CN100540633C - Two stage dewatering technology of fine coal mud - Google Patents
Two stage dewatering technology of fine coal mud Download PDFInfo
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- CN100540633C CN100540633C CNB200610102141XA CN200610102141A CN100540633C CN 100540633 C CN100540633 C CN 100540633C CN B200610102141X A CNB200610102141X A CN B200610102141XA CN 200610102141 A CN200610102141 A CN 200610102141A CN 100540633 C CN100540633 C CN 100540633C
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Abstract
本发明公开一种选煤工艺，具体地说是一种精煤泥双段脱水工艺。该工艺分为精煤泥脱水回收和细精煤泥脱水回收两段作业，按下述步骤进行，精煤磁选机尾矿用泵送到振动弧形筛进行分级，其筛下水用管路输出至浮选机，筛上的粗精煤泥与浮选机排出的浮选泡沫汇同一起输出至沉降过滤式离心脱水机进行煤泥掺粗，沉降过滤式离心脱水机回收＞0.045mm粒级为主的粗精煤泥，离心机的滤液返回它的入料管，离心液入压滤机；离心液用压滤机脱水回收，回收＜0.045mm细精煤泥，其清净的滤液汇入循环水作为脱节筛的喷水和浮选作业的稀释水，细精煤泥和粗精煤泥为产品。本发明工艺简单，用本发明所选的粗精煤泥综合水分低，商品精煤水分稳定在10%。
The invention discloses a coal preparation process, in particular to a double-stage dehydration process of clean coal slime. The process is divided into two stages: clean coal slime dehydration recovery and fine fine coal slime dehydration recovery, which are carried out according to the following steps. The tailings of the clean coal magnetic separator are pumped to the vibrating arc screen for classification, and the water under the screen is pipelined. Output to the flotation machine, the coarse fine coal slime on the sieve and the flotation foam discharged from the flotation machine are combined and output to the sedimentation filter centrifugal dehydrator for coal slime mixing, and the sedimentation filter centrifugal dehydrator recovers particles > 0.045mm The filtrate of the centrifuge is returned to its feeding pipe, and the centrate is fed into the filter press; the centrate is dehydrated and recovered by the filter press, and the fine fine coal slime <0.045mm is recovered, and the clean filtrate sinks The circulating water is used as the dilution water for spraying and flotation operations of the disjointed sieve, and fine fine coal slime and coarse fine coal slime are the products. The process of the invention is simple, the comprehensive water content of the coarse and fine coal slime selected by the invention is low, and the water content of the commercial clean coal is stable at 10%.
Description
Technical field
The present invention relates to a kind of coal preparation technique, specifically a kind of two stage dewatering technology of fine coal mud.
Background technology
Moisture of cleaned coal content is an important product index of check quality of cleaned coal, and moisture of cleaned coal is too high, will have a negative impact to national economy, mainly contains following several respects
For coking coal cleans, the moisture superelevation will prolong the coking time, reduce coke oven output, shorten coke oven work-ing life.For non-coking coal cleans, its thermal value increases with moisture and descends.
Most coal separating plants are far away from the user, and moisture is too high will inevitably to cause invalid transportation.
At the northern China severe winter, during with train transportation cleaned coal, can on railcar and track, freeze phenomenon if moisture of cleaned coal is too high, so that overstock railway carriage, stop up battle line, influence normal safe operation.So some coal separating plant in three northern areas of China has to build the warming up storehouse, consumes a large amount of heat energy, is used for cleaned coal and thaws.
Developed country requires between 8-10% the commodity moisture of cleaned coal as far back as the eighties in last century, and China is because dehydration equipment and technologic backwardness, moisture of cleaned coal is paced up and down between 11-13% for a long time, so that export moisture of cleaned coal above 10% o'clock, face foreign trader's claim or rejection, cause financial loss.
The first cause that China's moisture of cleaned coal is high is a floatation clean coal moisture height, raising along with the mining mechanization degree, the primary slime amount is also corresponding to be increased, the floatation clean coal amount generally accounts for sells about 20% of cleaned coal, that have even more than 30%, how cleaned coal muddy water branch being lowered, is key subjects that must solve.For this reason, some coal separating plant of China once adopted screen-bowl centrifuge that floatation clean coal is carried out the single hop dewatering and recovery, but did not have successful story, and its reason is:
Give dewatering and recovery for all thin mud are all settled down, just must increase the rotating speed of whizzer spiral and rotary drum.Can make equipment dynamic consumption strengthen like this, require higher manufacturing accuracy and maintaining level, cause acquisition expenses and running cost to improve.The rotating speed of spiral and rotary drum is fast more in fact, and the hindered falling degree is also just serious more, can not reach the purpose that all thin mud can both sedimentation reclaim.
The filtrate of screen-bowl centrifuge, centrifugate are carried thin mud and are returned flotation operation, and its internal circulating load is about 20%, and therefore make flotation machine volume, flotation agent addition, the also corresponding increase of the dilution water yield has also increased the process cost of full factory.Because thin mud participates in circulation, also constantly produce secondary thin mud, cause floatation feed flotability variation.
In recent years, China also applies pressure filter in succession, clean coal pressur filter carries out dewatering and recovery to floatation clean coal, has replaced the vacuum filter of original use, and commercial coal moisture is dropped to below 11%.Its weak point is a capital construction investment expense height, and equipment electric motor total power height wastes energy.
Summary of the invention
The technical problem to be solved in the present invention is the many defectives at prior art, provides the comprehensive moisture of a kind of coarse coal slurry low, and the commodity moisture of cleaned coal is stabilized in 10%, saves the energy, the two stage dewatering technology of fine coal mud that equipment hunchback expense is low.
Solve the problems of the technologies described above by the following technical solutions:
A kind of two stage dewatering technology of fine coal mud, involving vibrations sieve-bend screen, flotation machine, screen-bowl centrifuge is characterized in that, and described technology is divided into clean coal slime dewatering and reclaims and two sections operations of refined coal slurry dewatering and recovery, and this technology is undertaken by following step,
Cleaned coal magnetic separator mine tailing carries out classification with being pumped into vibration sieve bend, its backwater exports flotation machine to pipeline, the flotation froth that coarse coal slurry on the sieve and flotation machine are discharged is reinstated feeding pipe with one and is exported screen-bowl centrifuge to and carry out coal slime and mix slightly, screen-bowl centrifuge recovery＞0.045mm grade is main coarse coal slurry, the filtrate of whizzer is returned its feeding pipe, and centrifugate is gone into pressure filter;
Centrifugate pressure filter dewatering and recovery, recovery＜0.045mm refined coal slurry, its peace and quiet filtrate imports recirculated water as the water spray of sieve and the dilution water of flotation operation of disconnecting, and refined coal slurry and coarse coal slurry are product.
Owing to adopted technique scheme, the present invention compared with prior art adopts two stage dewatering technologies, the comprehensive moisture of coarse coal slurry is reduced significantly, can make coal separating plant's commodity moisture of cleaned coal be stabilized in 10%, satisfy user's specification of quality, reduce the invalid transportation that commercial coal carries the water yield.Can not re-use the heating power drying facility of the wasteful amount energy at severe cold season for the coal separating plant that is in northern area.The present invention is lower than the capital construction investment expense of two kinds of technologies of background technology, especially just 31% of pressure filter (expression as follows) on equipment electric motor total power.
Table the present invention is (286t feed coal/h. production system) compared with the prior art
| Scheme | The two sections of screen-bowl centrifuge and pressure filter reclaim | Pressure filter single hop dewatering and recovery | Pressure filter single hop dewatering and recovery |
| Main frame model and platform number | 2 of LWZ1400 * 1 XMGZ350/1600-X/U type of 1200 type whizzers pressure filter | 4 in XMGZ250/1600-X/U type pressure filter | 1 of GPJ120 type pressure filter |
| Utility appliance platform number | 7 | 11 | 9 |
| Equipment electric motor total power/KW | 427.5 | 402.1 | 1378.84 |
| Purchasing and installation costs/ten thousand yuan of electromechanical equipment, non-standard component, pipeline | 382.48 | 470.37 | 849.39 |
| Civil engineering is with/ten thousand yuan | 60.98 | 47.12 | 88.70 |
| Add up to/ten thousand yuan | 443.46 | 517.49 | 938.09 |
| Labour requirement/people. the class of production | 5 | 8 | 5 |
Description of drawings
Accompanying drawing 1 is a process flow sheet of the present invention.
Embodiment
Below in conjunction with accompanying drawing the present invention is done further detailed description.
Referring to accompanying drawing 1, a kind of two stage dewatering technology of fine coal mud, involving vibrations sieve-bend screen, flotation machine, screen-bowl centrifuge.Described technology is divided into clean coal slime dewatering and reclaims and two sections operations of refined coal slurry dewatering and recovery, and this technology is undertaken by following step,
Cleaned coal magnetic separator mine tailing carries out classification with being pumped into vibration sieve bend, its backwater exports flotation machine to pipeline and carries out flotation operation, the flotation froth that coarse coal slurry on the sieve and flotation machine are discharged is reinstated feeding pipe with one and is exported screen-bowl centrifuge to and carry out coal slime and mix slightly, screen-bowl centrifuge recovery＞0.045mm grade is main coarse coal slurry, the filtrate of whizzer is returned its feeding pipe, and centrifugate is gone into pressure filter;
Centrifugate pressure filter dewatering and recovery, recovery＜0.045mm refined coal slurry, its peace and quiet filtrate imports recirculated water as the water spray of sieve and the dilution water of flotation operation of disconnecting, and refined coal slurry and coarse coal slurry are product.
Use the coal separating plant of dense-medium cyclone coal preparation technique to implement two stage dewatering technology of fine coal mud embodiment.This flow process is made up of two operations.
1 coal slime dewatering reclaims operation (one section dehydration)
This operation select for use screen-bowl centrifuge reclaim＞the 0.045mm grade is main coarse coal slurry.
Pan feeding is mixed slightly
The screen overflow of cleaned coal mud vibration sieve bend and flotation froth mixed mix slightly, make the size composition chap, guarantee in the pan feeding＜0.045mm fine fraction productive rate is less than 40%, is that screen-bowl centrifuge is created necessary processing condition.
Requirement to screen-bowl centrifuge:
Select for use centrifugal intensity between 200-280, length-to-diameter ratio (rotary drum L/D ratio value) is between 1.43-2, screen-bowl centrifuge based on recovery＞0.045mm grade, require its solid recovery rate 〉=80%, in the centrifugate＞and 0.045mm grade productive rate≤20%, dewatered product moisture≤16.50%.
Refined coal slurry dewatering and recovery operation (two sections dehydrations)
This operation selects for use pressure filter to reclaim＜the 0.045mm refined coal slurry.
Solid-liquid separation is thorough, and filtrate is peace and quiet, does not have thin mud and circulates with it.
Filter cake moisture＜35%.
Effect
The comprehensive moisture of coarse coal slurry reduces significantly, and the commodity moisture of cleaned coal is stabilized in 10% level.Satisfy user's specification of quality, reduce the invalid transportation that commercial coal carries the water yield.
Working process of the present invention
Cleaned coal magnetic separator tailings pump is delivered to vibratory screening apparatus and is carried out classification, and its backwater is handled by flotation operation.Its sieve go up coarse coal slurry with flotation froth after carry out " mixing thick ", be master's grade by screen-bowl centrifuge recoverys＞0.045mm.The filtrate of whizzer is returned among its pan feeding.
Carry＜centrifugate of the screen-bowl centrifuge of 0.045mm refined coal slurry is by the pressure filter dewatering and recovery, and its peace and quiet filtrate imports recirculated water as the water spray of sieve and the dilution water of flotation operation of disconnecting.The dewatered product of screen-bowl centrifuge and pressure filter filter cake (being the coarse coal slurry of coal separating plant) mix in the cleaned coal of sink float, as final cleaned coal merchandising coking coal cleans.
Claims (2)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
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| CNB200610102141XA CN100540633C (en) | 2006-11-10 | 2006-11-10 | Two stage dewatering technology of fine coal mud |
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| CNB200610102141XA CN100540633C (en) | 2006-11-10 | 2006-11-10 | Two stage dewatering technology of fine coal mud |
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| CN1948434A CN1948434A (en) | 2007-04-18 |
| CN100540633C true CN100540633C (en) | 2009-09-16 |
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Families Citing this family (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101708634B (en) * | 2009-11-11 | 2012-01-18 | 黑旋风工程机械开发有限公司 | Stone waste sludge recycling device |
| CN102399028A (en) * | 2010-09-16 | 2012-04-04 | 永城煤电控股集团有限公司 | Technology for treating coal slime water through secondary flow and settlement filtering centrifuge |
| CN102274786A (en) * | 2011-05-18 | 2011-12-14 | 唐山国华科技国际工程有限公司 | Coal slime two-stage flotation process with granularity smaller than 0.5mm |
| CN102284354B (en) * | 2011-09-13 | 2013-01-16 | 永城煤电控股集团有限公司 | Coarse slime separating process |
| CN102357428A (en) * | 2011-10-27 | 2012-02-22 | 唐山国华科技国际工程有限公司 | Novel floatation process capable of ensuring upper limit of fed material granularity and improving dehydration effect of foam product |
| CN104722388A (en) * | 2013-12-18 | 2015-06-24 | 深圳市华天顿能源环保技术有限公司 | Method for recycling reduction coal from coal slime |
| CN104923388B (en) * | 2015-05-27 | 2017-03-22 | 安徽理工大学 | Flotation clean coal recycling even material mixing technology |
| CN105858964B (en) * | 2016-05-17 | 2019-01-25 | 北京国华科技集团有限公司 | A kind of wet coal preparation factory tail coal Slurry treatment method |
| CN106237708A (en) * | 2016-09-23 | 2016-12-21 | 苏州三体智能科技有限公司 | A kind of Coal Preparation Plant coal slime dewatering system and method |
| CN107597412A (en) * | 2017-09-21 | 2018-01-19 | 淮南矿业(集团)有限责任公司 | One kind drift mud recovery system |
-
2006
- 2006-11-10 CN CNB200610102141XA patent/CN100540633C/en active Active
Non-Patent Citations (2)
| Title |
|---|
| 煤泥水两段浓缩粗细煤泥分别回收工艺流程的评述. 张勇.煤炭工程，第2期. 1993 |
| 煤泥水两段浓缩粗细煤泥分别回收工艺流程的评述. 张勇.煤炭工程，第2期. 1993 * |
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| CN1948434A (en) | 2007-04-18 |
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