Agent finished product:
2 100 parts of 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 production method of iron mineral inhibitor, it is preferable that including following steps It is rapid:
The first step is reacted 2 hours under the conditions of 82 DEG C~85 DEG C by the mixture of following parts by weight of component obtains high effective additives 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 to be obtained efficiently for 4~5 hours Auxiliary agent 2:
1 100 parts of high effective additives obtained by the above-mentioned first step
7~8 parts of ethylene oxide
0.4~0.8 part of sodium carbonate catalyst
Third step is reacted 2~3 hours under the conditions of 52 DEG C~55 DEG C by the mixture of following parts by weight of component to be inhibited Agent finished product:
2 100 parts of 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 production method of iron mineral inhibitor, it is preferable that including following steps It is rapid:
The first step is reacted 2 hours under the conditions of 82 DEG C~85 DEG C by the mixture of following parts by weight of component obtains high effective additives 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 to be obtained efficiently for 4~5 hours Auxiliary agent 2:
1 100 parts of high effective additives obtained by the above-mentioned first step
7~8 parts of ethylene oxide
0.4~0.8 part of sodium carbonate catalyst
Third step is reacted 2~3 hours under the conditions of 53 DEG C~55 DEG C by the mixture of following parts by weight of component to be inhibited Agent finished product:
2 100 parts of 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 a kind of iron mineral inhibitor that above-mentioned production method obtains.
Invention beneficial effect
The present invention forms carboxyl, ethyoxyl and the suppression of the iron mineral of carbonyl functional group by three-step reaction on starch molecule Preparation, this inhibitor are a kind of wide grade polymeric inhibitors of iron mineral.It is strengthened by groups such as hydroxyl, ether and carbonyls With the useful effect of iron mineral, the selectivity with iron mineral effect is improved.It especially significantly increases and inhibits fine grained iron ore The ability to function of stone expands the range for inhibiting iron ore partial size, considerably reduces flotation tailing, realizes " mentioning iron drop tail " Purpose.
Specific embodiment
Following non-limiting embodiments can with a person of ordinary skill in the art will more fully understand the present invention, but not with Any mode limits the present invention.
Embodiment 1
The first step is reacted 2 hours under the conditions of 82 DEG C~85 DEG C by the mixture of following parts by weight of component obtains high effective additives 1:
100 parts of cornstarch
0.8 part of ethyl alcohol 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 to be obtained efficiently for 4~5 hours Auxiliary agent 2:
1 100 parts of high effective additives obtained by the above-mentioned first step
8 parts of ethylene oxide
0.6 part of sodium acetate catalyst
Third step is reacted 2~3 hours under the conditions of 52 DEG C~55 DEG C by the mixture of following parts by weight of component to be inhibited Agent finished product:
2 100 parts of 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, floatation of iron ore temperature reduces by 13 DEG C, Iron concentrate grade improves 0.2%, and Iron Grade of Tailings reduces by 2.4%, and unit consumption of medicine improves 20%.
Embodiment 2
The first step is reacted 2 hours under the conditions of 82 DEG C~85 DEG C by the mixture of following parts by weight of component obtains high effective additives 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 to be obtained efficiently for 4~5 hours Auxiliary agent 2:
1 100 parts of high effective additives obtained by the above-mentioned first step
8 parts of ethylene oxide
0.6 part of sodium carbonate catalyst
Third step is reacted 2~3 hours under the conditions of 52 DEG C~55 DEG C by the mixture of following parts by weight of component to be inhibited Agent finished product:
2 100 parts of 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, floatation of iron ore temperature reduces by 15 DEG C, Iron concentrate grade reduces by 0.15%, and Iron Grade of Tailings reduces by 1.73, and unit consumption of medicine improves 10%.
Embodiment 3
The first step is reacted 2 hours under the conditions of 82 DEG C~85 DEG C by the mixture of following parts by weight of component obtains high effective additives 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 to be obtained efficiently for 4~5 hours Auxiliary agent 2:
1 100 parts of high effective additives obtained by the above-mentioned first step
8 parts of ethylene oxide
0.8 part of sodium carbonate catalyst
Third step is reacted 2~3 hours under the conditions of 53 DEG C~55 DEG C by the mixture of following parts by weight of component to be inhibited Agent finished product:
2 100 parts of 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, floatation of iron ore temperature reduces by 14 DEG C, Iron concentrate grade reduces by 0.08%, and Iron Grade of Tailings reduces by 1.54, and unit consumption of medicine improves 12%.
Embodiment 4
The first step is reacted 2 hours under the conditions of 80 DEG C~82 DEG C by the mixture of following parts by weight of component obtains high effective additives 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 to be obtained efficiently for 4~5 hours Auxiliary agent 2:
1 100 parts of high effective additives obtained by the above-mentioned first step
8 parts of ethylene oxide
0.7 part of sodium carbonate catalyst
Third step is reacted 2~3 hours under the conditions of 53 DEG C~55 DEG C by the mixture of following parts by weight of component to be inhibited Agent finished product:
2 100 parts of 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, floatation of iron ore temperature reduces by 13 DEG C, Iron concentrate grade improves 0.02%, and Iron Grade of Tailings reduces by 2.04%, and unit consumption of medicine improves 12%.
Embodiment 5
The first step is reacted 2 hours under the conditions of 82 DEG C~84 DEG C by the mixture of following parts by weight of component obtains high effective additives 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 to be obtained efficiently for 4~5 hours Auxiliary agent 2:
1 100 parts of high effective additives obtained by the above-mentioned first step
8 parts of ethylene oxide
0.3 part of sodium carbonate catalyst
Third step is reacted 2~3 hours under the conditions of 53 DEG C~55 DEG C by the mixture of following parts by weight of component to be inhibited Agent finished product:
2 100 parts of 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, floatation of iron ore temperature reduces by 15 DEG C, Iron concentrate grade draft 0.05%, Iron Grade of Tailings reduce by 2.43%, and unit consumption of medicine improves 11%.

Claims (5)

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

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
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
CN108620240B (en) * 2018-05-22 2019-10-08 中南大学 A kind of sulfide mineral inhibitor of bismuth and its application
CN108787176B (en) * 2018-05-22 2019-11-08 中南大学 A kind of application of the based compound containing peroxide
CN112774869B (en) * 2020-12-25 2022-09-16 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
CN114011582B (en) * 2021-11-09 2022-08-16 昆明理工大学 Flotation method for improving beneficiation index of gold-bearing copper sulfide ore
CN114011581B (en) * 2021-11-09 2023-03-24 昆明理工大学 Preparation method and application of inhibitor for copper-sulfur separation under weak acidic condition

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1081091C (en) * 1999-03-26 2002-03-20 清华大学 Process for preparing iron ore antifloating inhibitor
CN1141184C (en) * 2001-01-11 2004-03-10 徐井春 Reverse floatation depressant of iron ore and its preparing process
CN102443071B (en) * 2011-11-16 2015-10-14 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

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