CN101530824B - A coal dressing method and system of four-product jigging primary cleaning, secondary head coal small simplified heavy medium reelecting - Google Patents

A coal dressing method and system of four-product jigging primary cleaning, secondary head coal small simplified heavy medium reelecting Download PDF

Info

Publication number
CN101530824B
CN101530824B CN 200910131301 CN200910131301A CN101530824B CN 101530824 B CN101530824 B CN 101530824B CN 200910131301 CN200910131301 CN 200910131301 CN 200910131301 A CN200910131301 A CN 200910131301A CN 101530824 B CN101530824 B CN 101530824B
Authority
CN
China
Prior art keywords
coal
product
gained
jigging
cleaned
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.)
Active
Application number
CN 200910131301
Other languages
Chinese (zh)
Other versions
CN101530824A (en
Inventor
常建勇
李叶强
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.)
JINYITONG TECHNOLOGY (BEIJING) CO LTD
Original Assignee
JINYITONG TECHNOLOGY (BEIJING) CO LTD
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by JINYITONG TECHNOLOGY (BEIJING) CO LTD filed Critical JINYITONG TECHNOLOGY (BEIJING) CO LTD
Priority to CN 200910131301 priority Critical patent/CN101530824B/en
Publication of CN101530824A publication Critical patent/CN101530824A/en
Application granted granted Critical
Publication of CN101530824B publication Critical patent/CN101530824B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Images

Landscapes

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

Abstract

The invention discloses a coal dressing method and system of four-product jigging primary cleaning and secondary head coal small simplified heavy medium reelecting. The invention is a coal dressing method and system that selects the secondary head coal product through the four-product jigging technique and then reelects the secondary head coal with small simplify heavy medium separation technology. The adoption of the invention to select coal is characterized by less total investment, simpler system and lower operational expense, which can improve the stability of the system, reduce the powerconsumption, simplify the managing and maintaining work. The method can be easily realized with present technical merits, which is beneficial to be popularized in the middle and small coal washeries where the management level is low and if the method is used in oversize coal washeries, the cost for washing is lower.

Description

Coal preparation method and Recognition Applied in Coal Preparation System that a kind of four-product jigging main separation, inferior cleaned coal small simplified heavy medium select again
Affiliated technical field
The present invention relates to a kind of coal preparation method and technique, especially relate to coal preparation method and Recognition Applied in Coal Preparation System that a kind of four-product jigging main separation, inferior cleaned coal small simplified heavy medium are selected again.
Background technology
At present, both at home and abroad the most frequently used coal preparation method of coal preparation plant has two kinds of coal jigging method and heavy media coal separation methods, wherein: the coal jigging method has small investment, running expense is low, treating capacity is large, the advantages such as technique is simple, and equipment control is convenient, and weak point is to select above coal sharpness of separation low to difficulty; And the heavy media coal separation method has the pluses and minuses opposite with the coal jigging method.Facts have proved for many years, but the choosing of jigging commute and medium coal separation are applicable, it is applicable to difficulty choosing and utmost point difficult separation coal heavily to be situated between, and these two kinds of each have their own scope of applications of method do not have a kind of method can substitute another kind under any condition.In order to develop both advantages, overcome both deficiencies, in the past few years many experts and scholar have successively developed some jiggings and the combined coal-dressing method that heavily is situated between, contained two product jigging discharge refuses, (the middle coal+cleaned coal) of " mineral dressing " book 262-269 page or leaf of publishing such as publishing house of China Mining University in October, 2002 second impression heavily is situated between and washes, and three products jigging master washes, middle coal heavily is situated between the method such as washes again.From density and the relation with contents curve map (as shown in Figure 1) of a certain difficult separation coal, if by existing two product jigging discharge refuses, (middle coal+cleaned coal) the again washing method sorting that heavily is situated between, the treating capacity that heavily is situated between reaches 88%.If by existing three products jigging master wash, middle coal heavily is situated between again washing method sorting, the treating capacity that heavily is situated between reaches 48%.There are the following problems for these methods: get involved heavily 1. that to wash the partial feed cleaning amount system that greatly, heavily is situated between huge; 2. the large system of two covers is with depositing, and gross investment is high; 3. the large system of two covers is with operation, complexity; 4. cost of business operation is high.Just because of these problems, so that these good methods can not be applied preferably.This has become expert and scholar for many years always in effort, and never obtains something of fine solution.
Analyze from the principle of coal jigging method, coal jigging is that coal carries out sorting by density variation in the speed change current of vertical lift, this sorting is relevant with granularity and the shape of coal, belong to a kind of coarse fuzzy sorting, the result is that the material within theoretical separa tion density δ ± 0.1 can not strictly separate by proportion.
Density and relation with contents curve map (as shown in Figure 1) from a certain difficult separation coal, content within the theoretical separa tion density 1.41 ± 0.1 reaches 28%, if only this wherein not thin-graded that some of the utmost point take out the choosing that heavily is situated between again, heavily getting involved the amount of washing will be less than 20%, this will become many times reduce heavily to be situated between system scale.
Summary of the invention
The purpose of this invention is to provide and a kind ofly by four-product jigging technology raw coal is divided into spoil, middle coal, inferior cleaned coal, four products of cleaned coal first, and then the coal preparation method that time cleaned coal is selected with small simplified heavy medium sorting technology again.The method has gross investment still less, and system is simpler, and the advantage that cost of business operation is lower can reach the raising system reliability, reduces system power dissipation, the purpose of streamlining management and maintenance work.The method can realize under the prior art level easily, is conducive to promote the use of in the medium and small coal washery of the horizontal backward areas of operational administrative, uses the washing cost lower in super-huge coal washery.
Technical scheme of the present invention is summarized as follows:
The coal preparation method that a kind of four-product jigging main separation, inferior cleaned coal small simplified heavy medium select again, comprise existing three sections coal jigging methods and small simplified heavy medium coal preparation method, in three sections coal jigging methods, the middle product of coal of the 3rd section discharge of jigging machine is carried out online again sorting by small simplified heavy medium Recognition Applied in Coal Preparation System.
The coal preparation method that four-product jigging main separation of the present invention, inferior cleaned coal small simplified heavy medium select is again wherein controlled the product quality of the 3rd section discharge of jigging machine, allows the product quality of this section discharge be the inferior cleaned coal close to separating density.
The coal preparation method that four-product jigging main separation of the present invention, inferior cleaned coal small simplified heavy medium select again, the quantity that wherein controls the product of the 3rd section discharge of jigging machine arrives minimum.
The coal preparation method that four-product jigging main separation of the present invention, inferior cleaned coal small simplified heavy medium select again, its middle-size and small-size dense media are simplified Recognition Applied in Coal Preparation System for there being two product heavy-medium cyclones of pressure to simplify separation system.
It is that three products heavy medium cyclone is simplified separation system that the coal preparation method that four-product jigging main separation of the present invention, inferior cleaned coal small simplified heavy medium select again, its middle-size and small-size dense media are simplified Recognition Applied in Coal Preparation System.
The coal preparation method that four-product jigging main separation of the present invention, inferior cleaned coal small simplified heavy medium select again, its middle-size and small-size dense media are simplified the dense media simplification separation system that Recognition Applied in Coal Preparation System is other form.
Another object of the present invention provides the Recognition Applied in Coal Preparation System that a kind of four-product jigging main separation, inferior cleaned coal small simplified heavy medium are selected again, comprises following process procedure:
A. raw coal is carried out the sorting of four-product jigging;
B. the inferior head coal product of the 3rd section discharge of jigging machine, send into the sorting link that heavily is situated between;
C. after other products obtained therefrom cleaned coal, middle coal and spoil dewater respectively, in coal and spoil product send into respectively middle coal bunker and waste bin, cleaned coal enters next step;
D. the head coal product from step c is carried out primary dewatering and second dehydration, the gained sieve is top grade to be the piece head coal product, and sends into the cleaned coal storehouse; The sieve low-grades enter buffer barrel, send into cleaned coal mud concentrate cyclone with the cleaned coal dredge pump again and concentrate, and concentrated gained overflow enters the flotation link, and concentrated gained underflow enters cleaned coal mud high-frequency screen;
E. cleaned coal mud high-frequency screen gained sieve is top grade is thin head coal product, and sends into the cleaned coal storehouse; Cleaned coal mud high-frequency screen gained sieve is gone to the bottom and is flow to into the flotation link;
F. the inferior cleaned coal from step b is carried out fragmentation and sends into the qualified medium bucket, be pumped into two products with qualified medium and have and press cyclone to carry out sorting afterwards;
G. counterweight Jie sorting products obtained therefrom cleaned coal, middle coal carry out respectively a de-mediated, and the sieve low-grades of described cleaned coal enter shunting, and the sieve low-grades of part shunting and middle coal enter the qualified medium bucket, wherein sieve the top grade next step that enters;
H. two kinds of products from step g are carried out respectively secondary de-mediated, dehydration, wherein the selected sieve of two kinds of products is top grade is respectively cleaned coal piece, middle coal cinder, and sends into respectively cleaned coal storehouse and middle coal bunker;
I. collect cleaned coal among the above-mentioned steps h and rare Jie of sieve low-grades of middle coal secondary de-mediated, and from the part shunting of step g, carry out magnetic separation;
J. magnetic separation gained medium enters the qualified medium bucket, and magnetic separation gained mine tailing is sent into middle coal slime bucket;
K. to the mine tailing in the middle coal slime bucket in step j, with in the coal medium pump send into middle coal slime concentrate cyclone and concentrate, concentrated gained overflow enters the flotation link, concentrated gained underflow enters middle coal slime high-frequency screen;
L. middle coal slime high-frequency screen gained sieve is top grade is middle product of coal, and sends into middle coal bunker; Middle coal slime high-frequency screen gained sieve is gone to the bottom and is flow to into next step;
M. send into flotation device after overflow converges from underflow under the sieve of step l with from step k;
N. carry out flotation to the black water from step k and step m, and from the black water of steps d and step e, the gained flotation concentrate enters the concentrate pond, and the gained flotation tailing enters thickener;
O. to entering the flotation concentrate in the concentrate pond among the above-mentioned steps n, deliver in the clean coal pressur filter with the concentrate feed pump and dewater, the gained filter cake is the fine cleaned coal product, and sends into the cleaned coal storehouse; Gained filtrate enters circulating water pool;
P. to from the black water that enters thickener among the step n, concentrate in thickener, gained overflows to circulating water pool, and the gained underflow is delivered in the tail coal filter press with the mine tailing feed pump and dewatered, and the gained filter cake is product from failing, and sends into tailing bin; Gained filtrate enters circulating water pool;
Q. to from the filtrate of step o and filtrate and the overflow of step p, in circulating water pool, store, with water circulating pump for systemic circulation;
R. circulating water pool is added the water of disappearance;
S. the qualified medium bucket is added the medium of disappearance.
The Recognition Applied in Coal Preparation System that four-product jigging main separation of the present invention, inferior cleaned coal small simplified heavy medium select again, wherein control the product quality of the 3rd section discharge of jigging machine among the above-mentioned steps b, allow the product quality of this section discharge be the inferior cleaned coal close to separating density, and the product quantity of the 3rd section discharge of control jigging machine is to minimum.
The Recognition Applied in Coal Preparation System that four-product jigging main separation of the present invention, inferior cleaned coal small simplified heavy medium select again, wherein to cleaned coal second dehydration, classification, and products obtained therefrom also comprises the steps: behind the clean coal slime dewatering
Gained smalls is wherein carried out centrifugal dehydration;
Fine cleaned coal sieves top and is divided into the fine cleaned coal product after centrifugal dehydration, send into the cleaned coal storehouse, and the lower part of screen is divided into black water and enters buffer barrel, carries out flotation.
The present invention compares with Recognition Applied in Coal Preparation System with dense media combined coal-dressing method with the jigging of prior art, has fully shown following advantage:
1. heavily Jie's scale reduces 2-4 doubly, has reduced to greatest extent the system that heavily is situated between;
2. brought into play to greatest extent the advantage of jigging;
3. gross investment more economizes, and system is simpler, and cost of business operation is lower;
4. improve system reliability, reduced system power dissipation, streamlining management and maintenance work;
5. the method and technique can realize under the prior art level conditions easily;
6. be more conducive in the medium and small coal washery of the horizontal backward areas of operational administrative, promote the use of;
Cost is lower when 7. using washing in super-huge coal washery.
In sum, advantage of the present invention is: system's investment reduces, and system reliability improves, and system consumption power reduces, it is further simple to administer and maintain work, coal preparation method and Recognition Applied in Coal Preparation System that to be the jigging more simplified in a kind of present coal separation industry unite with dense media.
Description of drawings
Fig. 1 represents a kind of density and relation with contents curve synoptic diagram of difficult separation coal
Fig. 2 represents the Recognition Applied in Coal Preparation System process flow diagram that a kind of four-product jigging main separation, inferior cleaned coal small simplified heavy medium select again
The specific embodiment
Technical method of the present invention is summarized as follows:
The coal preparation method that a kind of four-product jigging main separation, inferior cleaned coal small simplified heavy medium select again, comprise existing three sections coal jigging methods and small simplified heavy medium coal preparation method, in three sections coal jigging methods, the middle product of coal of the 3rd section discharge of jigging machine is carried out online again sorting by small simplified heavy medium Recognition Applied in Coal Preparation System.
The coal preparation method that four-product jigging main separation of the present invention, inferior cleaned coal small simplified heavy medium select is again wherein controlled the product quality of the 3rd section discharge of jigging machine, allows the product quality of this section discharge for relatively close to the inferior cleaned coal of separating density.
The coal preparation method that four-product jigging main separation of the present invention, inferior cleaned coal small simplified heavy medium select again, the quantity that wherein controls the product of the 3rd section discharge of jigging machine arrives minimum.
The coal preparation method that four-product jigging main separation of the present invention, inferior cleaned coal small simplified heavy medium select again, its middle-size and small-size dense media are simplified Recognition Applied in Coal Preparation System for there being two product heavy-medium cyclones of pressure to simplify separation system.
It is that three products heavy medium cyclone is simplified separation system that the coal preparation method that four-product jigging main separation of the present invention, inferior cleaned coal small simplified heavy medium select again, its middle-size and small-size dense media are simplified Recognition Applied in Coal Preparation System.
The coal preparation method that four-product jigging main separation of the present invention, inferior cleaned coal small simplified heavy medium select again, its middle-size and small-size dense media are simplified the dense media simplification separation system that Recognition Applied in Coal Preparation System is other form.
Below in conjunction with accompanying drawing Recognition Applied in Coal Preparation System technological process of the present invention is done as detailed below:
Fig. 2 is the Recognition Applied in Coal Preparation System process chart that a kind of four-product jigging main separation, inferior cleaned coal small simplified heavy medium select again, in the jigging system, be with first water running, heavily be with first the qualified medium operation in Jie system, behind two system's normal operations, raw coal feeds three sections jigging machines 2 through coal supply link 1, and its technological process comprises the steps:
A. after raw coal enters three sections jigging machines 2, sub-elect cleaned coal, middle coal, inferior cleaned coal, four kinds of products of spoil by this jigging machine;
B. the inferior head coal product of the 3rd section discharge of three sections jigging machines 2, send into the sorting link 35 that heavily is situated between;
C. other products obtained therefrom cleaned coal, middle coal and spoil dewater respectively, and coal and spoil product are sent into respectively middle coal bunker 19 and waste bin 18 in the rear handle, and cleaned coal enters next step;
D. the head coal product from step c is entered camber sieve 3 successively and straight line shaker 4 carries out primary dewatering and second dehydration, the gained sieve is top grade to be the piece head coal product, and sends into cleaned coal storehouse 20; The sieve low-grades enter buffer barrel 5, send into cleaned coal mud concentrate cyclone 7 with cleaned coal dredge pump 6 again and concentrate, and are concentrated that overflow enters flotation link 9, and concentrated gained underflow enters cleaned coal mud high-frequency screen 8;
E. cleaned coal mud high-frequency screen 8 gained sieve is top grade is thin head coal product, and sends into cleaned coal storehouse 20; Cleaned coal mud high-frequency screen 8 gained sieve is gone to the bottom and is flow to into flotation link 9;
F. the inferior cleaned coal from step b is carried out fragmentation 35 and sends into qualified medium bucket 33, sending into two products with qualification medium pump 34 has the cyclone 22 of pressure to carry out sorting.
G. counterweight Jie sorting gained head coal product carries out a de-mediated 23, product of coal carries out a de-mediated 24 in counterweight Jie sorting gained, the sieve low-grades of described cleaned coal enter shunting 26, and the sieve low-grades of part shunting and middle coal enter qualified medium bucket 33, wherein sieve the top grade next step that enters;
H. the head coal product from step g is carried out secondary de-mediated, dehydration 25, wherein selected sieve is top grade is the cleaned coal piece, and sends into cleaned coal storehouse 20; Middle product of coal from step g is carried out secondary de-mediated, dehydration 27, and wherein selected sieve is top grade is middle coal cinder, and sends into middle coal bunker 19;
I. collect cleaned coal among the above-mentioned steps h and rare Jie of sieve low-grades of middle coal secondary de-mediated, and from the part shunting of step g, carry out magnetic separation 28;
J. magnetic separation 28 gained media enter qualified medium bucket 33, and magnetic separation 28 gained mine tailings are sent into middle coal slime bucket 29;
K. to from the mine tailing in the middle coal slime bucket 29 among the step j, with in coal medium pump 30 send into middle coal slime concentrate cyclone 31 and concentrate, concentrated gained overflow enters flotation link 9, concentrated gained underflow enters middle coal slime high-frequency screen 32;
L. middle coal slime high-frequency screen 32 gained sieve is top grade is middle product of coal, and sends into middle coal bunker 19; Middle coal slime high-frequency screen gained sieve is gone to the bottom and is flow to into next step;
M. send into flotation device 9 after overflow converges from underflow under the sieve of step l with from step k;
N. carry out flotation 9 to the black water from step k and step m, and from the black water of steps d and step e, the gained flotation concentrate enters concentrate pond 10, and the gained flotation tailing enters thickener 13;
O. to entering the flotation concentrate in the concentrate pond 10 among the above-mentioned steps n, deliver in the clean coal pressur filter 12 with concentrate feed pump 11 and dewater, the gained filter cake is the fine cleaned coal product, and sends into cleaned coal storehouse 20; Gained filtrate enters circulating water pool 16;
P. to from the black water that enters thickener 13 among the step n, concentrate in thickener, gained overflows to circulating water pool 16, and the gained underflow is delivered in the refuse filter press 15 with mine tailing feed pump 14 and dewatered, the gained filter cake is product from failing, and sends into tailing bin 21; Gained filtrate enters circulating water pool 16;
Q. to from the filtrate of step o and filtrate and the overflow of step p, in circulating water pool 16, store, use water circulating pump 17 for systemic circulation during use;
R. circulating water pool 16 is added the water of disappearance;
S. qualified medium bucket 33 is added the medium of disappearance.
In the above-mentioned processing step, and the conveying that does not indicate on the figure, recirculated water, moisturizing, detection, control, the system such as electric be routine techniques, no longer narration here.
Based on same principle and method, the present invention can be in above-mentioned processing step b, product quality and the quantity of control jigging machine the 3rd section discharge, allow the product quality of this section discharge for relatively close to the inferior cleaned coal of separating density, make the product quantity of the 3rd section discharge of jigging machine minimum.Do like this and can reach goal of the invention equally, and can bring into play to a greater extent the function of jigging machine, reduce to greatest extent scale and the treating capacity of the system that heavily is situated between.
Based on same principle and method, the present invention can in above-mentioned processing step, increase cleaned coal second dehydration, classification, and gained smalls product carry out the centrifugal dehydration step behind the clean coal slime dewatering:
Fine cleaned coal sieves top and is divided into the fine cleaned coal product after centrifugal dehydration, send into the cleaned coal storehouse, and the lower part of screen is divided into black water and enters buffer barrel, carries out flotation; Do like this and can reach goal of the invention equally, and can further reduce head coal product moisture content.
Based on same principle and method, the present invention can in above-mentioned processing step, increase buffering, pumping, preprocessor link before flotation device.Do like this and can reach goal of the invention equally.Described buffering, pumping, preprocessor link are routine techniques, here no longer narration.
In sum, above embodiment is described as the basis take a kind of typical process flow shown in Figure 2, based on same principle and method, the present invention also can be incorporated in the flow process by the principle in the technique shown in Figure 2 and the method small simplified heavy medium sorting process with other pattern, realizes equally the process coal preparation flowsheet that the four-product jigging main separation of corresponding form, inferior cleaned coal small simplified heavy medium select again.
As mentioned above, the coal preparation method and the technique that adopt a kind of four-product jigging main separation of the present invention, inferior cleaned coal small simplified heavy medium to select again, can obtain the investment of minimizing system, improve system reliability, reduce system consumption power, improving the effect of the work that administers and maintains, is jigging and the dense media combined coal-dressing Method and process of more simplifying in a kind of present coal separation industry.
The invention discloses coal preparation method and technique that a kind of four-product jigging main separation, inferior cleaned coal small simplified heavy medium are selected again; although more than enumerated less embodiment; but for those of ordinary skill in the art; some remodeling that the present invention is done, improvement, replacement etc.; perhaps above-mentioned embodiment is done any combination variation, all drops within protection scope of the present invention.

Claims (2)

1. coal preparation method that four-product jigging main separation, inferior cleaned coal small simplified heavy medium select again, comprise existing three sections coal jigging methods and small simplified heavy medium coal preparation method, it is characterized in that: in three sections coal jigging methods the inferior head coal product of the 3rd section discharge of jigging machine is carried out online again sorting by small simplified heavy medium Recognition Applied in Coal Preparation System, it comprises following technological process:
A. raw coal is carried out the sorting of four-product jigging;
B. the inferior head coal product of the 3rd section discharge of jigging machine, send into the sorting link that heavily is situated between;
C. after other products obtained therefrom cleaned coal, middle coal and spoil dewater respectively, in coal and spoil product send into respectively middle coal bunker and waste bin, cleaned coal enters next step;
D. to carrying out primary dewatering and second dehydration from step c head coal product, the gained sieve is top grade to be the piece head coal product, and sends into the cleaned coal storehouse; The sieve low-grades enter buffer barrel, send into cleaned coal mud concentrate cyclone with the cleaned coal dredge pump again and concentrate, and concentrated gained overflow enters the flotation link, and concentrated gained underflow enters cleaned coal mud high-frequency screen;
E. cleaned coal mud high-frequency screen gained sieve is top grade is thin head coal product, and sends into the cleaned coal storehouse; Cleaned coal mud high-frequency screen gained sieve is gone to the bottom and is flow to into the flotation link;
F. the inferior cleaned coal from step b is carried out fragmentation and sends into the qualified medium bucket, rear being pumped into qualified medium presses two product heavy-medium cyclones to carry out sorting;
G. counterweight Jie sorting products obtained therefrom cleaned coal, middle coal carry out respectively a de-mediated, and the sieve low-grades of described cleaned coal enter shunting, and the sieve low-grades of part shunting and middle coal enter the qualified medium bucket, wherein sieve the top grade next step that enters;
H. two kinds of products from step g are carried out respectively secondary de-mediated, dehydration, wherein the selected sieve of two kinds of products is top grade is respectively cleaned coal piece, middle coal cinder, and sends into respectively cleaned coal storehouse and middle coal bunker;
I. collect rare Jie of sieve low-grades of above-mentioned steps h cleaned coal and the de-mediated of middle coal secondary, and shunt from the part of step g, carry out magnetic separation;
J. magnetic separation gained medium enters the qualified medium bucket, and magnetic separation gained mine tailing is sent into middle coal slime bucket;
K. to from the mine tailing in the middle coal slime bucket among the step j, with in the coal medium pump send into middle coal slime concentrate cyclone and concentrate, concentrated gained overflow enters the flotation link, concentrated gained underflow enters middle coal slime high-frequency screen;
L. middle coal slime high-frequency screen gained sieve is top grade is the detail product of coal, and sends into middle coal bunker; Middle coal slime high-frequency screen gained sieve is gone to the bottom and is flow to into next step;
M. send into flotation device after overflow converges from underflow under the sieve of step 1 with from step k;
N. carry out flotation to the black water from step k and step m, and from the black water of steps d and step e, the gained flotation concentrate enters the concentrate pond, and the gained flotation tailing enters thickener;
O. to entering the flotation concentrate in the concentrate pond among the above-mentioned steps n, deliver in the clean coal pressur filter with the concentrate feed pump and dewater, the gained filter cake is the fine cleaned coal product, and sends into the cleaned coal storehouse; Gained filtrate enters circulating water pool;
P. to from the black water that enters thickener among the step n, concentrate in thickener, the gained overflow is discharged to circulating water pool, and the gained underflow is delivered in the refuse filter press with the mine tailing feed pump and dewatered, and the gained filter cake is product from failing, and sends into tailing bin; Gained filtrate enters circulating water pool;
Q. to from the filtrate of step o and filtrate and the overflow of step p, in circulating water pool, store, with water circulating pump for systemic circulation;
R. circulating water pool is added the water of disappearance;
S. the qualified medium bucket is added the medium of disappearance.
2. the coal preparation method that selects again of a kind of four-product jigging main separation as claimed in claim 1, inferior cleaned coal small simplified heavy medium is characterized in that: have two product heavy-medium cyclones of pressure to replace with three products heavy medium cyclone and simplify separation system.
CN 200910131301 2009-04-14 2009-04-14 A coal dressing method and system of four-product jigging primary cleaning, secondary head coal small simplified heavy medium reelecting Active CN101530824B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN 200910131301 CN101530824B (en) 2009-04-14 2009-04-14 A coal dressing method and system of four-product jigging primary cleaning, secondary head coal small simplified heavy medium reelecting

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN 200910131301 CN101530824B (en) 2009-04-14 2009-04-14 A coal dressing method and system of four-product jigging primary cleaning, secondary head coal small simplified heavy medium reelecting

Publications (2)

Publication Number Publication Date
CN101530824A CN101530824A (en) 2009-09-16
CN101530824B true CN101530824B (en) 2013-10-16

Family

ID=41101809

Family Applications (1)

Application Number Title Priority Date Filing Date
CN 200910131301 Active CN101530824B (en) 2009-04-14 2009-04-14 A coal dressing method and system of four-product jigging primary cleaning, secondary head coal small simplified heavy medium reelecting

Country Status (1)

Country Link
CN (1) CN101530824B (en)

Families Citing this family (25)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102059174B (en) * 2010-12-19 2016-01-20 烟台金华选煤工程有限公司 A kind of cleaned coal dehydration and realize this technique equipment combination
CN102179288A (en) * 2010-12-21 2011-09-14 王万明 Coal-reselecting process for heavy media coal separation
CN102357405A (en) * 2011-08-21 2012-02-22 太原艾柯夫选煤技术有限公司 Middling coal crushing, recleaning and quality improving method
CN103203280B (en) * 2012-06-20 2015-06-03 安徽恒源煤电股份有限公司 Dense-medium preparation technology for optimizing coal slime
CN102794227B (en) * 2012-08-22 2015-12-09 山西晋城无烟煤矿业集团有限责任公司 The lower dielectric film filter method of block spoil sieve and device
CN102896036B (en) * 2012-09-24 2014-01-01 刘立文 Three-section four-product heavy media coal preparation process
CN103170405B (en) * 2013-02-28 2015-07-08 宝钢集团新疆八一钢铁有限公司 Coal separation method for advanced dense medium cyclone technology
CN103394422A (en) * 2013-07-31 2013-11-20 神华集团有限责任公司 Method for separating coal and rock components from raw coal
CN103350027B (en) * 2013-08-06 2015-08-05 煤炭科学研究总院唐山研究院 Graded desliming pressurized feeding three products heavy medium cyclone coal preparation technique
CN105750075A (en) * 2014-03-10 2016-07-13 衢州市易凡设计有限公司 Device for washing separation of high-ash, high-clay and high-gangue coal
CN105944823A (en) * 2014-03-10 2016-09-21 衢州市易凡设计有限公司 Equipment for washing high-ash, high-mud and high-gangue stone coal
CN105016091B (en) * 2015-05-29 2018-08-17 内蒙古上海庙矿业有限责任公司 Sell terminal apparatus to a kind of coal
CN105057218B (en) * 2015-07-16 2017-06-06 陕西蟠龙实业有限公司 A kind of new dry coal preparation system and method
CN105694943B (en) * 2016-01-27 2017-04-26 中科合成油技术有限公司 Joint-converted polygeneration method for multiple coal types
CN105665124B (en) * 2016-04-13 2019-05-28 中国矿业大学 High intergrowth high ash sulphur coal sorts slurrying integral process
CN106179719B (en) * 2016-05-14 2019-06-21 北京浩沃特矿业技术有限公司 Container-combination formula module dense-medium separation system
CN106370555A (en) * 2016-10-10 2017-02-01 山西汾西矿业(集团)有限责任公司 Densitometer device for coal dressing system
CN107020201B (en) * 2017-06-14 2023-07-25 淮南矿业(集团)有限责任公司 Thickener underflow coarse slime recovery system
CN108273655A (en) * 2018-01-12 2018-07-13 华北科技学院 A kind of coal jigging system and method
CN108296009B (en) * 2018-01-29 2020-11-03 内蒙古伊泰煤炭股份有限公司 Coal deep processing method and coal treatment method
CN109201314B (en) * 2018-09-11 2020-12-01 乌拉特中旗毅腾矿业有限责任公司 Clean utilization production process for middlings
CN109701729B (en) * 2019-01-14 2020-11-17 乌拉特中旗毅腾矿业有限责任公司 Clean utilization production process for middlings
CN109794349B (en) * 2019-03-08 2020-03-17 中国矿业大学 Underground coal dressing process
CN109718944B (en) * 2019-03-08 2019-11-29 中国矿业大学 A kind of aqueous medium underground coal preparation technique
CN114887758B (en) * 2022-04-26 2023-10-20 鞍钢集团矿业有限公司 Stage grinding and selecting process for magnetite ore with sand setting and tailing discarding functions

Also Published As

Publication number Publication date
CN101530824A (en) 2009-09-16

Similar Documents

Publication Publication Date Title
CN101530824B (en) A coal dressing method and system of four-product jigging primary cleaning, secondary head coal small simplified heavy medium reelecting
CN1186126C (en) Process for heavy media separation of coarse coal slurry
CN109794349B (en) Underground coal dressing process
CN105597915B (en) The wide dual Jie's whole coarse slime separating process of grade can be achieved in one kind
CN103143432B (en) Efficient crushing and three-section type screening method of coking coal gravity middings
CN107008565A (en) A kind of thermal coal deep screening and dense medium separation technique
CN102728455B (en) Combined separation process for gravity concentration and flotation of difficult separation coal slime with high intermediate density material content
CN103240168A (en) Grading separation and dehydration method for high-ash difficult-separation coal slime
CN104084293B (en) Dense medium coarse slime sorting device and sorting process
CN106179717A (en) A kind of full level of thermal coal is selected in simplified heavy medium sorting process
CN102430481A (en) Sorting process for high-ash and difficult-separation coal slime
CN105080701A (en) Separation method for roughing slime through teetered bed separator (TBS) and concentrating coarse slime difficult to separate through slime dense medium cyclone
CN104549710A (en) Three-stage opening compounding separation process and three-stage opening compounding separation system for coarse slime
CN101185912A (en) Torbanite washbox, coal separation system and coal separation method thereof
CN107008566B (en) A kind of steam coal separation technique
CN108745622A (en) A kind of jet coal washing system and washing method
CN104475238A (en) Enrichment method for sedimentary type vanadium ores
CN103252286B (en) Method for using dense medium to sort coal-series kaolinite rocks in gangues
CN110170370B (en) System and process for reducing lower limit of gravity separation granularity of dense medium coal preparation plant
CN1210107C (en) Heavy medium separating process for slime
CN110052326B (en) System and method for purifying and recycling refined coal slime
CN113560033B (en) Intelligent coal powder removal washing and selecting system and method
CN1465441A (en) Dense-media and flotation combined coal-dressing optimization method
CN104436854A (en) Slime water serial treatment system and slime water serial treatment process
CN109821648B (en) Re-selection system of medium coal pressure-free three-product dense medium cyclone of jigging

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
C53 Correction of patent for invention or patent application
CB02 Change of applicant information

Address after: 100083, room 3, building 16, 402 Qinghua East Road, Beijing, Haidian District

Applicant after: Jinyitong Science and Technology (Beijing) Co., Ltd.

Address before: 100083, room 3, building 16, 204 Qinghua East Road, Beijing, Haidian District

Applicant before: Jinyitong Science and Technology (Beijing) Co., Ltd.

C53 Correction of patent for invention or patent application
CB02 Change of applicant information

Address after: 100083, room 3, building 16, 402 Qinghua East Road, Beijing, Haidian District

Applicant after: Jinyitong Technology (Beijing) Co.,Ltd.

Address before: 100083, room 3, building 16, 402 Qinghua East Road, Beijing, Haidian District

Applicant before: Jinyitong Science and Technology (Beijing) Co., Ltd.

C14 Grant of patent or utility model
GR01 Patent grant