CN105750099B - A kind of method of high shear oil aggregation sorting fine coal slime - Google Patents

A kind of method of high shear oil aggregation sorting fine coal slime Download PDF

Info

Publication number
CN105750099B
CN105750099B CN201610107574.8A CN201610107574A CN105750099B CN 105750099 B CN105750099 B CN 105750099B CN 201610107574 A CN201610107574 A CN 201610107574A CN 105750099 B CN105750099 B CN 105750099B
Authority
CN
China
Prior art keywords
high shear
coal
ore pulp
coal slime
motor
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
CN201610107574.8A
Other languages
Chinese (zh)
Other versions
CN105750099A (en
Inventor
沙杰
王梦蝶
邵怀志
雷贺宁
白雪
谢广元
彭耀丽
夏文成
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 CN201610107574.8A priority Critical patent/CN105750099B/en
Publication of CN105750099A publication Critical patent/CN105750099A/en
Application granted granted Critical
Publication of CN105750099B publication Critical patent/CN105750099B/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B04CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
    • B04CAPPARATUS USING FREE VORTEX FLOW, e.g. CYCLONES
    • B04C9/00Combinations with other devices, e.g. fans, expansion chambers, diffusors, water locks
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J19/00Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J19/18Stationary reactors having moving elements inside

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Separation Of Solids By Using Liquids Or Pneumatic Power (AREA)
  • Processing Of Solid Wastes (AREA)
  • Solid Fuels And Fuel-Associated Substances (AREA)

Abstract

The present invention discloses a kind of method of high shear oil aggregation sorting fine coal slime, and a. coal slimes enter in ore pulp preprocessor with the ore pulp that water is formed sizes mixing;B. sizing mixing while toward adding non-polar hydrocarbon oil in ore pulp preprocessor;C. the slurry ore deposit after mineralising is sized mixing enters in high shear reaction kettle through Pulp pump to be handled;D. the coal slime for completing high shear oil aggregation process enters hydroclone classification;E. fine grain not agglomerating tail coal enters cyclone overflow port, and pockets of cleaned coal enters cyclone underflow opening.Beneficial effect is:First using the high speed shear selectively fine beans of reunion, form the cleaned coal floc sedimentation that granularity is big, intensity is higher, then cleaned coal floc sedimentation is separated with fine spoil particle using the method for cyclone classification again, sorting process can sort high grey thin mud content big coal slime while simplification, achieve the purpose that aid for Micro-fine Coal Slurry Dewatering efficient separation.

Description

A kind of method of high shear oil aggregation sorting fine coal slime
Technical field
The present invention relates to a kind of method for separating, and in particular to a kind of method of high shear oil aggregation sorting fine coal slime.
Background technology
As the raising of mining mechanization degree, mining depth are deepened, coal resources geological conditions runs down, particulate Ratio shared in raw coal sharply increases with ultra-fine coal slurry, and the trend that high grey difficulty selects superfine coal slurry content increase is presented. Coal is as a kind of non-renewable resources, and with the continuous reduction of coal reserves, the high-efficiency cleaning of coal slime resource, which utilizes, has weight Researching value and realistic meaning are wanted, and realizes coal resources efficient separation, the emphasis utilized and difficult point at present.
At present, flotation is that graded shot fine coal is most ripe, effective method, and is widely used in industrial production.Flotation Journey, acts in ore pulp Chinese medicine and mineral surfaces first, increases the surface property differences of hydrophobic coal grain and hydrophily ore particle, Then by the floating of bubble, carry surface hydrophobic coal slime and float and enters froth bed, ultimately form cleaned coal, and hydrophilic ore particle Stay in ore pulp, finally discharged with tailing, become tail coal.
However, when high ash thin mud content is big in coal slime, high ash thin mud passes through moisture mechanical entrapment, coal grain surface the cover etc. Process influences flotation, the loss of pollution and low ash extract coal of the high grey thin mud to floatation clean coal easily occurs so that flotation is difficult to Reach comparatively ideal sorting to descend, cause floatation clean coal ash content to meet product quality requirement, and lose the flammable body of cleaned coal The rate of recovery.
Therefore, for the big coal slime of high grey thin mud content, it is necessary to take significantly more efficient method for separating, more managed with obtaining The separating effect thought, to meet the economic needs of enterprise, and the strategic demand that non-renewable resources maximally utilize.
The content of the invention
In view of the above-mentioned problems of the prior art, the present invention provides a kind of side of high shear oil aggregation sorting fine coal slime Method, can sort the big coal slime of high grey thin mud content.
To achieve these goals, the technical solution adopted by the present invention is:A kind of high shear oil aggregation sorts fine coal slime Method, including ore pulp preprocessor, Pulp pump, high shear reaction kettle and hydrocyclone, bottom, the side of ore pulp preprocessor Face offers feeding mouth, discharge port respectively, and the top of ore pulp preprocessor is equipped with the first motor, the discharge port of ore pulp preprocessor Connected with the feed inlet of Pulp pump, the discharge port of Pulp pump is connected by the feed inlet of reaction kettle pan feeding valve and high shear reaction kettle Logical, the top of high shear reaction kettle is equipped with the second motor, and the discharge port of high shear reaction kettle passes through cyclone pan feeding valve and water The feed inlet connection of power cyclone, top, the bottom of hydrocyclone open up cyclone overflow port, cyclone underflow opening respectively;
A. coal slime enters in ore pulp preprocessor with the ore pulp that water is formed and sizes mixing;
B. sizing mixing while toward adding non-polar hydrocarbon oil in ore pulp preprocessor;
C. the slurry ore deposit after mineralising is sized mixing enters in high shear reaction kettle through Pulp pump to be handled;
D. the coal slime for completing high shear oil aggregation process enters hydroclone classification;
E. fine grain not agglomerating tail coal enters cyclone overflow port, and pockets of cleaned coal enters cyclone underflow opening.
Compared with prior art, the present invention is first using the high speed shear selectively fine beans of reunion, and formation granularity is big, intensity Higher cleaned coal floc sedimentation, is then again separated cleaned coal floc sedimentation with fine spoil particle using the method for cyclone classification, sorting process High grey thin mud content big coal slime can be sorted while simplification, achievees the purpose that aid for Micro-fine Coal Slurry Dewatering efficient separation.
Brief description of the drawings
Fig. 1 is the structure diagram of the present invention;
In figure:1st, ore pulp preprocessor, 2, Low speed electric motor, 3, feeding mouth, 4, discharge port, 5, Pulp pump, 6, reaction kettle, 7th, high shear reaction kettle, 8, pot motor, 9, cyclone pan feeding valve, 10, hydrocyclone, 11, cyclone overflow, 12, Cyclone underflow opening.
Embodiment
The invention will be further described below in conjunction with the accompanying drawings.
As shown in Figure 1, this high shear oil aggregation sorting fine coal slime method, including ore pulp preprocessor 1, Pulp pump 5, High shear reaction kettle 7 and hydrocyclone 10, bottom, the side of ore pulp preprocessor 1 offer feeding mouth 3, discharge port respectively 4, the top of ore pulp preprocessor 1 is equipped with the first motor 2, and the first motor 2 is Low speed electric motor, the discharging of ore pulp preprocessor 1 Mouth 4 is connected with the feed inlet of Pulp pump 5, and the discharge port of Pulp pump 5 passes through reaction kettle pan feeding valve 6 and high shear reaction kettle 7 Feed inlet connects, and the top of high shear reaction kettle 7 is equipped with the second motor 8, and the second motor 8 is pot motor, and rotating speed is 1300rpm-1500rpm, the discharge port of high shear reaction kettle 7 pass through the charging of cyclone pan feeding valve 9 and hydrocyclone 10 Mouth connection, top, the bottom of hydrocyclone 10 open up cyclone overflow port 11, cyclone underflow opening 12 respectively;
A. the ore pulp that selected coal slime is formed with water initially enters sizes mixing in ore pulp preprocessor 1, and ore pulp preprocessor 1 pushes up Portion is provided with the first motor 2, and the first motor 2 is Low speed electric motor, drives rotor to slowly run;
B. toward addition non-polar hydrocarbon oil in ore pulp preprocessor 1 while the first motor 2 slowly runs and sizes mixing;
C. the slurry ore deposit after advance mineralising is sized mixing is discharged by discharge port 4, through Pulp pump 5 and reaction kettle pan feeding valve 6 Control, which enters in high shear reaction kettle 7, to be handled, and the top of high shear reaction kettle 7 is equipped with the second motor 8, in 8 rotating speed of the second motor For under the drive of 1300rpm-1500rpm, coal slime particle completes high shear oil aggregation process within the regular hour;
D. the coal slime for completing high shear oil aggregation process enters hydrocyclone by the control of cyclone pan feeding valve 9 10 classifications;
E. fine grain not agglomerating tail coal enters cyclone overflow port 11, and pockets of cleaned coal enters cyclone underflow opening 12, by the post-treatment procedures such as being further dehydrated, form final low ash extract coal.
High shear oil aggregation method is to sort another effective method of fine beans, and basic principle is according to coal surface With the hydrophobic difference of mineral surfaces, invigoration effect is sheared by the stirring of high speed, using the bridge linking effect of non-polar oil micro- Particulate, hydrophobic coal wrap up in into small granule, and hydrophilic gangue particle is dispersed in water, then by grading granule from water In separate, high shear oil aggregation process is not related to air bubble problem, it is possible to prevente effectively from mechanical caused by bubble hydration shell Entrainment problem, while high speed shear acts on, can be by thin mud the cover coal grain compulsory commutation, and cause hydrophobicity coal slime and non-polar oil Hydrophobic forces are continuously increased, the intensity and granularity for making granule constantly increase, and the present invention is first selectively reunited using high speed shear Fine beans, forms the cleaned coal floc sedimentation that granularity is big, intensity is higher, then again using cyclone classification method by cleaned coal floc sedimentation with it is micro- Thin spoil particle separation, achievees the purpose that aid for Micro-fine Coal Slurry Dewatering efficient separation.

Claims (4)

  1. A kind of 1. method of high shear oil aggregation sorting fine coal slime, it is characterised in that including ore pulp preprocessor(1), slurry Pump(5), high shear reaction kettle(7)And hydrocyclone(10), ore pulp preprocessor(1)Bottom, side offer respectively into Material mouth(3), discharge port(4), ore pulp preprocessor(1)Top be equipped with the first motor(2), ore pulp preprocessor(1)Discharging Mouthful(4)With Pulp pump(5)Feed inlet connection, Pulp pump(5)Discharge port pass through reaction kettle pan feeding valve(6)It is anti-with high shear Answer kettle(7)Feed inlet connection, high shear reaction kettle(7)Top be equipped with the second motor(8), high shear reaction kettle(7)Go out Material mouth passes through cyclone pan feeding valve(9)With hydrocyclone(10)Feed inlet connection, hydrocyclone(10)Top, bottom Portion opens up cyclone overflow port respectively(11), cyclone underflow opening(12);
    A. the ore pulp that coal slime is formed with water enters ore pulp preprocessor(1)In size mixing;
    B. sizing mixing while toward ore pulp preprocessor(1)Middle addition non-polar hydrocarbon oil;
    C. the slurry ore deposit after mineralising is sized mixing is through Pulp pump(5)Into high shear reaction kettle(7)Middle processing;
    D. the coal slime for completing high shear oil aggregation process enters hydrocyclone(10)Classification;
    E. fine grain not agglomerating tail coal enters cyclone overflow port(11), and pockets of cleaned coal enters cyclone underflow opening (12).
  2. 2. the method for a kind of high shear oil aggregation sorting fine coal slime according to claim 1, it is characterised in that described First motor(2)For Low speed electric motor.
  3. 3. the method for a kind of high shear oil aggregation sorting fine coal slime according to claim 1, it is characterised in that described Second motor(8)For pot motor.
  4. 4. the method for a kind of high shear oil aggregation sorting fine coal slime according to claim 3, it is characterised in that described Second motor(8)Rotating speed is 1300rpm-1500rpm.
CN201610107574.8A 2016-02-29 2016-02-29 A kind of method of high shear oil aggregation sorting fine coal slime Expired - Fee Related CN105750099B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201610107574.8A CN105750099B (en) 2016-02-29 2016-02-29 A kind of method of high shear oil aggregation sorting fine coal slime

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201610107574.8A CN105750099B (en) 2016-02-29 2016-02-29 A kind of method of high shear oil aggregation sorting fine coal slime

Publications (2)

Publication Number Publication Date
CN105750099A CN105750099A (en) 2016-07-13
CN105750099B true CN105750099B (en) 2018-04-13

Family

ID=56330314

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201610107574.8A Expired - Fee Related CN105750099B (en) 2016-02-29 2016-02-29 A kind of method of high shear oil aggregation sorting fine coal slime

Country Status (1)

Country Link
CN (1) CN105750099B (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN114768271A (en) * 2022-04-29 2022-07-22 义乌市新江工艺品有限公司 Pressure-reducing grape ball and production process thereof

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4248697A (en) * 1979-05-29 1981-02-03 Consolidation Coal Company Oil agglomeration process
CN2068016U (en) * 1990-02-23 1990-12-26 煤炭科学研究总院唐山分院 Double feed port water media cyclone group for coal washery
CA2172028A1 (en) * 1996-03-18 1997-09-19 Olev Trass Flotation of oil-agglomerated coal for ash and pyrite removal-simultaneous grinding and agglomeration
CN101543738A (en) * 2009-03-20 2009-09-30 中国矿业大学 Equipment and method for forcibly mixing size
CN102430481A (en) * 2011-10-19 2012-05-02 中国矿业大学 Sorting process for high-ash and difficult-separation coal slime
CN103962251A (en) * 2014-04-18 2014-08-06 松阳县中奇环境工程有限公司 Shearing emulsifying smashing device for processing materials containing ferrites

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4248697A (en) * 1979-05-29 1981-02-03 Consolidation Coal Company Oil agglomeration process
CN2068016U (en) * 1990-02-23 1990-12-26 煤炭科学研究总院唐山分院 Double feed port water media cyclone group for coal washery
CA2172028A1 (en) * 1996-03-18 1997-09-19 Olev Trass Flotation of oil-agglomerated coal for ash and pyrite removal-simultaneous grinding and agglomeration
CN101543738A (en) * 2009-03-20 2009-09-30 中国矿业大学 Equipment and method for forcibly mixing size
CN102430481A (en) * 2011-10-19 2012-05-02 中国矿业大学 Sorting process for high-ash and difficult-separation coal slime
CN103962251A (en) * 2014-04-18 2014-08-06 松阳县中奇环境工程有限公司 Shearing emulsifying smashing device for processing materials containing ferrites

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
微细粒矿物疏水聚团的研究现状及进展;陈军等;《矿物学报》;20140630;第34卷(第2期);第3.3.2、4.1.2、4.2、5节 *

Also Published As

Publication number Publication date
CN105750099A (en) 2016-07-13

Similar Documents

Publication Publication Date Title
CN102430481B (en) Sorting process for high-ash and difficult-separation coal slime
CN204338316U (en) The Mineral separation device of barite, fluorite, calcite mineral intergrowth
Jameson et al. Coarse chalcopyrite recovery in a universal froth flotation machine
CN103381389A (en) Production technology for improving secondary recovery rate of tailings
CN105689155A (en) Multi-product flotation column separation equipment and method
CN101507946B (en) Double tail-removing gravity-flotation combined sorting method and device
Jameson et al. Flotation of coarse coal particles in a fluidized bed: The effect of clusters
CN103480502B (en) Three-product cyclone microbubble floatation column screening installation and method
CN101757982A (en) Coal slime floating process
CN105057085B (en) A kind of eddy flow scans interference bed separation of coarse slime method
CN106861891B (en) A kind of method for separating of low-grade black and white tungsten ore
CN109967226B (en) Method for recycling fine clean coal
CN205926037U (en) Synthesize and optimize flotation equipment
CN105944825B (en) A kind of ore dressing and desiliconizing enrichment method of Fine Hematite Ore
CN106583023A (en) Beneficiation method for microgranular cassiterite
CN105642431B (en) Method for gravity separation of sulfur concentrate from sulfur-containing coal gangue
CN105750099B (en) A kind of method of high shear oil aggregation sorting fine coal slime
CN100563838C (en) Mine tailing reclaims sulphur iron separation ore-sorting system and method
CN205361696U (en) High shear oil is reunited and is selected separately device of fine coal slime
CN108714482A (en) Rhombohedral iron ore beneficiation technics
CN109013068A (en) A kind of upgrading drop general labourer's skill of copper mine
CN210700594U (en) High-efficient fine-grained oxidized coal slime system of selecting separately
CN116020664A (en) Device and method for grading and refloating flotation clean coal
Abols et al. Maximizing gravity recovery through the application of multiple gravity devices
CN206444722U (en) Fluorite lump ore particle ore deposit gravity treatment separator

Legal Events

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

Granted publication date: 20180413

Termination date: 20190228

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