CN103143432B - Efficient crushing and three-section type screening method of coking coal gravity middings - Google Patents

Efficient crushing and three-section type screening method of coking coal gravity middings Download PDF

Info

Publication number
CN103143432B
CN103143432B CN201310062702.8A CN201310062702A CN103143432B CN 103143432 B CN103143432 B CN 103143432B CN 201310062702 A CN201310062702 A CN 201310062702A CN 103143432 B CN103143432 B CN 103143432B
Authority
CN
China
Prior art keywords
coal
enters
medium
product
screen
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.)
Expired - Fee Related
Application number
CN201310062702.8A
Other languages
Chinese (zh)
Other versions
CN103143432A (en
Inventor
陶秀祥
屈进州
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.)
China University of Mining and Technology CUMT
Original Assignee
China University of Mining and Technology CUMT
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 China University of Mining and Technology CUMT filed Critical China University of Mining and Technology CUMT
Priority to CN201310062702.8A priority Critical patent/CN103143432B/en
Publication of CN103143432A publication Critical patent/CN103143432A/en
Application granted granted Critical
Publication of CN103143432B publication Critical patent/CN103143432B/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Landscapes

  • Separation Of Solids By Using Liquids Or Pneumatic Power (AREA)
  • Combined Means For Separation Of Solids (AREA)

Abstract

An efficient crushing and three-section type screening method of coking coal gravity middings belongs to coal crushing, dissociating and screening processes. Gravity middings in a coking coal preparation plant are taken as a raw material to be crushed through rolling to the fraction being below 6 mm or 3 mm; a desliming screen is used to deslime a material with the fraction being 1 mm, a material with the fraction being 6 to 1 mm or 3 to 1 mm enters into a three-product dense medium cyclone, and clean coal, middings and gangues are respectively obtained after two sections are subjected to medium drainage; the material with the fraction being 1 mm is mixed with tailings in a clean coal magnetic separator, fine coal slimes with the fraction being 0.25 mm are deslimed by a classifying cyclone; coarse coal slimes with the fractions being 1 to 0.25 mm enter into a teetered bed separator for screening, light products are dewatered by a sieve bend and a coal slime centrifuge to obtain coarse clean coal, and heavy products are dewatered by a screen bowl centrifuge to obtain tailings; the fine coal slimes with the fractions being 0.25 mm enter into a flotation machine for flotation, and foamed clean coal and the tailings are sequentially subjected to concentration and pressure filtration dewatering to obtain flotation clean coal and the tailing product; and after the gravity middings are crushed through rolling, the product returns to a mixing barrel. The method has the advantages that the graded screening is carried out on the preselected coal slimes with coarse fraction and fine fraction, and the equipment screening precision is improved.

Description

The efficiency crushing of coal and syllogic method for separating in a kind of coking coal gravity treatment
Technical field
The present invention relates to a kind of coal crushing sorting process that dissociates, relate in particular to efficiency crushing and the syllogic method for separating of coal in a kind of coking coal gravity treatment.
Background technology
Coal resources in China reserves are abundant, and coal is complete, but coking coal resource lacks relatively, account for 27.6%.Wherein rich coal, coking coal and three kinds of coking coals of lean coal account for respectively 3.75%, 6.71% and 4.17% of coal total resources.At present; become scarce resource as the indispensable coking coal of coking industry and rich coal resource; its exploitation and processing and utilization have been subject to the protection of national policy or energy strategy; due to many reasons; in existing coal for coking, the recovery process of coal is lower for the organic efficiency of scarce resource, needs rationally coal for coking sorting recovery process efficiently badly.
Summary of the invention
The object of the invention is to provide efficiency crushing and the syllogic method for separating of coal in a kind of coking coal gravity treatment, solve the low problem of the existing rare coal for coking rate of recovery.
The object of the present invention is achieved like this, by the following technical solutions: taking coal in Oversized Coking Coal Cleaning Plant gravity treatment as raw material, adopt the broken method of dissociating, select front desliming, thick middle three sections of sortings of fine fraction, carry out according to following steps:
(1) utilize tramp iron separator to remove in gravity treatment after the ironware foreign material in coal, enter rolling disintegrator 1, rolling disintegrator 1 material size <50mm, discharging-material size <6mm;
(2) utilize rolling disintegrator 1 centering coal to carry out fragmentation, the <6mm grade material after fragmentation enters desliming screen, and desliming screen need add Sprayer Circulation water, when quantity of circulating water is not enough, with clear water as a supplement;
(3) utilize desliming screen wet method that sieve aperture is 1mm to remove the coal slime of <1mm in pan feeding, 6 ~ 1mm grade oversize enters mixing tank;
(4) in mixing tank, 6 ~ 1mm grade desliming screen oversize and rolling disintegrator 2 return to broken material mix after, beat to three products heavy medium cyclone and carry out sorting with pump, three products heavy medium cyclone is two-part isodensity heavy medium cyclone, one section is carried out the sorting of the eddy flow field of force, and two sections to carry out strong eddy flow selected;
(5) mixture of the mixed material in mixing tank and qualified medium is under the rotational flow sorting effect of three products heavy medium cyclone, light product enters head coal sculpingscreen, intermediate product enters middle coal sculping screen, heavy product enters Coal Stone Separation, head coal sculpingscreen, middle coal sculping screen and Coal Stone Separation need add Sprayer Circulation water, when quantity of circulating water is not enough, with clear water as a supplement;
(6) one section of head coal sculpingscreen is deviate from dense medium, deviates from rare medium for two sections, and oversize becomes dense medium head coal product; Utilize cleaned coal magnetic separator to carry out magnetic separation to rare medium, magnetic concentrate and one section of dense medium of deviating from together enter qualified medium bucket;
(7) in, one section of coal sculping screen is deviate from dense medium, deviates from rare medium for two sections, and oversize enters rolling disintegrator 2; One section of dense medium of deviating from of middle coal sculping screen enters qualified medium bucket, and two sections of rare media of deviating from enter middle cash magnetic separator;
(8) one section of Coal Stone Separation is deviate from dense medium, deviates from rare medium for two sections, and oversize becomes spoil product; One section of dense medium of deviating from of Coal Stone Separation enters qualified medium bucket, two sections of rare media of deviating from of two sections of rare media of deviating from and middle coal sculping screen together enter middle cash magnetic separator, in utilization, cash magnetic separator carries out magnetic separation to rare medium, magnetic concentrate enters qualified medium bucket, the qualified medium of qualified medium bucket is beaten to three products heavy medium cyclone as separating medium with pump, regulates the Media density of qualified medium bucket by the method for adding medium or adding clear water;
(9), under the roller crushing effect of rolling disintegrator 2, middle coal sculping screen oversize is crushed into fritter, returns to mixing tank;
(10) after desliming screen screenings mixes in coal slime bucket with cleaned coal magnetic tailing, beat to classifying cyclone group and carry out classification with pump, the overflow of classifying cyclone group enters mixing cirtern, and underflow enters hindered bed separator; The granularity of described overflow is <0.25mm grade fine coal slurry; Described underflow granularity is 1 ~ 0.25mm grade coarse slime;
(11) under the sorting of hindered bed separator, light product enters cleaned coal sieve bend, and heavy product enters screen bowl centrifuge, and hindered bed separator needs recirculated water/clear water as top water, in the time of water shortage in circulating water pool, with clear water as a supplement;
(12) use cleaned coal sieve bend to carry out primary dewatering to the light product of hindered bed separator, oversize enters cleaned coal centrifuge, and screenings enters mixing cirtern;
(13) use cleaned coal centrifuge to carry out second dehydration to cleaned coal sieve bend oversize, its product is thick cleaned coal, and centrifugate enters mixing cirtern together with cleaned coal sieve bend screenings;
(14) use screen bowl centrifuge to dewater to the heavy product of hindered bed separator, its product is tail coal, and filtrate enters tail coal thickener;
(15) overflow of classifying cyclone group and clean coal pressur filter return to filtrate, cleaned coal sieve bend screenings and cleaned coal centrifuge centrifugate and in mixing cirtern, size mixing after pretreatment, enter flotation device sorting;
(16) under flotation device sorting, flotation device foam cleaned coal enters clean coal pressur filter, and tail coal enters tail coal thickener;
(17) use clean coal pressur filter to dewater to flotation device cleaned coal, after dehydration, product is floatation clean coal product, and filtrate is returned to mixing cirtern;
(18) in, cash magnetic tailing, flotation device tail coal and screen bowl centrifuge centrifugate together enter tail coal thickener, and thickener overflow enters circulating water pool, and underflow enters tail coal filter press;
(19) use tail coal filter press to dewater to tail coal thickener underflow, filter press product is tail coal product, and filtrate enters circulating water pool.
Beneficial effect: owing to having adopted such scheme, adopted twice fragmentation-slightly middle fine fraction to carry out respectively dense medium sorting, disturb bed sorting and three sections of sorting process methods of flotation to coal in rare coking coal gravity treatment, effectively realized " substep release, recovery step by step ".Coal in gravity treatment is crushed to <6mm grade, lump coal and mineral matter intergrowth are dissociated, 6 ~ 1mm grade raw coal adopts the three products heavy medium cyclone of technology maturation, and two-part isodensity heavy medium cyclone carries out sorting, has improved coarsely graded sharpness of separation; <1mm grade coal slime adopts after classifying cyclone component level, 1 ~ 0.25mm grade coarse slime adopts hindered bed separator sorting, <0.25mm grade fine coal slurry adopts flotation device sorting, in three products heavy medium cyclone, product of coal adopts rolling disintegrator to carry out second-time breakage, coal in coal and mineral matter intergrowth in coarse grain are further dissociated, greatly improved sharpness of separation and the rate of recovery of thick fine slime.
Advantage: in gravity treatment, coal is after fragmentation is dissociated, adopt dense medium sorting, disturb bed sorting and three sections of sorting process of flotation, thick, fine fraction coal slime classification and sorting that preliminary election is deviate from, improve the sharpness of separation of equipment, and reclaim as much as possible rare coking coal resources, increase economy, society and ecological benefits.
Brief description of the drawings
Fig. 1 is process chart of the invention process.
Detailed description of the invention
Embodiment 1: in Fig. 1, in rare coking coal gravity treatment, coal is by near tramp iron separator rubber belt conveyor head, remove ironware foreign material, enter rolling disintegrator 1, breakdown products enters the wet method desliming screen that sieve aperture is 1mm, after wet method desliming screen oversize mixes with rolling disintegrator 2 returns, beat to three products heavy medium cyclone with pump, light product enters head coal sculpingscreen, one section of dense medium of deviating from enters qualified medium bucket, two sections of rare media of deviating from enter cleaned coal magnetic separator, magnetic concentrate enters qualified medium bucket, mine tailing enters coal slime bucket, oversize is dense medium head coal product, the intermediate product of three products heavy medium cyclone enters middle coal sculping screen, one section of dense medium of deviating from enters qualified medium bucket, and two sections of rare media of deviating from enter middle cash magnetic separator, and magnetic concentrate enters qualified medium bucket, mine tailing enters tail coal thickener, and oversize enters rolling disintegrator 2, the heavy product of three products heavy medium cyclone enters Coal Stone Separation, one section of dense medium of deviating from enters qualified medium bucket, and two sections of rare media of deviating from enter middle cash magnetic separator, and magnetic concentrate enters qualified medium bucket, mine tailing enters tail coal thickener, and oversize is spoil product, after desliming screen screenings mixes with cleaned coal magnetic separator mine tailing in coal slime bucket, beat to classifying cyclone group with pump, overflow enters mixing cirtern, underflow enters hindered bed separator, the light product of hindered bed separator enters cleaned coal sieve bend, cleaned coal sieve bend oversize enters cleaned coal centrifuge, and cleaned coal centrifuge product is thick head coal product, and centrifugate and cleaned coal sieve bend screenings are mixed into mixing cirtern, the heavy product of hindered bed separator enters screen bowl centrifuge, and centrifuge product is tail coal product, and centrifugate enters tail coal thickener, the overflow of classifying cyclone group and clean coal pressur filter return to filtrate, cleaned coal sieve bend screenings and cleaned coal centrifuge centrifugate and are mixed into mixing cirtern, after the pretreatment of sizing mixing, enter flotation device, flotation device froth pulp enters clean coal pressur filter, filter press product is floatation clean coal product, and filtrate is returned to mixing cirtern, flotation device tail coal enters tail coal thickener, and the overflow of tail coal thickener enters circulating water pool, and tail coal thickener underflow enters tail coal filter press, and tail coal filter press filtrate enters circulating water pool, and tail coal filter press product is tail coal product.
In desliming and de-mediated process, need to add Sprayer Circulation water, hindered bed separator needs recirculated water/clear water as top water, in the time of water shortage in circulating water pool, with clear water as a supplement.Dense medium and magnetic concentrate that cleaned coal, middle coal and spoil are deviate from enter qualified medium bucket, cause when Media density changes, and can adjust by the method for adding medium or adding clear water.

Claims (1)

1. the efficiency crushing of coal and a syllogic method for separating in coking coal gravity treatment, is characterized in that, taking coal in Oversized Coking Coal Cleaning Plant gravity treatment as raw material, adopts the broken method of dissociating, select front desliming, thick middle three sections of sortings of fine fraction, carries out according to following steps:
(1) utilize tramp iron separator to remove in gravity treatment after the ironware foreign material in coal, enter rolling disintegrator 1, rolling disintegrator 1 material size <50mm, discharging-material size <6mm;
(2) utilize rolling disintegrator 1 centering coal to carry out fragmentation, the <6mm grade material after fragmentation enters desliming screen, and desliming screen need add Sprayer Circulation water, when quantity of circulating water is not enough, with clear water as a supplement;
(3) utilize desliming screen wet method that sieve aperture is 1mm to remove the coal slime of <1mm in pan feeding, 6 ~ 1mm grade oversize enters mixing tank;
(4) in mixing tank, 6 ~ 1mm grade desliming screen oversize and rolling disintegrator 2 return to broken material mix after, beat to three products heavy medium cyclone and carry out sorting with pump, three products heavy medium cyclone is two-part isodensity heavy medium cyclone, one section is carried out the sorting of the eddy flow field of force, and two sections to carry out strong eddy flow selected;
(5) mixture of the mixed material in mixing tank and qualified medium is under the rotational flow sorting effect of three products heavy medium cyclone, light product enters head coal sculpingscreen, intermediate product enters middle coal sculping screen, heavy product enters Coal Stone Separation, head coal sculpingscreen, middle coal sculping screen and Coal Stone Separation need add Sprayer Circulation water, when quantity of circulating water is not enough, with clear water as a supplement;
(6) one section of head coal sculpingscreen is deviate from dense medium, deviates from rare medium for two sections, and oversize becomes dense medium head coal product; Utilize cleaned coal magnetic separator to carry out magnetic separation to rare medium, magnetic concentrate and one section of dense medium of deviating from together enter qualified medium bucket;
(7) in, one section of coal sculping screen is deviate from dense medium, deviates from rare medium for two sections, and oversize enters rolling disintegrator 2; One section of dense medium of deviating from of middle coal sculping screen enters qualified medium bucket, and two sections of rare media of deviating from enter middle cash magnetic separator;
(8) one section of Coal Stone Separation is deviate from dense medium, deviates from rare medium for two sections, and oversize becomes spoil product; One section of dense medium of deviating from of Coal Stone Separation enters qualified medium bucket, two sections of rare media of deviating from of two sections of rare media of deviating from and middle coal sculping screen together enter middle cash magnetic separator, in utilization, cash magnetic separator carries out magnetic separation to rare medium, magnetic concentrate enters qualified medium bucket, the qualified medium of qualified medium bucket is beaten to three products heavy medium cyclone as separating medium with pump, regulates the Media density of qualified medium bucket by the method for adding medium or adding clear water;
(9), under the roller crushing effect of rolling disintegrator 2, middle coal sculping screen oversize is crushed into fritter, returns to mixing tank;
(10) after desliming screen screenings mixes in coal slime bucket with cleaned coal magnetic tailing, beat to classifying cyclone group and carry out classification with pump, the overflow of classifying cyclone group enters mixing cirtern, and underflow enters hindered bed separator; The granularity of described overflow is <0.25mm grade fine coal slurry; Described underflow granularity is 1 ~ 0.25mm grade coarse slime;
(11) under the sorting of hindered bed separator, light product enters cleaned coal sieve bend, and heavy product enters screen bowl centrifuge, and hindered bed separator needs recirculated water/clear water as top water, in the time of water shortage in circulating water pool, with clear water as a supplement;
(12) use cleaned coal sieve bend to carry out primary dewatering to the light product of hindered bed separator, oversize enters cleaned coal centrifuge, and screenings enters mixing cirtern;
(13) use cleaned coal centrifuge to carry out second dehydration to cleaned coal sieve bend oversize, its product is thick cleaned coal, and centrifugate enters mixing cirtern together with cleaned coal sieve bend screenings;
(14) use screen bowl centrifuge to dewater to the heavy product of hindered bed separator, its product is tail coal, and filtrate enters tail coal thickener;
(15) overflow of classifying cyclone group and clean coal pressur filter return to filtrate, cleaned coal sieve bend screenings and cleaned coal centrifuge centrifugate and in mixing cirtern, size mixing after pretreatment, enter flotation device sorting;
(16) under flotation device sorting, flotation device foam cleaned coal enters clean coal pressur filter, and tail coal enters tail coal thickener;
(17) use clean coal pressur filter to dewater to flotation device cleaned coal, after dehydration, product is floatation clean coal product, and filtrate is returned to mixing cirtern;
(18) in, cash magnetic tailing, flotation device tail coal and screen bowl centrifuge centrifugate together enter tail coal thickener, and thickener overflow enters circulating water pool, and underflow enters tail coal filter press;
(19) use tail coal filter press to dewater to tail coal thickener underflow, filter press product is tail coal product, and filtrate enters circulating water pool.
CN201310062702.8A 2013-02-28 2013-02-28 Efficient crushing and three-section type screening method of coking coal gravity middings Expired - Fee Related CN103143432B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201310062702.8A CN103143432B (en) 2013-02-28 2013-02-28 Efficient crushing and three-section type screening method of coking coal gravity middings

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201310062702.8A CN103143432B (en) 2013-02-28 2013-02-28 Efficient crushing and three-section type screening method of coking coal gravity middings

Publications (2)

Publication Number Publication Date
CN103143432A CN103143432A (en) 2013-06-12
CN103143432B true CN103143432B (en) 2014-07-16

Family

ID=48541906

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201310062702.8A Expired - Fee Related CN103143432B (en) 2013-02-28 2013-02-28 Efficient crushing and three-section type screening method of coking coal gravity middings

Country Status (1)

Country Link
CN (1) CN103143432B (en)

Families Citing this family (28)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103386355B (en) * 2013-07-23 2015-10-14 侯英 A kind of high pressure roller selective molecular attraction of middle coal and method for separating
CN103433121B (en) * 2013-08-29 2015-07-08 永城煤电控股集团有限公司 Dense-medium and low-density separation process
CN103623932B (en) * 2013-11-20 2016-01-20 辽宁科技大学 A kind of whole grinding of high pressure roller of middle coal and method for separating
CN103831164B (en) * 2014-02-24 2016-10-05 太原理工大学 In a kind of coking, coal heavily floats combined sorting technique
CN103962230B (en) * 2014-04-28 2016-06-29 辽宁科技大学 The method that the high pressure roller of a kind of gangue is pulverized and reclaimed coal
CN103934080B (en) * 2014-04-29 2016-01-20 神华集团有限责任公司 Direct liquefaction coal and preparation method thereof
CN104174481A (en) * 2014-08-27 2014-12-03 中国矿业大学(北京) Simplified shallow-slot dense medium coal separation method
CN105363549B (en) * 2014-11-19 2018-02-27 晋江市冠兴建材有限责任公司 A kind of good environment-friendly type cinder recovery and processing system of metal recovery effect
CN104525358A (en) * 2014-12-22 2015-04-22 纪玉华 Process of coarse coal slime back washing in pre-desliming dense medium cyclone sorting
CN104741211A (en) * 2015-03-02 2015-07-01 中国矿业大学 Grading size mixing and bulk flotation separation process
CN104722390B (en) * 2015-03-02 2019-01-04 中国矿业大学 Coal floats combined sorting technique again in a kind of coking
CN105080701B (en) * 2015-09-02 2017-11-03 中国矿业大学 One kind interference selected difficulty of bed roughing Slime dense medium cyclone selects separation of coarse slime method
CN105689109B (en) * 2016-01-27 2018-01-30 中国矿业大学 A kind of fine coal slurry medium solid cyclone separation of coarse slime method
CN105597915B (en) * 2016-03-11 2018-02-16 中煤科工集团唐山研究院有限公司 The wide dual Jie's whole coarse slime separating process of grade can be achieved in one kind
CN105797831B (en) * 2016-03-22 2018-03-09 中国矿业大学 Technique is selected in the dissociation of coal again in a kind of coking end
CN105728156B (en) * 2016-03-22 2018-02-02 中国矿业大学 A kind of preparation technology of super clean coal
CN105728155B (en) * 2016-03-22 2018-01-16 中国矿业大学 Technique is selected in the dissociation of coal again in a kind of coking
CN107008564B (en) * 2017-01-11 2019-04-30 北京中煤煤炭洗选技术有限公司 The method of the dense media rate of recovery is improved in a kind of coal preparation technique
CN108745622B (en) * 2018-05-28 2020-08-28 湖南兴辉洗选药剂科技开发有限公司 Long flame coal washing system and washing method
CN109092550A (en) * 2018-08-31 2018-12-28 陕西陕煤黄陵矿业有限公司 A kind of coarse-fine coal centrifugate recovery system and its recovery method
CN109718944B (en) 2019-03-08 2019-11-29 中国矿业大学 A kind of aqueous medium underground coal preparation technique
CN109967226B (en) * 2019-05-05 2021-03-19 山西鑫畅远选煤科技股份有限公司 Method for recycling fine clean coal
CN110523525A (en) * 2019-09-09 2019-12-03 安徽理工大学 In a kind of Oversized Coking Coal Cleaning Plant, cash magnetic separation tail coal mud flotation recovery technique
CN111298960B (en) * 2020-04-16 2022-01-28 平顶山天安煤业股份有限公司八矿选煤厂 Echelon reduction process for flotation tailing coal slime
CN112237984B (en) * 2020-09-27 2021-09-24 中国平煤神马能源化工集团有限责任公司天成实业分公司 Medium coal physical crushing dissociation re-washing process
CN113441275A (en) * 2021-07-02 2021-09-28 唐山国华科技国际工程有限公司 High-ash coking coal deep dissociation separation equipment and method
CN114950715B (en) * 2022-05-27 2024-01-23 徐州工程学院 Coarse and refined coal classification and crushing equipment system in main re-selection system of heavy medium cyclone
CN114950713B (en) * 2022-05-27 2023-07-18 徐州工程学院 Dense medium cyclone main recleaning coal preparation process capable of improving recovery rate of cleaned coal of difficult coal preparation

Family Cites Families (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CA1327342C (en) * 1987-11-30 1994-03-01 James Kelly Kindig Process for beneficiating particulate solids
CN102179288A (en) * 2010-12-21 2011-09-14 王万明 Coal-reselecting process for heavy media coal separation
CN102211054B (en) * 2011-05-30 2013-04-03 中国矿业大学 Process for sorting coarse coal slime by utilizing heavy medium liquid-solid fluidized bed
CN102861663B (en) * 2012-10-08 2013-10-30 中国矿业大学 Breaking grinding dissociation and re-flotation two-stage recovery process of coal in scarce coking

Also Published As

Publication number Publication date
CN103143432A (en) 2013-06-12

Similar Documents

Publication Publication Date Title
CN103143432B (en) Efficient crushing and three-section type screening method of coking coal gravity middings
CN102861663B (en) Breaking grinding dissociation and re-flotation two-stage recovery process of coal in scarce coking
CN103831164B (en) In a kind of coking, coal heavily floats combined sorting technique
CN102430481B (en) Sorting process for high-ash and difficult-separation coal slime
CN107008565A (en) A kind of thermal coal deep screening and dense medium separation technique
CN104815748B (en) The broken mill floatation process of two sections of coal in a kind of coking
CN101602029A (en) From raw coal and select the technology of cleaned coal in the locked middlings of coal
CN110560258B (en) Device and process for selecting ultra-clean coal by physical cyclone recovery jigging overflow coal slime
CN105772212B (en) A kind of moderate cohesive coal produces extraordinary white cement coal method
CN202129156U (en) Three-product autogenous medium cyclone for coarse coal slime separation
CN112371323A (en) Combined separation process of pressurized two-product and pressurized three-product cyclones
CN109201315B (en) Coal washing process capable of improving utilization rate
CN109701730B (en) Efficient coal washing process capable of improving utilization rate
CN108855579B (en) Coal dressing method by using aqueous medium cyclone
CN107008566A (en) A kind of steam coal separation technique
CN110385197A (en) A kind of the gravity separation system and technique of barite fluorite associated minerals
CN214021353U (en) Gravity-flotation combined separation system for refractory fluorite ores
CN102179290A (en) Method for recycling clean coal from high-ash coal slurry tailings
CN210449500U (en) Coal dressing and desliming system for coal slime reseparation
CN104722390B (en) Coal floats combined sorting technique again in a kind of coking
CN110052326B (en) System and method for purifying and recycling refined coal slime
CN109731674B (en) Power coal separation method
CN115646638A (en) Gasification slag fine separation process
CN108855586B (en) Combined unit for coal flotation
CN109331992A (en) A kind of raw coal wholegrain radial sector method for separating

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
C14 Grant of patent or utility model
GR01 Patent grant
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20140716

Termination date: 20170228

CF01 Termination of patent right due to non-payment of annual fee