CN1161366A - Coal compounding method for producing wet-milled metallurgical coke powder, and process for producing same - Google Patents

Coal compounding method for producing wet-milled metallurgical coke powder, and process for producing same Download PDF

Info

Publication number
CN1161366A
CN1161366A CN 96115717 CN96115717A CN1161366A CN 1161366 A CN1161366 A CN 1161366A CN 96115717 CN96115717 CN 96115717 CN 96115717 A CN96115717 A CN 96115717A CN 1161366 A CN1161366 A CN 1161366A
Authority
CN
China
Prior art keywords
coke powder
coke
wet
milling
coal
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.)
Granted
Application number
CN 96115717
Other languages
Chinese (zh)
Other versions
CN1078605C (en
Inventor
温燕明
赵广奎
徐新洲
刁询民
徐文胜
申亚飞
张大本
毛云节
卜庆福
常宇
王恩振
梁丽萍
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.)
Jinan Iron and Steel Group Co Ltd
Original Assignee
Jinan Iron and Steel Group 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 Jinan Iron and Steel Group Co Ltd filed Critical Jinan Iron and Steel Group Co Ltd
Priority to CN96115717A priority Critical patent/CN1078605C/en
Publication of CN1161366A publication Critical patent/CN1161366A/en
Application granted granted Critical
Publication of CN1078605C publication Critical patent/CN1078605C/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Abstract

A wet grinding fine coke coal blending method uses grain size equal to or less than 0.2 mm fine coke as inert additive, leanizing agent. After it is mixed with other coking coal, then fed into the carbonizing chamber of coke oven for coking, the weight of compounded wet grinding fine coke is equal to or less than 8%. The addition of wet grinding fine coke into the coking coal significantly increases the quantity of high volatile coal.

Description

The wet-milling coke powder blending method and the wet-milling coke powder technology thereof of refining metallurgical coke
The present invention relates to a kind of wet-milling coke powder blending method and wet-milling coke powder technology thereof of refining metallurgical coke.
At present, along with developing rapidly of Iron And Steel Industry, high-quality caking coal resource worsening shortages.For a long time, in order to utilize coal resources effectively and reasonably, how to obtain the measured metallurgical coke of matter be one of important topic of domestic and international metallurgy industry to the upgrading by mixed coal.Allocate coke powder into and improve the amount of allocating into of fat coal as leaning agent, increase the intensity of institute's coking charcoal, the blending method of producing the high-quality metallurgical coke is subjected to domestic and international coking worker's attention day by day.That more domestic medium and small coal chemical enterprises once carried out was higher at the coal blending fugitive constituent, its cohesiveness has again in certain coal charge more than needed and allocates inert material (high temperature coke powder, semicoke or petroleum coke powder, hard coal etc.) into, to slow down the string stress after semicoke generates, reduce the generation of crackle, improve the test of metallurgical coke quality and obtain certain effect, but its coke powder amount of allocating into generally is no more than 5%, coke fines size<0.5mm, and set up the dry and fine grinding workshop section of corresponding coke powder.Because dry grinding coke powder dust pollution serious problems are not resolved, to making more domestic medium and small coal chemical enterprises no longer adopt this kind dry grinding coke powder blending method and dry grinding coke powder technology thereof.Second phase nineteen ninety-five " external coking chemistry " discloses the coal blending technology and the dry grinding coke powder technology of coke-oven plant, German Sa Er area a kind of " join coke powder and make production metallurgy Jiao firm by ramming ", it adopts and makes side coal technology firm by ramming, the content of coke fines size<0.09mm reaches 65% in the mixed coal, the fat coal amount of allocating into can reach more than 70%, and the coke powder amount of allocating into is 8%.The characteristics of its coke powder drying and grinding technology are: one, the dry and grinding of coke powder is carried out in same equipment; Two, grinding and classification are to use by realizing in ball mill that is contained in closed-circuit system and the air classifier; Three, with pneumatic conveyer coke powder is delivered to dosing unit; Four, make flue gas or delivering gas enter atmosphere after bag filter equipment is collected the part coke powder through two chimneys; Five, coke powder is added in the beater grinder and carry out homogenizing with coal.This coke powder coal blending TAMPING COKING PROCESS has improved the amount of allocating into (can reach 70%) of fat coal and has improved the intensity of metallurgical coke that (M40 73% brings up to 76.4% by what do not join coke powder greatly, M10 is increased to 6.2% by 5.6%), the technical process advanced person in its drying and grinding coke powder workshop, good dedusting effect.But its existing technology is too complicated, drawbacks such as facility investment is more, unit consumption of energy height, and the practical situation present according to China can't be widely used in coal chemical enterprise.
The purpose of this invention is to provide a kind of wet-milling coke powder blending method and wet-milling coke powder technology thereof that can overcome the refining metallurgical coke of above-mentioned dry grinding coke powder weak point.
The object of the present invention is achieved like this: the wet-milling coke powder blending method and the wet-milling coke powder technology thereof of refining metallurgical coke, it is that wet-milling coke powder with coke powder particle diameter≤0.2mm is as inert additwe, leaning agent, with the laggard coke furnace carbonization chamber coking that is mixed of other coking coal, its wet-milling coke powder amount of allocating into≤8%.The raw material coke powder of coke powder particle diameter≤10mm by transfer roller input ball mill with pigment broken for the coke powder particle diameter be that the slip of 0.05-0.5mm is gone into kiln basin side by side, its weight ratio of going into to grind coke powder and water is 1/2-4/5, this slip is admitted to becomes water content≤20% after filter separates its moisture, the coke powder particle diameter is the finely-ground coke of 0.05-0.5mm, after finely-ground coke is handled by transfer roller input dosing vessel, send on the transfer roller that electronic scales is housed by the batching dish, then quantitatively sent in the beater grinder of coal blending chamber be mixed with other coking coal after, advance coke furnace carbonization chamber coking.
Advantage of the present invention: one, remarkable benefit, the wet-milling coke powder blending method of refining metallurgical coke substantially can be near the various technico-economical comparisones of external dry grinding coke powder coal-blending coking, its coke strenth M40 is increased to 75.6% by 74.9%, and M10 reduces to 8.12% by 8.37%; So coke quality obviously improves, under the prerequisite that guarantees coke quality, after allocating the wet-milling coke powder amount of allocating into≤8% into coking coal, the proportioning that makes its fat coal is increased to 50-70% by original 46%, the amount of allocating into of coking coal can be reduced to 15-20% by original 30-40% and medium fugitive constituent bonds by force, so saved the coking coal and the rich coal of domestic shortage greatly, and wet-milling coke powder coal-blending coking also can alleviate coal in the swelling pressure of molten state to furnace wall, prolongs its coke oven stove order; Two, comprehensive cost is low, adopts wet-milling coke powder technology to change the complicated technology of dry grinding coke powder, so facility investment is few, energy consumption is low, no dust pollution, its energy consumption only is 1/5 of an external equal scale dry grinding coke powder.Widespread use of the present invention can produce significant social, economic benefit.
Figure of description is a wet-milling coke powder process flow sheet of the present invention.
The present invention is described in further detail in conjunction with the embodiments below with reference to Figure of description.
The wet-milling coke powder blending method of refining metallurgical coke of the present invention and wet-milling coke powder technology thereof, it is that wet-milling coke powder with coke powder particle diameter≤0.2mm is as inert additwe, leaning agent, with the laggard coke furnace carbonization chamber coking that is mixed of other coking coal, its wet-milling coke powder amount of allocating into≤8%.The raw material coke powder of coke powder particle diameter≤10mm is by transfer roller
(1) input ball mill (2) with pigment broken for the coke powder particle diameter be that the slip of 0.05-0.5mm is gone into kiln basin (3) side by side, its weight ratio of going into to grind coke powder and water is 1/2-4/5, this slip is admitted to becomes water content≤20% after filter (4) separates its moisture, the coke powder particle diameter is the finely-ground coke of 0.05-0.5mm, after finely-ground coke is handled by transfer roller (7) input dosing vessel (8), send on the transfer roller (10) that electronic scales (11) are housed by batching dish (9), then quantitatively sent in the coal blending chamber beater grinder (12) be mixed with other coking coal after, advance coke furnace carbonization chamber coking.Water after slip separates through filter (4) enters settling bowl (6) by automatic draining device (5), and the water purification after sedimentation is handled is admitted to the ingress of ball mill (2) once more.Other technology, the equipment that uses that matches with the present invention is prior art, does not just give unnecessary details one by one here.

Claims (3)

1, a kind of wet-milling coke powder blending method and wet-milling coke powder technology thereof of refining metallurgical coke, it is characterized in that: with the wet-milling coke powder of coke powder particle diameter≤0.2mm as inert additwe, leaning agent, with the laggard coke furnace carbonization chamber coking that is mixed of other coking coal, its wet-milling coke powder amount of allocating into≤8%.
2, the wet-milling coke powder blending method of refining metallurgical coke according to claim 1 and wet-milling coke powder technology thereof, it is characterized in that: the raw material coke powder of coke powder particle diameter≤10mm by transfer roller (1) input ball mill (2) with pigment broken for the coke powder particle diameter be that the slip of 0.05-0.5mm is gone into kiln basin (3) side by side, its weight ratio of going into to grind coke powder and water is 1/2-4/5, this slip is admitted to becomes water content≤20% after filter (4) separates its moisture, the coke powder particle diameter is the finely-ground coke of 0.05--0.5mm, after finely-ground coke is handled by transfer roller (7) input dosing vessel (8), send on the transfer roller (10) that electronic scales (11) are housed by batching dish (9), then quantitatively sent in the coal blending chamber beater grinder (12) be mixed with other coking coal after, advance coke furnace carbonization chamber coking.
3, the wet-milling coke powder blending method of refining metallurgical coke according to claim 1 and 2 and wet-milling coke powder technology thereof, it is characterized in that: the water after slip separates through filter (4) enters settling bowl (6) by automatic draining device (5), and the water purification after sedimentation is handled is admitted to the ingress of ball mill (2) once more.
CN96115717A 1996-04-02 1996-04-02 Coal compounding method for producing wet-milled metallurgical coke powder, and process for producing same Expired - Fee Related CN1078605C (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN96115717A CN1078605C (en) 1996-04-02 1996-04-02 Coal compounding method for producing wet-milled metallurgical coke powder, and process for producing same

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN96115717A CN1078605C (en) 1996-04-02 1996-04-02 Coal compounding method for producing wet-milled metallurgical coke powder, and process for producing same

Publications (2)

Publication Number Publication Date
CN1161366A true CN1161366A (en) 1997-10-08
CN1078605C CN1078605C (en) 2002-01-30

Family

ID=5122943

Family Applications (1)

Application Number Title Priority Date Filing Date
CN96115717A Expired - Fee Related CN1078605C (en) 1996-04-02 1996-04-02 Coal compounding method for producing wet-milled metallurgical coke powder, and process for producing same

Country Status (1)

Country Link
CN (1) CN1078605C (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101705104B (en) * 2009-11-12 2012-08-22 重庆汉砧科技有限公司 Pulverized coal activator and coking coal prepared from same
CN101418221B (en) * 2007-10-23 2012-09-05 上海寰球石油化学工程有限公司 Remixing process of dry pulverized coke and wet pulverized coke of coke making raw material
CN103517965A (en) * 2011-05-11 2014-01-15 驰瑞莱股份公司 Closed coke slurry system and method for gaining sellable petroleum coke pieces out of solidified petroleum coke in a coke drum unit

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1049371A (en) * 1990-09-14 1991-02-20 陶国延 The adhering method of fluoroplastics and metal and binding agent

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101418221B (en) * 2007-10-23 2012-09-05 上海寰球石油化学工程有限公司 Remixing process of dry pulverized coke and wet pulverized coke of coke making raw material
CN101705104B (en) * 2009-11-12 2012-08-22 重庆汉砧科技有限公司 Pulverized coal activator and coking coal prepared from same
CN103517965A (en) * 2011-05-11 2014-01-15 驰瑞莱股份公司 Closed coke slurry system and method for gaining sellable petroleum coke pieces out of solidified petroleum coke in a coke drum unit
CN103517965B (en) * 2011-05-11 2015-09-23 驰瑞莱股份公司 For obtaining the closed coke slip system and method for the oil the sold coke button be made up of solidified petroleum Jiao in coke-drum unit

Also Published As

Publication number Publication date
CN1078605C (en) 2002-01-30

Similar Documents

Publication Publication Date Title
US4116679A (en) Metallized iron briquet
RU2353660C2 (en) Manufacturing method of briquettes with direct usage of coal with wide particle distribution by dimensions, method and facility with usage of this method
US4142941A (en) Method for producing blast furnace coke
CN111233422B (en) Concrete containing coal-to-liquid coarse slag and preparation method thereof
CN111717916B (en) Method and device for producing active calcium oxide as calcium carbide raw material by wet method calcium carbide slag
CN106755981A (en) A kind of method that utilization iron ore mine produces metallized pellet
RU2264435C2 (en) Coal briquettes for reductive melting process and a method for manufacture thereof
CN201589515U (en) Roasting reduction shaft furnace
CN106396729A (en) Method for preparing light ceramsite filter material by using coal slime
CN1537959A (en) Cold aggregated pellet ore for ironmaking in blast furnace and its preparation method
US7105114B2 (en) Briquetting of lime based products with carbon based additives
CN101225530B (en) Use of low-ash carbonaceous raw material in manufacture of pre-baked anode
CN1078605C (en) Coal compounding method for producing wet-milled metallurgical coke powder, and process for producing same
CN100515929C (en) Cinder processing method in acid preparing process from pyrite ore
CN101020960B (en) Pellet for smelting Al-Si alloy and its preparation method
RU2713143C1 (en) Carbonaceous reducing agent for production of technical silicon and method of its production
CN214495743U (en) Device of semi coke for preparation of calcium carbide raw materials
KR100298685B1 (en) Lump cokes used to Electric furnace or steel-making furnace
RU2151738C1 (en) Charge for production of silicon and method of preparing molding material for production of silicon
CN201128749Y (en) System for producing cold bonding block with steel making and steel rolling sludge
CN114921643B (en) Composite organic binder and preparation method and application thereof
US4158550A (en) Apparatus for producing blast furnace coal
CN1163620C (en) Technology and equipment for sphericizing powdered magnetic concentrate
RU2703084C1 (en) Method of producing technical silicon
RU2796955C2 (en) Briquetted mixture for smelting technical silicon

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
C14 Grant of patent or utility model
GR01 Patent grant
REG Reference to a national code

Ref country code: HK

Ref legal event code: GR

Ref document number: 1053660

Country of ref document: HK

C17 Cessation of patent right
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20020130