CN104694145B - The coke and coking process of a kind of adapted Indonesia bottle coal - Google Patents

The coke and coking process of a kind of adapted Indonesia bottle coal Download PDF

Info

Publication number
CN104694145B
CN104694145B CN201310649633.0A CN201310649633A CN104694145B CN 104694145 B CN104694145 B CN 104694145B CN 201310649633 A CN201310649633 A CN 201310649633A CN 104694145 B CN104694145 B CN 104694145B
Authority
CN
China
Prior art keywords
coal
coking
indonesia
bottle
coke
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
CN201310649633.0A
Other languages
Chinese (zh)
Other versions
CN104694145A (en
Inventor
任学延
张文成
顾建
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.)
Shanghai Meishan Iron and Steel Co Ltd
Original Assignee
Shanghai Meishan Iron and Steel 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 Shanghai Meishan Iron and Steel Co Ltd filed Critical Shanghai Meishan Iron and Steel Co Ltd
Priority to CN201310649633.0A priority Critical patent/CN104694145B/en
Publication of CN104694145A publication Critical patent/CN104694145A/en
Application granted granted Critical
Publication of CN104694145B publication Critical patent/CN104694145B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10BDESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
    • C10B57/00Other carbonising or coking processes; Features of destructive distillation processes in general
    • C10B57/04Other carbonising or coking processes; Features of destructive distillation processes in general using charges of special composition

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Organic Chemistry (AREA)
  • Coke Industry (AREA)

Abstract

The invention discloses the coke and coking process of a kind of adapted Indonesia bottle coal, the volatile matter height, caking property height, degree of metamorphism for mainly solving Indonesia's bottle coal in the prior art are low, it is poor with the amalgamation of other coking coals, it is difficult to the technical issues of high-quality smelter coke of stable quality is produced for coal-blending coking.The technical scheme is that:A kind of coke of adapted Indonesia bottle coal is formed by following mass percent coal blending mixed coking:1/3 coking coal 10%~15%, Indonesia's bottle coal 5%~10%, bottle coal 15%~20%, rich coal 20%~25%, coking coal 30%~40%, lean coal 4%~8%.The present invention proposes corresponding Con trolling index according to the characteristics of Indonesia's bottle coal, i.e., with components of coal ash and substitutes coal so that when participating in coal-blending coking production using this Indonesia's bottle coal resource, ensure that the stabilization of coke quality.

Description

The coke and coking process of a kind of adapted Indonesia bottle coal
Technical field
The present invention relates to a kind of coke and coking process, the coke of more particularly to a kind of adapted Indonesia bottle coal and coking side Method belongs to technical field of coal chemical industry.
Background technology
In Coking Coal Blending Technology, the selection of coal is a key technology.The height of coal selection technique level is not only It decides the height of coke quality, also determines the height of the coal blending cost on the basis of coke quality is ensured.
In recent years, with the expansion of Chinese coking production capacity, the contradiction of high-quality caking coal shortage of resources is also outstanding day by day, especially It is that high-quality coking coal is more nervous as the important coal supply of coke making and coal blending, becomes one of focus of each coal chemical enterprise contention.Respectively Coal chemical enterprise has to seek new resource in foreign countries, since the coking coal condition of coal formation of various regions is different, although volatile matter and viscous The characteristics of knot performance indicator meets the criteria for classification of China coking coal, but its coking characteristic and geological characteristics etc. have itself, This brings difficulty to the application of these import coals.
The degree of metamorphism of Indonesia's bottle coal is relatively low, and China import Indonesia bottle coal mostly uses, and have correlation as thermal coal Document disclose, and to being used for coal-blending coking, applicant has no relevant report.
Document《Coal-burning power plant's coal mixing combustion experimental study》(Hubei Electric Power, 2011(5))A kind of Indonesia is described in one text Burning of coal characteristic, by the control in relation to operating parameter to ensure the safe operation of boiler and pulverized coal preparation system.
Document《Boiler, which changes, burns Indonesia coal examination burning and Economic and Efficiency Analysis》(BJ Power High Level Training School's journal:It is natural Science version, 2012(7))A kind of Indonesia's coal resources are described in one text, resource reserve is 58,000,000,000 tons, proven reserve 19,300,000,000 Ton.In today that the energy is increasingly in short supply, the exploitation of Indonesia coal seems very there is realistic meaning.To find new coal source and reduction The operation cost of power plant has carried out combustion test, and achieve success to Indonesia coal.
Experimental study and production application have been carried out to Indonesia's bottle coal in above-mentioned document, have been mainly used in boiler combustion field, It is not applied to coal-blending coking technical field.The main reason is that the degree of metamorphism of Indonesia's bottle coal is low, volatile matter is high, to a certain degree On can cause the decline of coke quality.
A kind of volatile matter of Indonesia's bottle coal is between 39%~41%, maximum vitrinite reflectance 0.55%~0.65%;Bonding refers to Number G is more than 85~90, maximum thick ness of plastic layer Y16~20mm.The coal belongs to bottle coal QM45 by CHINESE COAL classification, but it volatilizees It is point high and caking property is also high, different from domestic common bottle coal.
In addition, due to its volatile matter height, degree of metamorphism is low, poor with the amalgamation of other coking coals, exists to Indonesia's bottle coal The production application of coal-blending coking brings difficulty.
Invention content
The object of the present invention is to provide the coke and coking process of a kind of adapted Indonesia bottle coal, mainly solve in the prior art The volatile matter of Indonesia's bottle coal is high, caking property is high, degree of metamorphism is low, poor with the amalgamation of other coking coals, it is difficult to be refined for coal blending Coke produces the technical issues of high-quality smelter coke of stable quality.So that after adding in Indonesia's bottle coal in coal blending raw material, meet It under conditions of certain coal blending quality requirement, can ensure that the quality of coal blending reaches high-quality coking coal index, can be given birth on the dress coke oven of top The high-quality smelter coke that output quality is stablized.
The technical solution adopted by the present invention is:
A kind of coke of adapted Indonesia bottle coal is formed by following mass percent coal blending mixed coking:1/3 coking coal 10%~ 15%, Indonesia's bottle coal 5%~10%, bottle coal 15%~20%, rich coal 20%~25%, coking coal 30%~40%, lean coal 4%~8%.
A kind of coking process of adapted Indonesia bottle coal, includes the following steps:
A, by following mass percent coal blending, 1/3 coking coal 10%~15%, Indonesia coal 5%~10%, bottle coal 15%~20%, fertilizer Coal 20%~25%, coking coal 30%~40%, lean coal 4%~8%;
B, Mixture Density Networks crush, and the Mixture Density Networks after coal blending in step a are crushed, and Mixture Density Networks of the grain size less than 3mm is preferably made to account for it The 75%~80% of gross mass;
Broken Mixture Density Networks are sent into top dress coking by coke oven by c, coal-blending coking, and coking temperature is 1000 ± 50 DEG C, knot The burnt time is 20 ± 2 hours;
D, it discharges of the coke postcooling.
Coke quality detection is carried out later, measures the fingers such as coke ash, sulfur content in coke, coke reactivity and post reaction strength Mark.
Further, the postcooling of the discharging of the coke described in step d of the present invention cools down coke using nitrogen(Also known as dry coke quenching cools down), With the coke of nitrogen cooling red heat, the moisture of coke can be not only reduced, but also the variation of coke chilling can be reduced, avoid coke The decline of charcoal intensity.It can be recycled for heat power generation etc., so as to avoid energy waste with the nitrogen after coke heat exchange.
The Coal Characteristics of Indonesia's bottle coal of institute's adapted are as follows in the present invention:Volatilization is divided into 39%~41%, and maximum vitrinite is anti- Penetrate rate 0.55%~0.65%;Adhesive index is more than 85~90, maximum thick ness of plastic layer Y16~20mm.
The classification that the coal quality of above-mentioned other various single coking coals used meets in corresponding chinese national standard refers to Mark.
Above-mentioned coal blending certain mass requires to refer to that the adhesive index value of Mixture Density Networks after coal blending is 75~85, and gelatinous layer is maximum 14~17mm of thickness.
The requirement of above-mentioned coal blending quality is derived from the mass property research to Indonesia's bottle coal.Indonesia's bottle coal is found by research Volatile matter be up to 39%~41%, but maximum vitrinite reflectance is 0.55%~0.65%, is remained at low levels, from reflectivity It sees that a part strides into the range of jet coal and bottle coal on distribution map, therefore proposes that the coal replaces part bottle coal and jet coal, with Reduce the influence to coal blending quality.
After experiment shows above-mentioned technical proposal using the present invention, the not only macro-indicators adhesive index of mixed coal(Table Levy the bonding itself of coking coal and the ability of inert material)75 can be more than, maximum thickness of colloidal matter layer Y(Characterize the coking of coking coal Gel quantity is generated in the process)14mm can be more than;The drum strength DI of coke completely can be more than 85%, after coke gasification reaction Intensity(CSR)65% can be more than, therefore disclosure satisfy that 3000m3And the needs of Yi Shang blast furnace process.
The present invention has following good effect compared with prior art:
1st, coking coal resource is expanded, reduces coal blending production cost.Break what Indonesia's bottle coal was used as thermal coal Indonesia's bottle coal is replaced part part bottle coal and jet coal to be applied to coal-blending coking, expands the range of coking coal by conventional thought, Resource is made to obtain Optimum utilization;The market price of Indonesia's bottle coal is generally relatively low, therefore reduces coal blending by the adapted of Indonesia coal Production cost.
2nd, coke quality is maintained.The present invention breaks through limitation of traditional national standard classification by coking coal application method coking, according to The characteristics of Indonesia coal, proposes corresponding Con trolling index, by maintaining the matter of coke to matching components of coal ash and substituting the control of coal Amount, ensure that coke meets the needs of blast furnace ironmaking.
3rd, the coke making and coal blending method of adapted Indonesia provided by the invention bottle coal, in the coke energy of common top dress coke oven production Reach high-quality smelter coke quality requirement.
Specific embodiment
A kind of coke of adapted Indonesia of the invention bottle coal, is formed by following mass percent coal blending mixed coking:1/3 coking coal 10%~15%, Indonesia coal 5%~10%, bottle coal 15%~20%, rich coal 20%~25%, coking coal 30%~40%, lean coal 4%~8%.Specifically Proportioning is shown in Table 1, and table 1 is specific embodiment, 1 non-adapted Indonesia bottle coal of scheme, 2 Indonesia's bottle coal proportioning 5% of scheme, 3 Indonesia's gas of scheme Coal proportioning 8%, 4 Indonesia's bottle coal proportioning 10% of scheme.
A kind of coking process of adapted Indonesia bottle coal, includes the following steps:
A, by following mass percent coal blending, 1/3 coking coal 10%~15%, Indonesia's bottle coal 5%~10%, bottle coal 15%~20%, Rich coal 20%~25%, coking coal 30%~40%, lean coal 4%~8%;
B, Mixture Density Networks crush, and the belt of the Mixture Density Networks in step a is sent into crusher in crushing, makes grain size mixed less than 3mm It closes coal and accounts for the 75%~80% of its gross mass;
C, coal-blending coking, by broken Mixture Density Networks be sent into top dress coking by coke oven, coke furnace carbonization chamber height be 6m, coking Temperature is 1000 DEG C, coking time 20h;
D, it is cooled down after the discharging of the coke with nitrogen(Also known as dry coke quenching cools down)Coke.
Coke quality detection is carried out later, measures the fingers such as coke ash, sulfur content in coke, coke reactivity and post reaction strength Mark, measurement result are shown in Table 1.
The embodiment of the present invention pushes up charging coke coking using 6m, carries out coal blending with Indonesia's bottle coal, coal blending dry ash free basis is waved Hair point (Vd) is 27~30%, and caking index is 75~85, and in the prior art with 1/3 coking coal, bottle coal, rich coal, coking coal and thin Five class coal cokings of coal, obtain the coke for having quality essentially identical, post reaction strength of coke(CSR)It is 65%~70%.
1 coke making and coal blending of table(Mass percent)And coke quality tables of data
Scheme 2 to 4 measurement result of scheme can be seen that adapted Indonesia bottle coal substitution part bottle coal and long flame from upper table 1 After coal, each qualitative data of obtained coke and the data of the measurement of scheme 1 without adapted Indonesia bottle coal are essentially identical, completely may be used To meet 3000m3And the needs of Yi Shang blast furnace process.
It is summed up, the present embodiment has the advantages that:
1st, coking coal resource is expanded.The conventional thought that Indonesia's bottle coal is used as coking coal is broken, Indonesia coal has been replaced Part jet coal and bottle coal are applied to coal-blending coking, expand the range of coking coal, resource is made to obtain Optimum utilization.
2nd, coke quality is maintained.The Coal Blending Technology that Indonesia's bottle coal participates in passes through to maintaining coke to the control of coal blending quality The quality of charcoal ensure that coke meets the needs of blast furnace ironmaking.
3rd, coal blending cost is reduced.The price of Indonesia's bottle coal is reduced less than similar Chinese Domestic Coal by coal-blending coking Production cost.
In addition to the implementation, the present invention can also have other embodiment.It is all to use equivalent substitution or equivalent transformation shape Into technical solution, all fall within the present invention claims protection domain.

Claims (5)

1. a kind of coke of adapted Indonesia bottle coal, it is characterized in that being formed by following mass percent coal blending mixed coking:1/3 coking coal 10%~15%, Indonesia's bottle coal 5%~10%, bottle coal 15%~20%, rich coal 20%~25%, coking coal 30%~40% is thin Coal 4%~8%;The volatilization of Indonesia's bottle coal is divided into 39%~41%, and maximum vitrinite reflectance 0.55%~0.65% is glued It ties index G and is more than 85~90, maximum thick ness of plastic layer Y16~20mm.
2. the coke of adapted Indonesia as described in claim 1 bottle coal, it is characterized in that, Mixture Density Networks need to be through broken after coal blending, grain size The Mixture Density Networks of below 3mm account for the 75%~80% of its gross mass.
3. a kind of coking process of adapted Indonesia bottle coal, it is characterized in that including the following steps:
A, by following mass percent coal blending, 1/3 coking coal 10%~15%, Indonesia's bottle coal 5%~10%, bottle coal 15%~ 20%, rich coal 20%~25%, coking coal 30%~40%, lean coal 4%~8%;The volatilization of Indonesia's bottle coal is divided into 39%~ 41%, maximum vitrinite reflectance 0.55%~0.65%, adhesive index be more than 85~90, maximum thick ness of plastic layer Y16~ 20mm;
B, Mixture Density Networks crush, and the Mixture Density Networks after coal blending in step a are crushed;
Broken Mixture Density Networks are sent into top dress coking by coke oven by c, coal-blending coking, and coking temperature is 1000 ± 50 DEG C, coking time It is 20 ± 2 hours;
D, it discharges of the coke postcooling.
4. a kind of coking process of adapted Indonesia as claimed in claim 3 bottle coal, it is characterized in that, in the step a, after coal blending Mixture Density Networks adhesive index value is 75~85,14~17mm of maximum thick ness of plastic layer.
5. a kind of coking process of adapted Indonesia as claimed in claim 3 bottle coal, it is characterized in that, in the step b, Mixture Density Networks After broken, the Mixture Density Networks of below grain size 3mm account for the 75%~80% of its gross mass.
CN201310649633.0A 2013-12-06 2013-12-06 The coke and coking process of a kind of adapted Indonesia bottle coal Active CN104694145B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201310649633.0A CN104694145B (en) 2013-12-06 2013-12-06 The coke and coking process of a kind of adapted Indonesia bottle coal

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201310649633.0A CN104694145B (en) 2013-12-06 2013-12-06 The coke and coking process of a kind of adapted Indonesia bottle coal

Publications (2)

Publication Number Publication Date
CN104694145A CN104694145A (en) 2015-06-10
CN104694145B true CN104694145B (en) 2018-06-26

Family

ID=53341711

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201310649633.0A Active CN104694145B (en) 2013-12-06 2013-12-06 The coke and coking process of a kind of adapted Indonesia bottle coal

Country Status (1)

Country Link
CN (1) CN104694145B (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN113637496A (en) * 2020-04-27 2021-11-12 宝山钢铁股份有限公司 Microwave heating-based coking method
CN115141665A (en) * 2021-03-29 2022-10-04 上海梅山钢铁股份有限公司 Coke for matching Australian gas coal and coking method

Citations (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101081989A (en) * 2007-06-29 2007-12-05 武汉钢铁(集团)公司 Coal coking blending method
CN101942315A (en) * 2010-08-16 2011-01-12 中国神华能源股份有限公司 High-proportion coal blending and coking method
CN102260510A (en) * 2010-05-26 2011-11-30 上海梅山钢铁股份有限公司 Coke by adding long flame coal and coking method
CN102424758A (en) * 2011-10-17 2012-04-25 开滦(集团)有限责任公司 Multi-index blended coal coking method
CN102453490A (en) * 2010-10-22 2012-05-16 宝山钢铁股份有限公司 Coal blending method for preparing high-activity high-strength coke
CN102533299A (en) * 2011-12-15 2012-07-04 武汉钢铁(集团)公司 Russian fat coal participant coking and coal blending method
CN102559227A (en) * 2010-12-10 2012-07-11 上海梅山钢铁股份有限公司 Method for coal blending coking through utilizing Gieseler fluidity index
CN102604659A (en) * 2012-04-18 2012-07-25 武汉钢铁(集团)公司 Coking coal blending method using high-expansion coking coal
CN102994129A (en) * 2012-12-03 2013-03-27 广东韶钢松山股份有限公司 Gas coal blended coking blending coal and preparation method thereof

Patent Citations (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101081989A (en) * 2007-06-29 2007-12-05 武汉钢铁(集团)公司 Coal coking blending method
CN102260510A (en) * 2010-05-26 2011-11-30 上海梅山钢铁股份有限公司 Coke by adding long flame coal and coking method
CN101942315A (en) * 2010-08-16 2011-01-12 中国神华能源股份有限公司 High-proportion coal blending and coking method
CN102453490A (en) * 2010-10-22 2012-05-16 宝山钢铁股份有限公司 Coal blending method for preparing high-activity high-strength coke
CN102559227A (en) * 2010-12-10 2012-07-11 上海梅山钢铁股份有限公司 Method for coal blending coking through utilizing Gieseler fluidity index
CN102424758A (en) * 2011-10-17 2012-04-25 开滦(集团)有限责任公司 Multi-index blended coal coking method
CN102533299A (en) * 2011-12-15 2012-07-04 武汉钢铁(集团)公司 Russian fat coal participant coking and coal blending method
CN102604659A (en) * 2012-04-18 2012-07-25 武汉钢铁(集团)公司 Coking coal blending method using high-expansion coking coal
CN102994129A (en) * 2012-12-03 2013-03-27 广东韶钢松山股份有限公司 Gas coal blended coking blending coal and preparation method thereof

Also Published As

Publication number Publication date
CN104694145A (en) 2015-06-10

Similar Documents

Publication Publication Date Title
CN104232131B (en) The coke of a kind of adapted Canada coking coal and coking process
CN101942315B (en) High-proportion coal blending and coking method
CN102031172B (en) Low-cost high-strength coke and coke refining method thereof
CN110746997B (en) Method for refining metallurgical coke
CN112980482B (en) Method for coking with American coking coal participating in coal blending
CN101870875B (en) Method for producing metallurgical coke from 1/3 coking coal and non-coking coal
CN103710037A (en) Fluidized-bed low-rank coal upgrading utilization system and method
CN104194816B (en) A kind of method preparing coke
CN107267183A (en) A kind of method of coke making and coal blending
CN104694145B (en) The coke and coking process of a kind of adapted Indonesia bottle coal
CN105219412A (en) A kind of coke of adapted Australian coking coal and coking process
CN107541229B (en) Coke prepared by blending ultrahigh-sulfur coking coal and coking method
CN101250418A (en) Gasification, dry distillation and carbonization integrated system carbonization
CN103011163A (en) Method for producing calcium carbide from semi-coke obtained through destructive distillation of weakly caking coal
CN110468243B (en) 100% adding tamping coke high-smelting-strength production process for large-scale blast furnace
CN110467953B (en) Method for producing clean formed coke based on water glass transition state binder
CN103965929B (en) A kind of method that raising high volatile does not stick bituminous coal consumption in process of coking
CN104232132A (en) Petroleum coke-added coke and coking method
CN106520246A (en) Method for applying biomass briquettes to coal blending for coking
CN101555427B (en) High thermal stability synthetic ammonia gasification moulded coal and preparation method thereof
CN115044386A (en) Top-loading coking coal blending coking method for fully blending imported coal, product thereof and blended coal for coking
CN112680240B (en) Coking coal blending and application thereof, coke and preparation method thereof
CN113088310A (en) Tamping coal blending coking method, product thereof and blended coal for coking
CN102041130A (en) Method for improving biomass ash fusion point
CN104946284A (en) Coke of blended pretreated low-order non-sticking bituminous coal and coking method

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