CN109482354A - Novel combined collecting and foaming agent for sorting copper ores in alpine regions and application thereof - Google Patents
Novel combined collecting and foaming agent for sorting copper ores in alpine regions and application thereof Download PDFInfo
- Publication number
- CN109482354A CN109482354A CN201811369430.5A CN201811369430A CN109482354A CN 109482354 A CN109482354 A CN 109482354A CN 201811369430 A CN201811369430 A CN 201811369430A CN 109482354 A CN109482354 A CN 109482354A
- Authority
- CN
- China
- Prior art keywords
- copper
- frother
- collector
- added
- ester
- 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
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B03—SEPARATION 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
- B03D—FLOTATION; DIFFERENTIAL SEDIMENTATION
- B03D1/00—Flotation
- B03D1/001—Flotation agents
- B03D1/004—Organic compounds
- B03D1/012—Organic compounds containing sulfur
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B03—SEPARATION 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
- B03D—FLOTATION; DIFFERENTIAL SEDIMENTATION
- B03D2201/00—Specified effects produced by the flotation agents
- B03D2201/02—Collectors
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B03—SEPARATION 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
- B03D—FLOTATION; DIFFERENTIAL SEDIMENTATION
- B03D2201/00—Specified effects produced by the flotation agents
- B03D2201/04—Frothers
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B03—SEPARATION 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
- B03D—FLOTATION; DIFFERENTIAL SEDIMENTATION
- B03D2203/00—Specified materials treated by the flotation agents; specified applications
- B03D2203/02—Ores
Landscapes
- Manufacture And Refinement Of Metals (AREA)
Abstract
The invention discloses a novel combined collecting foaming agent for sorting copper ores in alpine regions and application thereof, and is characterized by comprising 2-5 parts of azothionitrile ester, 1-2 parts of ammonium butryate, 0.25-0.5 part of diesel oil, 0.5-0.75 part of ethanol and 1-2 parts of 43# cyanic ester, so that the problems that in the winter production process of copper mines in alpine regions, the outdoor temperature reaches below-20 to 30 ℃, and the currently used ester collecting agent is high in melting point and easy to crystallize, inconvenience is brought to production, and production indexes are affected are solved.
Description
Technical field
The present invention relates to Copper Ores collector and frother technical field is sorted, in particular to a kind of extremely frigid zones sort copper mine
The novel compositions collector and frother of stone and application.
Background technique
In extremely frigid zones, since winter temperature is lower (individual places reach subzero 20 DEG C, refer to medicament storage temperature),
This just gives the bargh produced in winter to bring larger impact: the ore and industrial water in workshop region, stockyard when 1, producing
Temperature is all lower, causes Copper Ores selecting factory's production process Chinese medicine mineralising bad, to affect index;2, common efficient
Select copper esters medicament to be easy to produce crystallization at low ambient temperatures, and it is most common select copper medicament ester -105, at 23 DEG C of room temperature or less
Just gradually crystal, to selecting factory's production to make troubles.Therefore needing to heat its medicament in advance in process of production could use, if plus
Heat is not thorough, and medicament mineralising is bad, not only dosing is increased, and has an effect on production target, finally reduces the warp of enterprise
Ji benefit.
Summary of the invention
The present invention provides novel compositions collector and frother and the application that a kind of extremely frigid zones sort Copper Ores, for mesh
The live winter Copper Ores collector and frother of preceding extremely frigid zones is easy crystallization, leads to the problem that production target is lower, provides one kind
It does not crystallize at low ambient temperatures, and the novel compositions collector and frother for selecting factory's production target can be improved.
To achieve the goals above, technical solution of the present invention is specific as follows:
A kind of extremely frigid zones sort the novel compositions collector and frother of Copper Ores, including 2~5 parts of ester of sulphur nitrogen nitrile, and butyl ammonium aerofloat 1~
2 parts, 0.25~0.5 part of diesel oil, 0.5~0.75 part of ethyl alcohol, 1~2 part of 43# Huang hydrocyanic ester.
The invention also discloses the applications that a kind of extremely frigid zones sort the novel compositions collector and frother of Copper Ores, including such as
Lower step:
It (1) is that -0.074mm accounts for 70%~85% by Copper Ores wet-milling to granularity, ore milling concentration 50~60%, the stone in grinding process
Ash, additional amount are 500g/t~3000g/t;
(2) flotation pulp mass percentage concentration being adjusted 30~40%, is added common collecting agent butyl xanthate, dosage is 10~
Then the novel compositions collector and frother that a kind of extremely frigid zones described in claim 1 sort Copper Ores is added in 40g/t, be added
Amount be 30~50g/t, by roughing, it is selected, scan, output copper concentrate and tailing.
The beneficial effects of the present invention are:
1, using alcohols and the lower melting-point physical property of petrochemicals, the molten of new ester combination collector and frother is reduced
Point eliminates conventional esters collector and frother and crystallizes the link that need to be heated, and increases dissolution dispersion degree of the medicament in ore pulp,
Reduce collecting agent consumption, improves mineral processing index, reduce costs;
2, the sulphur nitrogen nitrile ester in the present invention, butyl ammonium aerofloat, diesel oil and the combination of 43# Huang hydrocyanic ester play the work of efficiency complementation
With reinforcement adds low melting point ethyl alcohol as lytic agent, so that novel group provided by the invention to the selection collecting sexuality of copper
It is simple to close collector and frother composition, stability is good, simple process, production cost are low, have stronger selection collecting frothing capacity,
Environmental pollution is less, realizes valuable metal synthetical recovery.
Specific embodiment
Embodiment 1
Low temperature crystallization experiment
2 parts of ester of sulphur nitrogen nitrile, 1 part of butyl ammonium aerofloat, 0.25 part of diesel oil, 0.5 part of ethyl alcohol, 1 part of 43# Huang hydrocyanic ester is prepared through equipment and is completed
Later, 3 days are stood in subzero 30 degree of environment, takes out observation and does not find crystalline polamer.
Embodiment 2
Low temperature crystallization experiment
5 parts of ester of sulphur nitrogen nitrile, 2 parts of butyl ammonium aerofloat, 0.5 part of diesel oil, 0.75 part of ethyl alcohol, 2 parts of 43# Huang hydrocyanic ester is prepared through equipment and is completed
Later, 5 days are stood in subzero 30 degree of environment, takes out observation and does not find crystalline polamer.
Embodiment 3
Certain copper dressing plant of Subei, Gansu Province south:
More than three km of ground height above sea level, 4 DEG C of mine temperature on average, -35 DEG C of extreme temperature in winter, factory is selected to produce throughout the year.Copper raw ore
Grade is 0.62%, and before using pharmaceutical preparations, conventional esters collector and frother crystallization is more serious, is brought to selecting factory to produce
It is extreme inconvenient, not only high production cost, and have an effect on index.On the basis of this background and laboratory small-scale test, carry out for
Commerical test in phase 30 days.
The present invention 2 parts of sulphur nitrogen nitrile ester of selection, 1 part of butyl ammonium aerofloat, 0.25 part of diesel oil, 0.5 part of ethyl alcohol, 1 part of 43# Huang hydrocyanic ester.
It is that -0.074mm accounts for 70% by Copper Ores wet-milling to fineness, lime is added in grinding process, adds for ore milling concentration 50%
Entering amount is 500g/t, and flotation pulp mass percentage concentration is adjusted 30%, and common collecting agent butyl xanthate, dosage 10g/ is added
T, is then added novel collector and frother of the invention, additional amount 30g/t, by roughing, it is selected, scan, output copper concentrate
And tailing, obtain accumulative copper concentrate copper grade 22.88%, add up the mineral processing index of copper recovery 94.11%, compared with commerical test it
Before, butyl xanthate reduces 20g/t, and collector and frother reduces by 30 g/t, and mutually instantly, the rate of recovery improves 6.32 to copper concentrate copper grade
Percentage point, significant effect.
Embodiment 4
Certain copper dressing plant of Subei, Gansu Province south:
More than three km of ground height above sea level, 4 DEG C of mine temperature on average, -35 DEG C of extreme temperature in winter, factory is selected to produce throughout the year.Copper raw ore
Grade is 0.80%, and before using pharmaceutical preparations, conventional esters collector and frother crystallization is more serious, is brought to selecting factory to produce
It is extreme inconvenient, not only high production cost, and have an effect on index.On the basis of this background and laboratory small-scale test, carry out for
Commerical test in phase 30 days.
The present invention 2 parts of sulphur nitrogen nitrile ester of selection, 1 part of butyl ammonium aerofloat, 0.25 part of diesel oil, 0.5 part of ethyl alcohol, 1 part of 43# Huang hydrocyanic ester.
It is that 0.074mm accounts for 75% by Copper Ores wet-milling to-fineness, lime is added in grinding process, adds for ore milling concentration 55%
Entering amount is 1500g/t.Flotation pulp mass percentage concentration is adjusted 35%, and common collecting agent butyl xanthate, dosage 20g/ is added
T, is then added novel collector and frother of the invention, additional amount 40g/t, by roughing, it is selected, scan, output copper concentrate
And tailing.Accumulative copper concentrate copper grade 22.88% is obtained, the mineral processing index of copper recovery 94.11% is added up.Compared with commerical test it
Before, butyl xanthate reduces 20g/t, and collector and frother reduces by 30 g/t, and mutually instantly, the rate of recovery improves 6.32 to copper concentrate copper grade
Percentage point, significant effect.
Embodiment 5
In Altay, xinjiang copper dressing plant: 15 DEG C of mine temperature on average, -28 DEG C of winter Annual lowest climate temperature selects factory to give birth to throughout the year
It produces, has carried out commerical test in 30 days by a definite date.
The present invention 5 parts of sulphur nitrogen nitrile ester of selection, 2 parts of butyl ammonium aerofloat, 0.5 part of diesel oil, 0.75 part of ethyl alcohol, 2 parts of 43# Huang hydrocyanic ester.
It is that 0.074mm accounts for 80% by Copper Ores wet-milling to-fineness, lime is added in grinding process, adds for ore milling concentration 50%
Entering amount is 1000g/t.Flotation pulp mass percentage concentration is adjusted 35%, and common collecting agent butyl xanthate, dosage 25g/ is added
T, is then added novel collector and frother of the invention, additional amount 35g/t, by roughing, it is selected, scan, output copper concentrate
And tailing, obtain copper grade 20.88%, the mineral processing index of copper recovery 91.39%.Before commerical test, butyl xanthate is reduced
40g/t, collector and frother reduce by 40 g/t, and copper concentrate copper grade improves 2.19 percentage points, and the rate of recovery improves 4.51 hundred
Branch, effect are more obvious.
Embodiment 6
In Altay, xinjiang copper dressing plant: 15 DEG C of mine temperature on average, -28 DEG C of winter Annual lowest climate temperature selects factory to give birth to throughout the year
It produces, has carried out commerical test in 30 days by a definite date.
The present invention 5 parts of sulphur nitrogen nitrile ester of selection, 2 parts of butyl ammonium aerofloat, 0.5 part of diesel oil, 0.75 part of ethyl alcohol, 2 parts of 43# Huang hydrocyanic ester.
It is that -0.074mm accounts for 85% by Copper Ores wet-milling to fineness, lime is added in grinding process, adds for ore milling concentration 60%
Entering amount is 3000g/t.Flotation pulp mass percentage concentration is adjusted 40%, and common collecting agent butyl xanthate, dosage 40g/ is added
T, is then added novel collector and frother of the invention, additional amount 50g/t, by roughing, it is selected, scan, output copper concentrate
And tailing, obtain copper grade 20.88%, the mineral processing index of copper recovery 91.39%.Before commerical test, butyl xanthate is reduced
40g/t, collector and frother reduce by 40 g/t, and copper concentrate copper grade improves 2.19 percentage points, and the rate of recovery improves 4.51 hundred
Branch, effect are more obvious.
Embodiment 7
Linzhou, Xizang copper dressing plant: 3,500 meters of ground height above sea level or more, 11 DEG C of mine temperature on average, winter extreme gas
- 30 DEG C of temperature, selects factory to produce throughout the year.Before using pharmaceutical preparations, factory's routine esters collector and frother is selected to crystallize more serious, medicine
Agent consumption is big and production target is low.The problem of fundamentally to solve final election factory, has carried out laboratory test, then at the scene first
Carry out commerical test.
The present invention 3 parts of sulphur nitrogen nitrile ester of selection, 1.5 parts of butyl ammonium aerofloat, 0.3 part of diesel oil, 0.6 part of ethyl alcohol, 43# Huang hydrocyanic ester 1.5
Part.
1, this laboratory test time is winter, and outside air temperature subzero, test water is zero degree.Copper head grade
Between 0.95~1.02%, it is that -0.074mm accounts for 80% that this, which is selected factory's Copper Ores wet-milling to fineness, ore milling concentration 50%, in ore grinding
Lime, additional amount 2000g/t are added in the process.Flotation pulp mass percentage concentration is adjusted 35%, and common collecting agent fourth is added
Then base xanthate, dosage 40g/t are added novel collector and frother, additional amount 60g/t, by roughing, it is selected, scan, produce
Copper concentrate and tailings.Copper concentrate copper grade 20.43% is obtained, the mineral processing index of copper recovery 89.24% is added up.More conventional esters
Collector and frother butyl xanthate reduces 50g/t, and collector and frother reduces by 55 g/t, and copper concentrate copper grade is suitable, and copper recovery mentions
It is 5.11 percentage points high.
2, on the basis of laboratory small-scale test, commerical test in 30 days by a definite date is carried out.By Copper Ores wet-milling to fineness be-
0.074mm accounts for 80%, and lime, additional amount 2000g/t is added in ore milling concentration 50% in grinding process.Flotation pulp quality hundred
Divide concentration to adjust 35%, common collecting agent butyl xanthate is added, then dosage 50g/t is added novel collector and frother, adds
Enter amount be 70g/t, by roughing, it is selected, scan, output copper concentrate and tailing.Accumulative copper grade 19.448% is obtained, copper is added up
The mineral processing index of the rate of recovery 87.59%.Before commerical test, butyl xanthate reduces 40g/t, and collector and frother reduces by 42 g/t,
Mutually instantly, copper recovery improves 4.51 percentage points to copper concentrate copper grade, significant effect.
Embodiment 8
Linzhou, Xizang copper dressing plant: 3,500 meters of ground height above sea level or more, 11 DEG C of mine temperature on average, winter extreme gas
- 30 DEG C of temperature, selects factory to produce throughout the year.Before using pharmaceutical preparations, factory's routine esters collector and frother is selected to crystallize more serious, medicine
Agent consumption is big and production target is low.The problem of fundamentally to solve final election factory, has carried out laboratory test, then at the scene first
Carry out commerical test.
The present invention 3 parts of sulphur nitrogen nitrile ester of selection, 1.5 parts of butyl ammonium aerofloat, 0.3 part of diesel oil, 0.6 part of ethyl alcohol, 43# Huang hydrocyanic ester 1.5
Part.
1, this laboratory test time is winter, and outside air temperature subzero, test water is close to zero degree.Copper raw ore product
Position is between 0.95~1.02%, and it is that -0.074mm accounts for 85% that this, which is selected factory's Copper Ores wet-milling to fineness, and ore milling concentration 60% is being ground
Lime, additional amount 3000g/t are added during mine.Flotation pulp mass percentage concentration is adjusted 38%, and common collecting agent is added
Then butyl xanthate, dosage 60g/t are added novel collector and frother, additional amount 80g/t, by roughing, it is selected, scan,
Output copper concentrate and tailing.Copper concentrate copper grade 20.43% is obtained, the mineral processing index of copper recovery 89.24% is added up.More conventional ester
Class collector and frother butyl xanthate reduces 50g/t, and collector and frother reduces by 55 g/t, and copper concentrate copper grade is suitable, copper recovery
Improve 5.11 percentage points.
2, on the basis of laboratory small-scale test, commerical test in 30 days by a definite date is carried out.By Copper Ores wet-milling to fineness be-
0.074mm accounts for 85%, and lime, additional amount 3000g/t is added in ore milling concentration 60% in grinding process.Flotation pulp quality hundred
Divide concentration to adjust 38%, common collecting agent butyl xanthate is added, then dosage 70g/t is added novel collector and frother, adds
Enter amount be 900g/t, by roughing, it is selected, scan, output copper concentrate and tailing.Accumulative copper grade 19.448% is obtained, copper is added up
The mineral processing index of the rate of recovery 87.59%.Before commerical test, butyl xanthate reduces 40g/t, and collector and frother reduces by 42 g/t,
Mutually instantly, copper recovery improves 4.51 percentage points to copper concentrate copper grade, significant effect.
Claims (2)
1. the novel compositions collector and frother that a kind of extremely frigid zones sort Copper Ores, which is characterized in that including sulphur nitrogen nitrile ester 2~5
Part, 1~2 part of butyl ammonium aerofloat, 0.25~0.5 part of diesel oil, 0.5~0.75 part of ethyl alcohol, 1~2 part of 43# Huang hydrocyanic ester.
2. a kind of extremely frigid zones sort the application of the novel compositions collector and frother of Copper Ores according to claim 1, special
Sign is, includes the following steps:
It (1) is that -0.074mm accounts for 70%~85% by Copper Ores wet-milling to granularity, ore milling concentration 50~60%, the stone in grinding process
Ash, additional amount are 500g/t~3000g/t;
(2) flotation pulp mass percentage concentration being adjusted 30~40%, is added common collecting agent butyl xanthate, dosage is 10~
Then the novel compositions collector and frother that a kind of extremely frigid zones described in claim 1 sort Copper Ores is added in 40g/t, be added
Amount be 30~50g/t, by roughing, it is selected, scan, output copper concentrate and tailing.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201811369430.5A CN109482354B (en) | 2018-11-16 | 2018-11-16 | Novel combined collecting and foaming agent for sorting copper ores in alpine regions and application thereof |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201811369430.5A CN109482354B (en) | 2018-11-16 | 2018-11-16 | Novel combined collecting and foaming agent for sorting copper ores in alpine regions and application thereof |
Publications (2)
Publication Number | Publication Date |
---|---|
CN109482354A true CN109482354A (en) | 2019-03-19 |
CN109482354B CN109482354B (en) | 2021-02-26 |
Family
ID=65696209
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201811369430.5A Active CN109482354B (en) | 2018-11-16 | 2018-11-16 | Novel combined collecting and foaming agent for sorting copper ores in alpine regions and application thereof |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN109482354B (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN110038730A (en) * | 2019-05-20 | 2019-07-23 | 北京矿冶科技集团有限公司 | A kind of beneficiation method containing two types copper cobalt sulfide ore containing cobalt mineralss |
CN110947523A (en) * | 2019-11-22 | 2020-04-03 | 西北矿冶研究院 | Collecting agent for recovering copper, lead and zinc minerals from iron ore dressing tailings |
Citations (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0097505A1 (en) * | 1982-06-17 | 1984-01-04 | Sentrachem Limited | Flotation processes using depressants |
CN101172267A (en) * | 2007-12-03 | 2008-05-07 | 西部矿业股份有限公司 | Technique for improving complex vulcanizing copper mine ore floatation indicators |
CN101983777A (en) * | 2010-11-23 | 2011-03-09 | 昆明冶金研究院 | Alumyte flotation compound collecting agent |
CN101992151A (en) * | 2010-11-11 | 2011-03-30 | 西北矿冶研究院 | High-sulfur copper ore collecting agent |
CN102600986A (en) * | 2011-12-21 | 2012-07-25 | 西北矿冶研究院 | Efficient copper-nickel polymetallic sulphide ore beneficiation reagent |
CN104668102A (en) * | 2015-03-10 | 2015-06-03 | 云南磷化集团有限公司 | Obverse flotation collecting agent for low temperature-resistant collophanite and preparation method thereof |
CN104923409A (en) * | 2014-03-19 | 2015-09-23 | 荆春芳 | High efficient copper sulphide ore collector |
WO2017116542A1 (en) * | 2015-12-28 | 2017-07-06 | Chevron Phillips Chemical Company Lp | Mixed decyl mercaptans compositions and use thereof as mining chemical collectors |
WO2018045025A1 (en) * | 2016-08-31 | 2018-03-08 | Kemiraoyj | Cationic polymer selective depressants and use thereof in mineral ore purification methods |
-
2018
- 2018-11-16 CN CN201811369430.5A patent/CN109482354B/en active Active
Patent Citations (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0097505A1 (en) * | 1982-06-17 | 1984-01-04 | Sentrachem Limited | Flotation processes using depressants |
CN101172267A (en) * | 2007-12-03 | 2008-05-07 | 西部矿业股份有限公司 | Technique for improving complex vulcanizing copper mine ore floatation indicators |
CN101992151A (en) * | 2010-11-11 | 2011-03-30 | 西北矿冶研究院 | High-sulfur copper ore collecting agent |
CN101983777A (en) * | 2010-11-23 | 2011-03-09 | 昆明冶金研究院 | Alumyte flotation compound collecting agent |
CN102600986A (en) * | 2011-12-21 | 2012-07-25 | 西北矿冶研究院 | Efficient copper-nickel polymetallic sulphide ore beneficiation reagent |
CN104923409A (en) * | 2014-03-19 | 2015-09-23 | 荆春芳 | High efficient copper sulphide ore collector |
CN104668102A (en) * | 2015-03-10 | 2015-06-03 | 云南磷化集团有限公司 | Obverse flotation collecting agent for low temperature-resistant collophanite and preparation method thereof |
WO2017116542A1 (en) * | 2015-12-28 | 2017-07-06 | Chevron Phillips Chemical Company Lp | Mixed decyl mercaptans compositions and use thereof as mining chemical collectors |
WO2018045025A1 (en) * | 2016-08-31 | 2018-03-08 | Kemiraoyj | Cationic polymer selective depressants and use thereof in mineral ore purification methods |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN110038730A (en) * | 2019-05-20 | 2019-07-23 | 北京矿冶科技集团有限公司 | A kind of beneficiation method containing two types copper cobalt sulfide ore containing cobalt mineralss |
CN110947523A (en) * | 2019-11-22 | 2020-04-03 | 西北矿冶研究院 | Collecting agent for recovering copper, lead and zinc minerals from iron ore dressing tailings |
CN110947523B (en) * | 2019-11-22 | 2022-05-03 | 西北矿冶研究院 | Collecting agent for recovering copper, lead and zinc minerals from iron ore dressing tailings |
Also Published As
Publication number | Publication date |
---|---|
CN109482354B (en) | 2021-02-26 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN109482354A (en) | Novel combined collecting and foaming agent for sorting copper ores in alpine regions and application thereof | |
CN100429188C (en) | Special controlled release fertilizer for peanut, soybean and manufacturing method thereof | |
CN103910567A (en) | Special organic-inorganic compound fertilizer for paddy rice | |
CN106622636B (en) | A kind of ore-dressing technique of copper nickel sulfide mineral | |
CN101983776A (en) | Collophane low-temperature reverse flotation collector and preparation method thereof | |
CN101791591A (en) | Phosphorite low-temperature foam flotation collector and preparation method thereof | |
CN106278693A (en) | Solid Water soluble fertilizer prepared by a kind of hot melt and preparation method thereof | |
CN107382381B (en) | Production process of high-quality potassium magnesium sulfate fertilizer | |
CN105967212A (en) | Method for preparing potassium sulphate by using potassium salt in sintering machine head electric dust removal ash | |
CN102826890A (en) | Efficient polymorphous fertilizer special for vegetables and preparation method thereof | |
CN102674985A (en) | Novel agricultural compound fertilizer | |
CN102391021B (en) | Method for producing silicon-calcium-magnesium fertilizer by using ironmaking blast furnace water-quenching slag as raw materials | |
CN101927214B (en) | Technology for extracting potassium from potassium mixed salt containing picromerite, KCL and carnallite | |
CN102775219A (en) | Method for preparing nitrogen-phosphorus-potassium compound fertilizer from biotite | |
CN110668875A (en) | Production method of high-sulfur full-water-soluble nitro-sulfur-based nitrogen fertilizer granules | |
Yuan-xue et al. | Effects of phosphorus fertilization on leaf area index, biomass accumulation and allocation, and phosphorus use efficiency of intercropped maize. | |
CN106111346B (en) | A kind of phosphorite flotation collector and preparation method thereof for efficiently removing sesquichloride | |
CN104649787B (en) | A kind of special amino sour water soluble fertilizers of lemon and preparation method thereof | |
CN105777446A (en) | Compound fertilizer special for rice | |
CN111468305A (en) | Ilmenite flotation collector | |
CN104387156B (en) | A kind of improvement technique producing spheric granules nitrogen-phosphorus-potassium compound fertilizer based on Nitro Phosphate Unit | |
CN113000219A (en) | Ilmenite flotation collector | |
CN103910568B (en) | A kind of multinutrient speciality fertilizer for tobacco material and its preparation method and application | |
CN107899752B (en) | Preparation method and application of zinc oxide collector | |
CN104671916A (en) | Formula of effective and safe special bulk blending fertilizer for sugar beets |
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 |