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CN102728455A - Combined separation process for gravity concentration and flotation of difficult separation coal slime with high intermediate density material content - Google Patents

Combined separation process for gravity concentration and flotation of difficult separation coal slime with high intermediate density material content Download PDF

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CN102728455A
CN102728455A CN2012102351484A CN201210235148A CN102728455A CN 102728455 A CN102728455 A CN 102728455A CN 2012102351484 A CN2012102351484 A CN 2012102351484A CN 201210235148 A CN201210235148 A CN 201210235148A CN 102728455 A CN102728455 A CN 102728455A
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coal
flotation
clean coal
separation
gravity
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CN102728455B (en
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王永田
刘炯天
于伟
周开洪
周杰
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China University of Mining and Technology CUMT
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China University of Mining and Technology CUMT
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Abstract

一种高中间密度物含量的难选煤泥重选浮选联合分选工艺,利用分级设备分级,分级后细粒粗选精煤直接进行浮选精选作业,得到细粒级精煤和尾煤产品;粗粒粗选精煤采用TBS干扰床重力分选,得到重选精煤和重选尾煤。将TBS干扰床分选得到的重选精煤通过脱水设备脱水,得到最终重选精煤产品和筛下水,筛下水合并进入细粒粗选精煤的精选作业;该工艺通过浮选粗选作业抛掉大量的高灰脉石矿物,TBS干扰床重选过程受到高灰细粒矸石的影响较小,浮选粗选粗粒精煤可以严格按照密度精确分选,提高分选效率。通过浮选和重选联合分选工艺有效地处理高中间密度物含量的难选煤泥,投资少,耗电量小,运行费用低,精煤产率高,且不破坏精煤产品的粒度组成。

Figure 201210235148

A refractory coal slime gravity separation flotation combined separation process with high intermediate density content. Classification equipment is used to classify. After classification, the fine-grained coarse-selected clean coal is directly flotation-selected to obtain fine-grained clean coal and tailings. Coal products: Coarse-grained coarse-separated clean coal adopts TBS interference bed gravity separation to obtain heavy-separated clean coal and heavy-separated tailing coal. The gravity-selected clean coal obtained by TBS interference bed separation is dehydrated through dehydration equipment to obtain the final gravity-selected clean coal product and sieve water, and the sieve water is combined into fine-grained coarse separation of clean coal; the process is through flotation rough separation A large amount of high-ash gangue minerals are thrown away during the operation, and the TBS disturbed bed gravity separation process is less affected by high-ash fine-grained gangue. Flotation roughing coarse-grained clean coal can be accurately sorted strictly according to density, and the separation efficiency is improved. The refractory coal slime with high intermediate density content can be effectively processed through the combined separation process of flotation and gravity separation, with low investment, low power consumption, low operating cost, high clean coal yield, and does not damage the particle size of clean coal products. composition.

Figure 201210235148

Description

The flotation combined sorting process of difficult separation coal mud gravity treatment of density thing content between senior middle school
Technical field
The present invention relates to a kind of slime separation technology, especially a kind of flotation combined sorting process of difficult separation coal mud gravity treatment that is applicable to density thing content between senior middle school.
Background technology
Density is at 1.4g/cm in coal slime 3-1.8g/cm 3Between the weight of material proportion that accounts for total material surpass at 30% o'clock, it can be called as density thing coal slime between senior middle school.When middle density thing content was high, coal was many with the particle of spoil adhesion, can't coal realized effectively separating with spoil through flotation, caused coal losses in tail coal, and perhaps spoil is entrained in the cleaned coal; When middle density thing content was low, pure coal and pure spoil granule content were high, can effectively separate through simple flotation and produce coal and spoil.Between senior middle school the characteristics of density thing content difficult separation coal mud mainly show the density of coal slime form in big, the several respects such as ash content is high, floatability difference of intermediate density level content, wherein intermediate density thing content is the bottleneck of restriction difficult separation coal mud sorting greatly always.This part coal slime is when flotation; Get into cleaned coal and make that then cleans ash is higher; Gets into tail coal and then cause the rate of recovery to reduce, and coal preparation plant is in order to ensure cleans ash, often through control floating agent consumption, roughly select technology means such as cleaned coal selects again and guarantee that cleans ash is qualified; And the intermediate density thing in the coal slime is finally got in the floating tail-coal, waste resource, reduced the economic benefit of coal preparation plant.This is for the rare fertile coking coal resource of China's high-quality, a kind of especially great waste.Along with the continuous minimizing of the rare fertile coking coal resource reserves of high-quality,, the difficult separation coal mud of density thing content between senior middle school is carried out efficient sorting seem particularly urgent as non-renewable resources.
Conventional flotation process is to send into floatation equipment (flotation column or flotation device) after floatation feed is handled through sizing mixing, and flotation obtains concentrate and tailings, and gets into subsequent product processing operation separately.This technology is mainly used in the conventional sorting that is prone to coal separation mud, and uses for many years in China, and for the sorting of density thing content difficult separation coal mud between senior middle school, the intermediate density thing that it is difficult in effective slime separation makes intermediate density level product often be lost in the tail coal.The efficient sorting technology of density level difficult separation coal mud has become a difficult problem needing solution in the coal resources efficient clean utilization process badly between exploitation senior middle school.
Summary of the invention
Technical problem: the objective of the invention is to overcome the weak point in the prior art, the flotation combined sorting process of difficult separation coal mud gravity treatment of density thing content between the senior middle school of provide that a kind of technology is simple, small investment, the efficiency of separation are high.
Technical scheme: the flotation combined sorting process of difficult separation coal mud gravity treatment of density thing content between senior middle school of the present invention: comprise with size mixing equipment the float coal mud of going into that adds collecting agent, foaming agent is sized mixing; The black water of sizing mixing is introduced the I floatation equipment roughly select operation, obtain I floatation clean coal and I floating tail-coal; Also comprise the steps:
A. the I floatation clean coal is sent into classifying equipoment to carrying out classification, obtain that coarse grain is roughly selected cleaned coal and particulate is roughly selected cleaned coal;
B. coarse grain is roughly selected cleaned coal and send into TBS and disturb bed to carry out gravity separation, obtain gravity treatment tail coal and gravity treatment cleaned coal;
C. the gravity treatment cleaned coal is sent into the I dehydration equipment and dewater, obtain gravity treatment head coal product and backwater;
D. particulate is roughly selected cleaned coal and backwater and send into the II floatation equipment and carry out selected operation, obtain II floatation clean coal and II floating tail-coal;
E. the II floatation clean coal is sent into the II dehydration equipment and dewater, obtain the final election head coal product.
Described classifying equipoment adopts partition size to be 0.125mm or to be the classifying cyclone of 0.15mm or screen cloth cyclone.
Beneficial effect: the present invention utilizes flotation technology earlier the difficult separation coal mud of density thing content between senior middle school to be roughly selected operation; The thick cleaned coal of roughly selecting that will obtain then carries out classification; The thick cleaned coal of coarse grain utilizes TBS to disturb the bed gravity separation after the classification, and the thick cleaned coal of particulate is still handled with floatation.Because a large amount of high grey gangue minerals of jettisoning when roughly selecting, the thick cleaned coal mineral composition of coarse grain improves, and when adopting TBS to disturb the bed gravity separation, the thick cleaned coal of coarse grain can be according to the accurate sorting of density; And the fine grained in the thick cleaned coal utilizes further deliming upgrading of flotation technology.Solved owing to the high coal slime difficulty that causes of the intermediate density thing content thin cement content of high and high ash is selected problem, can improve clean coal recovery, practiced thrift cost simultaneously.The II floatation clean coal can obtain qualified recirculated water after II dehydration equipment processed.Compare with traditional handicraft; Solved the contradiction between the type slime separation product quality and the rate of recovery; With strong points, cost is low, technology is simple, small investment, power consumption is little, operating cost is low, the cleaned coal output capacity is high and do not destroy the granularmetric composition of head coal product, remarkable in economical benefits.
Description of drawings
Fig. 1 is a process chart of the present invention.
The specific embodiment:
Below in conjunction with accompanying drawing one embodiment of the present of invention are done further to describe:
The flotation combined sorting process of difficult separation coal mud gravity treatment of density thing content between senior middle school of the present invention,
A. be that the float coal mud of going into of 60~120g/L is sent into size mixing equipment at first, add collecting agent and foaming agent, the float coal mud of going into that adds collecting agent, foaming agent is sized mixing through size mixing equipment in existing routine techniques ratio with black water concentration;
B. the black water 1 that will size mixing is introduced the I floatation equipment and is roughly selected operation, obtains I floatation clean coal 2 and I floating tail-coal 3, and gained I floatation clean coal rate is 70%~90%;
C. I floatation clean coal 2 is sent into classifying equipoment to carrying out classification, classifying equipoment adopts partition size to be 0.125mm or be the classifying cyclone of 0.15mm or screen cloth cyclone, and classified sizing of equipment obtains that coarse grain is roughly selected cleaned coal 4 and particulate is roughly selected cleaned coal 5;
D. coarse grain is roughly selected cleaned coal 4 and send into TBS and disturb bed to carry out gravity separation, obtain gravity treatment tail coal 6 and gravity treatment cleaned coal 7;
E. gravity treatment cleaned coal 7 is sent into the I dehydration equipment that is made up of high frequency sieve and coal slime centrifuge and dewater, obtain gravity treatment head coal product 8 and backwater 9;
F. particulate is roughly selected cleaned coal 5 and send into the II floatation equipment with backwater 9 and carry out selected operation, obtain II floatation clean coal 10 and II floating tail-coal 11;
G. II floatation clean coal 10 is sent into the II dehydration equipment and dewater, filtrating is made recirculated water, the cleaned coal 12 after the dehydration of II dehydration equipment and be the head coal product of final election from the gravity treatment head coal product 8 of I dehydration equipment; From I dehydration equipment I floating tail-coal 3 that flows out and the II floating tail-coal 11 that the II floatation equipment flows plinth is final tail coal product.

Claims (2)

1.一种高中间密度物含量的难选煤泥重选浮选联合分选工艺,包括用调浆设备对添加捕收剂、起泡剂的入浮煤泥进行调浆;将调浆好的煤泥水(1)引入Ⅰ浮选设备进行粗选作业,得到Ⅰ浮选精煤(2)和Ⅰ浮选尾煤(3);其特征在于,还包括如下步骤: 1. A refractory coal slime gravity separation flotation combined separation process with high intermediate density content, including slurry mixing equipment for adding collectors and foaming agents to the floating coal slime; The coal slime water (1) is introduced into I flotation equipment for roughing operation to obtain I flotation clean coal (2) and I flotation tailing coal (3); it is characterized in that it also includes the following steps: a.将Ⅰ浮选精煤(2)送入分级设备对进行分级,得到粗粒粗选精煤(4)和细粒粗选精煤(5); a. Sending the I flotation clean coal (2) into the classification equipment to classify to obtain the coarse coarse clean coal (4) and the fine rough clean coal (5); b.将粗粒粗选精煤(4)送入TBS干扰床进行重力分选,得到重选尾煤(6)和重选精煤(7); b. sending the coarse-grained coarsely-selected clean coal (4) into the TBS interfering bed for gravity separation to obtain gravity-selected tailing coal (6) and heavy-selected clean coal (7); c.将重选精煤(7)送入Ⅰ脱水设备进行脱水,得到重选精煤产品(8)和筛下水(9); c. Send the gravity-selected clean coal (7) into I dehydration equipment for dehydration to obtain the gravity-selected clean coal product (8) and sieve water (9); d.将细粒粗选精煤(5)和筛下水(9)送入Ⅱ浮选设备进行精选作业,得到Ⅱ浮选精煤(10)和Ⅱ浮选尾煤(11); d. Sending the fine-grained coarsely-selected clean coal (5) and sieved water (9) to II flotation equipment for beneficiation operation to obtain II flotation clean coal (10) and II flotation tailing coal (11); e.将Ⅱ浮选精煤(10)送入Ⅱ脱水设备进行脱水,得到复选精煤产品(12)。 e. The II flotation clean coal (10) is sent to the II dehydration equipment for dehydration to obtain a re-selection clean coal product (12). 2.根据权利要求1所述的高中间密度物含量的难选煤泥重选浮选联合分选工艺,其特征在于:所述的分级设备采用分级粒度为0.125mm或为0.15mm的分级旋流器或筛网旋流器。 2. The refractory coal slime gravity separation flotation combined separation process with high intermediate density content according to claim 1, characterized in that: the classification equipment adopts a classification rotary with a classification granularity of 0.125mm or 0.15mm Cyclone or screen cyclone.
CN 201210235148 2012-07-09 2012-07-09 Combined separation process for gravity concentration and flotation of difficult separation coal slime with high intermediate density material content Expired - Fee Related CN102728455B (en)

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Cited By (11)

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Publication number Priority date Publication date Assignee Title
CN102962122A (en) * 2012-12-03 2013-03-13 中国矿业大学 Deep preparation technology of coal for direct coal liquefacation
CN103028486A (en) * 2012-12-21 2013-04-10 中国矿业大学 High and medium density coarse slime separation process
CN103212479A (en) * 2013-05-02 2013-07-24 杨高灵 Tail coal recycling utilization
CN103752414A (en) * 2014-01-07 2014-04-30 中国矿业大学(北京) Pulp mixing reinforced deep flotation technology process
CN104668108A (en) * 2014-12-29 2015-06-03 山东东山王楼煤矿有限公司 Flotation device and method for coal slime
CN104722390A (en) * 2015-03-02 2015-06-24 中国矿业大学 Coking middling coal dms-flotation combined separation process
CN104741211A (en) * 2015-03-02 2015-07-01 中国矿业大学 Grading size mixing and bulk flotation separation process
CN109731697A (en) * 2019-03-14 2019-05-10 中国矿业大学 A wide particle size flotation system and process
CN110201790A (en) * 2019-06-21 2019-09-06 中国矿业大学 A kind of the sorting recovery system and sorting recovery process of width grade coal slime
CN113210125A (en) * 2021-05-17 2021-08-06 鄂托克旗建元洗煤有限责任公司 Method and system for partial middling heavy medium rewashing
CN114643194A (en) * 2022-03-21 2022-06-21 河南天元煤业有限公司 Method for treating flotation concentrate by adopting fine screen

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Cited By (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102962122A (en) * 2012-12-03 2013-03-13 中国矿业大学 Deep preparation technology of coal for direct coal liquefacation
CN103028486A (en) * 2012-12-21 2013-04-10 中国矿业大学 High and medium density coarse slime separation process
CN103212479A (en) * 2013-05-02 2013-07-24 杨高灵 Tail coal recycling utilization
CN103212479B (en) * 2013-05-02 2015-09-09 杨高灵 Tail coal is recycled method
CN103752414A (en) * 2014-01-07 2014-04-30 中国矿业大学(北京) Pulp mixing reinforced deep flotation technology process
CN104668108A (en) * 2014-12-29 2015-06-03 山东东山王楼煤矿有限公司 Flotation device and method for coal slime
CN104722390A (en) * 2015-03-02 2015-06-24 中国矿业大学 Coking middling coal dms-flotation combined separation process
CN104741211A (en) * 2015-03-02 2015-07-01 中国矿业大学 Grading size mixing and bulk flotation separation process
CN109731697A (en) * 2019-03-14 2019-05-10 中国矿业大学 A wide particle size flotation system and process
CN110201790A (en) * 2019-06-21 2019-09-06 中国矿业大学 A kind of the sorting recovery system and sorting recovery process of width grade coal slime
CN113210125A (en) * 2021-05-17 2021-08-06 鄂托克旗建元洗煤有限责任公司 Method and system for partial middling heavy medium rewashing
CN114643194A (en) * 2022-03-21 2022-06-21 河南天元煤业有限公司 Method for treating flotation concentrate by adopting fine screen

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