[go: up one dir, main page]
More Web Proxy on the site http://driver.im/

CN105772212B - A kind of moderate cohesive coal produces extraordinary white cement coal method - Google Patents

A kind of moderate cohesive coal produces extraordinary white cement coal method Download PDF

Info

Publication number
CN105772212B
CN105772212B CN201610262425.9A CN201610262425A CN105772212B CN 105772212 B CN105772212 B CN 105772212B CN 201610262425 A CN201610262425 A CN 201610262425A CN 105772212 B CN105772212 B CN 105772212B
Authority
CN
China
Prior art keywords
coal
white cement
ash
diameter
raw
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
CN201610262425.9A
Other languages
Chinese (zh)
Other versions
CN105772212A (en
Inventor
王大鹏
桂夏辉
曹亦俊
石磊
刁脐晨
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 CN201610262425.9A priority Critical patent/CN105772212B/en
Publication of CN105772212A publication Critical patent/CN105772212A/en
Application granted granted Critical
Publication of CN105772212B publication Critical patent/CN105772212B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B03SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
    • B03BSEPARATING SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS
    • B03B9/00General arrangement of separating plant, e.g. flow sheets
    • B03B9/005General arrangement of separating plant, e.g. flow sheets specially adapted for coal

Landscapes

  • Processing Of Solid Wastes (AREA)
  • Separation Of Solids By Using Liquids Or Pneumatic Power (AREA)
  • Solid Fuels And Fuel-Associated Substances (AREA)

Abstract

A kind of moderate cohesive coal produces extraordinary white cement coal method, used when selecting and produce suitable for coal, it is raw coal not walk using moderate cohesive coal, pass through the heavy magnetic process integration of the selected magnetic separation of jigging roughing hydrocyclone, iron-holder in ash content and raw coal is reduced, produces extraordinary ultra low-ash, low iron-holder white cement coal;To ensure extraordinary white cement coal iron content, assorting room is carried out in aqueous medium.The technological process of production is simple, and cost is low, is easy to promote, and sulphur coal can be used to be produced for the technique in addition, advantageously account for sulphur coal application problem.

Description

一种中等粘结性煤生产特种白水泥用煤方法A coal-use method for producing special white cement from medium caking coal

技术领域technical field

本技术涉及一种生产特种白水泥用煤方法,尤其适用于煤炭处理领域使用的一种中等粘结性煤生产特种白水泥用煤方法。The technology relates to a method of using coal for producing special white cement, and is especially suitable for a method of using coal for producing special white cement with medium caking coal used in the field of coal processing.

发明背景Background of the invention

白水泥由于强度高、水硬性好且能调成不同颜色,而广泛应用于建筑装饰工程,我国是至今为止用煤烧制白水泥的唯一国家。White cement is widely used in architectural decoration projects because of its high strength, good hydraulicity and the ability to adjust into different colors. my country is the only country that uses coal to burn white cement so far.

白水泥生产对燃料的要求:优先选择不产生灰分的重油、天然气或石油焦,如采用煤炭,应选择低灰分,特别是灰分中Fe2O3含量低的烟煤或炼焦用洗精煤,煤应满足:(以下是行业要求)Fuel requirements for white cement production: heavy oil, natural gas or petroleum coke that does not produce ash should be preferred. If coal is used, low ash should be selected, especially bituminous coal with low Fe 2 O 3 content in ash or clean coal for coking. Should meet: (the following are industry requirements)

挥发分25%~32%Volatile matter 25%~32%

灰分<12%Ash<12%

发热量>27200kJ/kgCalorific value>27200kJ/kg

灰分中的w(Fe2O3)<0.8%w(Fe 2 O 3 ) in ash<0.8%

目前没有使用中等粘结性煤生产特种白水泥用煤方法。At present, there is no method of using medium caking coal to produce special white cement.

发明内容Contents of the invention

针对现有技术的不足之处,提供一种步骤简单,生产稳定,效率高的中等粘结性煤生产特种白水泥用煤方法。Aiming at the deficiencies of the prior art, a coal-using method for producing special white cement from medium caking coal with simple steps, stable production and high efficiency is provided.

为实现上述技术目的,本发明的中等粘结性煤生产特种白水泥用煤方法,其步骤如下:In order to realize above-mentioned technical object, medium cohesive coal of the present invention produces special white cement coal method, and its steps are as follows:

a.利用50mm筛分设备将原煤经过预先筛分,将筛分出的直径小于50mm的筛下部分原煤给入孔径为1mm的脱泥筛,而筛上部分直径大于50mm的原煤则给入破碎机破碎后继续筛分;a. Use 50mm screening equipment to pre-screen the raw coal, feed the raw coal with a diameter of less than 50mm into the desliming screen with a diameter of 1mm, and feed the raw coal with a diameter greater than 50mm into the crushing screen Continue to sieve after crushing;

b.利用孔径为1mm的脱泥筛对直径小于50mm的原煤进行脱泥作业,获得直径小于1mm的筛下原煤产物,直径50-1mm的筛上原煤产物,脱泥筛筛上部分的直径50-1mm原煤产物给入跳汰机重选,重选后的精煤与筛下部分直径小于1mm的精煤给入进入煤泥桶准备进行粗煤泥处理环节;b. Use a desliming screen with an aperture of 1 mm to perform desliming operations on raw coal with a diameter of less than 50 mm, and obtain raw coal products under the sieve with a diameter of less than 1 mm, and raw coal products with a diameter of 50-1 mm on the sieve, and the diameter of the upper part of the desliming screen is 50 -1mm raw coal products are sent to the jig for gravity separation, and the clean coal after gravity separation and the clean coal with a diameter of less than 1mm under the screen are fed into the slime barrel to prepare for coarse slime treatment;

c.将直径50-1mm原煤产物给入跳汰机缓冲仓,利用跳汰机分选出矸石和高灰精煤,其中利用直线振动筛将矸石脱水后排出系统;c. Feed the raw coal products with a diameter of 50-1mm into the buffer bin of the jig machine, use the jig machine to separate the gangue and high-ash clean coal, and use the linear vibrating screen to dehydrate the gangue and discharge it out of the system;

d.针对进入煤泥桶的精煤进行加水调浆,调浆至浓度15%,利用泵送至水介质旋流器,在0.045-0.1Mpa入料压力下分选出超低灰精煤和尾煤,尾煤经固定筛-离心机脱水后与粗煤泥精煤混合成为最终低灰精煤产品;d. For the clean coal entering the slime tank, add water to adjust the slurry, adjust the slurry to a concentration of 15%, and use pumps to Water medium cyclone, under the feed pressure of 0.045-0.1Mpa, the ultra-low ash clean coal and tailing coal are separated, and the tail coal is dehydrated by a fixed sieve-centrifuge and mixed with coarse slime clean coal to become the final low ash clean coal product;

e.将超低灰精煤给入磁选设备,利用磁选设备对超低灰精煤进行除铁,并通过离心机脱水后得到磁选精矿作为含铁矿物部分被排出,尾矿通过离心机脱水得到最终特种白水泥用煤;e. Feed the ultra-low ash clean coal into the magnetic separation equipment, use the magnetic separation equipment to remove iron from the ultra-low ash clean coal, and dehydrate through the centrifuge to obtain the magnetic separation concentrate and discharge it as the iron-containing mineral part, tailings Dehydration by a centrifuge to obtain the final coal for special white cement;

f.将脱泥筛筛下原煤产物进入煤泥桶,经分级旋流器分级,底流进入粗煤泥分选机,粗煤泥精煤经离心机脱水后成为最终低灰精煤产品;f. Put the raw coal product under the desliming screen into the slime bucket, and then classify it through the grading cyclone. The underflow enters the coarse slime separator, and the coarse slime clean coal is dehydrated by the centrifuge to become the final low ash clean coal product;

g.利用煤泥分级旋流器溢流、各离心机离心液、矸石脱水筛下水通过浓缩—压滤作业得到煤泥。g. Using the overflow of the coal slime grading cyclone, the centrifugal liquid of each centrifuge, and the waste water from the gangue dehydration screen to obtain the coal slime through the operation of concentration-filtration.

采用跳汰机与水介质旋流器联合进行原煤降灰,分选介质为水;水介质旋流器精煤通过磁选降低铁含量;所述精煤所用的磁选设备是湿式粗粒强磁选机。A jig and a water medium cyclone are used to reduce the ash of the raw coal, and the separation medium is water; the clean coal of the water medium cyclone reduces the iron content through magnetic separation; the magnetic separation equipment used for the clean coal is a wet coarse-grained strong magnetic Choose machine.

有益效果:本方法采用两段降灰两段除铁方法:通过跳汰粗选-水介质旋流器精选两步降灰,通过重选-磁选联合两步除铁,采用全水介质重选方法和重、磁联合工艺有利于严格保证特种白水泥用煤的质量要求。生产工艺流程简单,成本低,便于推广。另外该工艺可使用高硫煤进行生产,有利于解决高硫煤应用问题。Beneficial effect: This method adopts two-stage ash reduction and two-stage iron removal methods: two-step ash reduction through jigging rough separation-water medium cyclone selection, two-step iron removal through gravity separation-magnetic separation, and full water medium gravity separation The method and combined gravity and magnetic process are beneficial to strictly guarantee the quality requirements of coal used in special white cement. The production process is simple, the cost is low, and the promotion is convenient. In addition, the process can use high-sulfur coal for production, which is beneficial to solve the problem of high-sulfur coal application.

发明附图invention drawings

图1是本发明的方法结构图。Fig. 1 is a method structural diagram of the present invention.

具体实施例specific embodiment

下面结合实例对本工艺进一步的详述:Below in conjunction with example this technology is further described in detail:

如图1所示,本发明的中等粘结性煤生产特种白水泥用煤方法,其步骤如下:As shown in Figure 1, medium cohesive coal of the present invention produces special white cement coal method, and its steps are as follows:

a.利用50mm筛分设备将原煤经过预先筛分,将筛分出的直径小于50mm的筛下部分原煤给入孔径为1mm的脱泥筛,而筛上部分直径大于50mm的原煤则给入破碎机破碎后继续筛分;a. Use 50mm screening equipment to pre-screen the raw coal, feed the raw coal with a diameter of less than 50mm into the desliming screen with a diameter of 1mm, and feed the raw coal with a diameter greater than 50mm into the crushing screen Continue to sieve after crushing;

b.利用孔径为1mm的脱泥筛对直径小于50mm的原煤进行脱泥作业,获得直径小于1mm的筛下原煤产物,直径50-1mm的筛上原煤产物,脱泥筛筛上部分的直径50-1mm原煤产物给入跳汰机重选,重选后的精煤与筛下部分直径小于1mm的精煤给入进入煤泥桶准备进行粗煤泥处理环节;b. Use a desliming screen with an aperture of 1 mm to perform desliming operations on raw coal with a diameter of less than 50 mm, and obtain raw coal products under the sieve with a diameter of less than 1 mm, and raw coal products with a diameter of 50-1 mm on the sieve, and the diameter of the upper part of the desliming screen is 50 -1mm raw coal products are sent to the jig for gravity separation, and the clean coal after gravity separation and the clean coal with a diameter of less than 1mm under the screen are fed into the slime barrel to prepare for coarse slime treatment;

c.将直径50-1mm原煤产物给入跳汰机缓冲仓,利用跳汰机分选出矸石和高灰精煤,其中利用直线振动筛将矸石脱水后排出系统;c. Feed the raw coal products with a diameter of 50-1mm into the buffer bin of the jig machine, use the jig machine to separate the gangue and high-ash clean coal, and use the linear vibrating screen to dehydrate the gangue and discharge it out of the system;

d.针对进入煤泥桶的精煤进行加水调浆,调浆至浓度15%,利用泵送至水介质旋流器,在0.045-0.1Mpa入料压力下分选出超低灰精煤和尾煤,尾煤经固定筛-离心机脱水后与粗煤泥精煤混合成为最终低灰精煤产品;d. For the clean coal entering the slime tank, add water to adjust the slurry, adjust the slurry to a concentration of 15%, and use pumps to Water medium cyclone, under the feed pressure of 0.045-0.1Mpa, the ultra-low ash clean coal and tailing coal are separated, and the tail coal is dehydrated by a fixed sieve-centrifuge and mixed with coarse slime clean coal to become the final low ash clean coal product;

e.将超低灰精煤给入磁选设备,利用磁选设备对超低灰精煤进行除铁,并通过离心机脱水后得到磁选精矿作为含铁矿物部分被排出,尾矿通过离心机脱水得到最终特种白水泥用煤;e. Feed the ultra-low ash clean coal into the magnetic separation equipment, use the magnetic separation equipment to remove iron from the ultra-low ash clean coal, and dehydrate through the centrifuge to obtain the magnetic separation concentrate and discharge it as the iron-containing mineral part, tailings Dehydration by a centrifuge to obtain the final coal for special white cement;

f.将脱泥筛筛下原煤产物进入煤泥桶,经分级旋流器分级,底流进入粗煤泥分选机,粗煤泥精煤经离心机脱水后成为最终低灰精煤产品;f. Put the raw coal product under the desliming screen into the slime bucket, and then classify it through the grading cyclone. The underflow enters the coarse slime separator, and the coarse slime clean coal is dehydrated by the centrifuge to become the final low ash clean coal product;

g.利用煤泥分级旋流器溢流、各离心机离心液、矸石脱水筛下水通过浓缩—压滤作业得到煤泥。g. Using the overflow of the coal slime grading cyclone, the centrifugal liquid of each centrifuge, and the waste water from the gangue dehydration screen to obtain the coal slime through the operation of concentration-filtration.

采用跳汰机与水介质旋流器联合进行原煤降灰,分选介质为水;水介质旋流器精煤通过磁选降低铁含量;所述精煤所用的磁选设备是湿式粗粒强磁选机。A jig and a water medium cyclone are used to reduce the ash of the raw coal, and the separation medium is water; the clean coal of the water medium cyclone reduces the iron content through magnetic separation; the magnetic separation equipment used for the clean coal is a wet coarse-grained strong magnetic Choose machine.

本方法包括两段降灰两段除铁从而生产超低灰、低含铁量煤的步骤:跳汰粗选-水介质旋流器精选两步降灰,重选-磁选联合两步除铁,具体是:The method includes two stages of ash reduction and two stages of iron removal to produce ultra-low ash and low iron content coal: jigging rough separation-water medium cyclone selection two-step ash reduction, gravity separation-magnetic separation combined two-step iron removal ,specifically is:

(1)通过跳汰粗选-水介质旋流器精选两步分选得出超低灰精煤,降灰、初步除铁均在水介质中进行,易于保证特种白水泥用煤铁含量。(1) Ultra-low ash clean coal is obtained through jigging rough separation-water medium cyclone selection two-step separation, ash reduction and preliminary iron removal are all carried out in water medium, which is easy to ensure the iron content of coal for special white cement.

(2)利用磁选进一步降低重选精煤含铁量,严格保证特种白水泥用煤的质量。(2) Use magnetic separation to further reduce the iron content of gravity-selected clean coal, and strictly ensure the quality of coal used for special white cement.

实施例一:Embodiment one:

利用山东地区的中等粘结性气煤通过跳汰粗选-水介质旋流器精选-强磁选的工艺生产出了特种白水泥用煤,满足了后续利用的要求,具体的来讲:Using medium cohesive gas coal in Shandong area to produce special white cement coal through the process of jigging rough separation-water medium cyclone selection-strong magnetic separation, which meets the requirements of subsequent utilization. Specifically:

将中等粘结性气煤(灰分34.23%,Fe2O3含量0.83%,粘结指数38.2,硫分4.19%)通过50mm圆振动筛筛分,+50mm经破碎后与筛下物混合,再经1mm脱泥筛得到50-1mm的所需原煤(产率91.25%,灰分30.53%)进入后续重选环节。50-1mm原煤进入跳汰机分选出高灰精煤和矸石。矸石经直线振动筛脱水后直接排出。高灰精煤(产率51.81%,灰分5.65%,Fe2O3含量0.52%)自流进入搅拌桶经泵送至水介质旋流器,在分选压力0.045-0.1Mpa条件下分选出超低灰精煤(产率36.54%,灰分1.68%,Fe2O3含量0.35%)。超低灰精煤流入缓冲桶泵送至湿式粗粒强磁选机,磁选尾矿经离心机脱水后得到特种白水泥用煤(产率35.89%,灰分1.63%,Fe2O3含量0.20%,粘结指数96.6);磁选精矿经离心机脱水后作为含铁矿物排出。Sieve medium caking gas coal (ash content 34.23%, Fe 2 O 3 content 0.83%, caking index 38.2, sulfur content 4.19%) through a 50mm circular vibrating sieve. The required raw coal (yield 91.25%, ash content 30.53%) obtained by 1mm desliming screen is 50-1mm, and enters the subsequent gravity separation process. 50-1mm raw coal enters the jig to separate high-ash clean coal and gangue. The gangue is directly discharged after being dehydrated by the linear vibrating screen. High ash clean coal (yield 51.81%, ash content 5.65%, Fe 2 O 3 content 0.52%) flows into the mixing tank and is pumped to The water medium cyclone is used to separate ultra-low ash clean coal (yield 36.54%, ash content 1.68%, Fe 2 O 3 content 0.35%) under the condition of separation pressure 0.045-0.1Mpa. The ultra-low ash clean coal flows into the buffer tank and is pumped to the wet coarse-grained strong magnetic separator. The magnetic separation tailings are dehydrated by the centrifuge to obtain special white cement coal (yield 35.89%, ash content 1.63%, Fe 2 O 3 content 0.20 %, caking index 96.6); the magnetically separated concentrate is dehydrated by a centrifuge and discharged as iron-containing minerals.

Claims (4)

1. a kind of method that moderate cohesive coal produces extraordinary white cement coal, it is characterised in that step is as follows:
A. raw coal is passed through into prescreening using 50mm screening plants, divides lower part of screen of the diameter screened out less than 50mm to raw coal Feed aperture and be 1mm desliming screen, and sieve after raw coal of the upper part diameter more than 50mm then feeds crusher in crushing and continue to sieve;
B. desliming operation is carried out to raw coal of the diameter less than 50mm using the desliming screen that aperture is 1mm, obtains diameter less than 1mm's The lower raw coal product of sieve, raw coal product on diameter 50-1mm sieve, the diameter 50-1mm raw coal products of desliming screen sieve upper part are fed Jigging machine gravity treatment, the cleaned coal that lower part of screen divides diameter to be less than 1mm feed coal slime bucket and are ready for handling;
C. diameter 50-1mm raw coal products are fed into jigging machine surge bunker, spoil and high grey cleaned coal is sub-elected using jigging machine, its Discharge system after spoil is dehydrated by middle utilization linear vibrating screen;
D. it is directed to the high grey cleaned coal sub-elected into the jigging machine of coal slime bucket to carry out adding water to size mixing, sizes mixing to concentration 15%, utilize Hydrocyclone is pumped to, ultra low-ash cleaned coal and tail coal are sub-elected under 0.045-0.1Mpa feed pressures, tail coal is through fixation Final low ash extract coal product is mixed into after sieve-centrifuge dewatering with coarse slime cleaned coal;
E. ultra low-ash cleaned coal is fed into magnetic plant, iron removaling is carried out to ultra low-ash cleaned coal using magnetic plant, and pass through centrifuge Obtain magnetic concentrate after dehydration to be discharged as iron-bearing mineral part, mine tailing obtains final extraordinary white cement by centrifuge dewatering Use coal;
F. desliming screen is sieved into lower raw coal product and enters coal slime bucket, be classified through classifying cyclone, underflow enters separation of coarse slime machine, slightly Coal slime cleaned coal turns into final low ash extract coal product after centrifuge dewatering;
G. concentration-press filtration operation is passed through using the overflow of coal slime classifying cyclone, each centrifuge liquid, spoil dehydration backwater Obtain coal slime.
2. moderate cohesive coal according to claim 1 produces extraordinary white cement coal method, it is characterised in that:Using jump Eliminate machine and combine progress raw coal drop ash with hydrocyclone, separating medium is water.
3. moderate cohesive coal according to claim 1 produces extraordinary white cement coal method, it is characterised in that:Aqueous medium Cyclone cleaned coal reduces iron content by magnetic separation.
4. moderate cohesive coal according to claim 1 produces extraordinary white cement coal method, it is characterised in that:The essence Magnetic plant used in coal is wet type coarse grain intensity magnetic separator.
CN201610262425.9A 2016-04-25 2016-04-25 A kind of moderate cohesive coal produces extraordinary white cement coal method Active CN105772212B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201610262425.9A CN105772212B (en) 2016-04-25 2016-04-25 A kind of moderate cohesive coal produces extraordinary white cement coal method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201610262425.9A CN105772212B (en) 2016-04-25 2016-04-25 A kind of moderate cohesive coal produces extraordinary white cement coal method

Publications (2)

Publication Number Publication Date
CN105772212A CN105772212A (en) 2016-07-20
CN105772212B true CN105772212B (en) 2018-01-19

Family

ID=56399480

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201610262425.9A Active CN105772212B (en) 2016-04-25 2016-04-25 A kind of moderate cohesive coal produces extraordinary white cement coal method

Country Status (1)

Country Link
CN (1) CN105772212B (en)

Families Citing this family (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107008565A (en) * 2017-05-09 2017-08-04 神华包头能源有限责任公司 A kind of thermal coal deep screening and dense medium separation technique
CN109821648B (en) * 2019-01-03 2021-06-11 恩迈特(青岛)新能源科技有限公司 Re-selection system of medium coal pressure-free three-product dense medium cyclone of jigging
CN109701732B (en) * 2019-01-14 2020-09-08 乌拉特中旗毅腾矿业有限责任公司 Clean utilization production method of clean coal
CN109794349B (en) * 2019-03-08 2020-03-17 中国矿业大学 Underground coal dressing process
CN111420798A (en) * 2020-04-10 2020-07-17 山东博选矿物资源技术开发有限公司 System and process for recycling overflow clean coal slime of graded cyclone group
CN113731620A (en) * 2021-08-10 2021-12-03 新疆宝明矿业有限公司 Medium recovery method and medium recovery system

Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3579442A (en) * 1970-07-09 1971-05-18 Bird Machine Co Coal converting process
DE2906630A1 (en) * 1979-02-21 1980-09-04 Kloeckner Humboldt Deutz Ag Slurry filtered dewatering system - using coarse grains sepd. by centrifuging as filter cake for fine ones
CN1061949A (en) * 1991-08-30 1992-06-17 宁夏回族自治区建筑材料研究所 Adopt flyash to produce the method for white cement
CN1883812A (en) * 2006-07-08 2006-12-27 枣庄矿业(集团)有限责任公司 Raw coal sorting process
CN101716552A (en) * 2009-12-28 2010-06-02 河南理工大学 Raw coal washing process capable of realizing non-polar ash conditioning
CN104549710A (en) * 2014-12-26 2015-04-29 中国矿业大学 Three-stage opening compounding separation process and three-stage opening compounding separation system for coarse slime
CN105126991A (en) * 2015-07-23 2015-12-09 金易通科技(北京)股份有限公司 Main washing technology of coal

Patent Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3579442A (en) * 1970-07-09 1971-05-18 Bird Machine Co Coal converting process
DE2906630A1 (en) * 1979-02-21 1980-09-04 Kloeckner Humboldt Deutz Ag Slurry filtered dewatering system - using coarse grains sepd. by centrifuging as filter cake for fine ones
CN1061949A (en) * 1991-08-30 1992-06-17 宁夏回族自治区建筑材料研究所 Adopt flyash to produce the method for white cement
CN1883812A (en) * 2006-07-08 2006-12-27 枣庄矿业(集团)有限责任公司 Raw coal sorting process
CN101716552A (en) * 2009-12-28 2010-06-02 河南理工大学 Raw coal washing process capable of realizing non-polar ash conditioning
CN104549710A (en) * 2014-12-26 2015-04-29 中国矿业大学 Three-stage opening compounding separation process and three-stage opening compounding separation system for coarse slime
CN105126991A (en) * 2015-07-23 2015-12-09 金易通科技(北京)股份有限公司 Main washing technology of coal

Also Published As

Publication number Publication date
CN105772212A (en) 2016-07-20

Similar Documents

Publication Publication Date Title
CN105772212B (en) A kind of moderate cohesive coal produces extraordinary white cement coal method
CN103464272B (en) A kind of coarse slime two sections of water Jie method for separating
CN102211054B (en) Process for sorting coarse coal slime by utilizing heavy medium liquid-solid fluidized bed
CN103240168B (en) Grading separation and dehydration method for high-ash difficult-separation coal slime
CN104722389B (en) Coal dissociation-is independently sized mixing-bulk flotation technique in a kind of particulate
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
WO2020181618A1 (en) Underground coal preparation process
CN103831164B (en) In a kind of coking, coal heavily floats combined sorting technique
CN102430481B (en) Sorting process for high-ash and difficult-separation coal slime
CN104549710B (en) A kind of three sections of open circuit compounding separation techniques of coarse slime and system
RU2498860C1 (en) Plant for slurry coal concentration in helical separators (versions)
CN104826727B (en) Coal Multistage ore-grinding floatation process and system in a kind of particulate
WO2015123798A1 (en) Comprehensive recovery method for gold flotation tailings and device therefor
CN105797831B (en) Technique is selected in the dissociation of coal again in a kind of coking end
CN104815748B (en) The broken mill floatation process of two sections of coal in a kind of coking
CN102847606A (en) Coarse slime separation process
CN110523524B (en) Simplified sorting process for full-grade sorting of anthracite
CN113976306A (en) Pre-waste-throwing system and process for complex refractory low-grade molybdenum ore heavy-medium beneficiation
CN103920582B (en) A kind of closed circuit grading technology being applicable to Bed for Fine Coal classification
CN103831163A (en) Pre-separation process of coal slime flotation
CN105642431B (en) Method for gravity separation of sulfur concentrate from sulfur-containing coal gangue
CN107020200B (en) Blending process of flotation clean coal in full-grain clean coal
CN107008566A (en) A kind of steam coal separation technique
CN108855579B (en) Coal dressing method by using aqueous medium cyclone

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