CN107686737A - Gu softening temperature section is the coke making and coal blending method of more than 90 DEG C 1/3 coking coal - Google Patents

Gu softening temperature section is the coke making and coal blending method of more than 90 DEG C 1/3 coking coal Download PDF

Info

Publication number
CN107686737A
CN107686737A CN201710868809.XA CN201710868809A CN107686737A CN 107686737 A CN107686737 A CN 107686737A CN 201710868809 A CN201710868809 A CN 201710868809A CN 107686737 A CN107686737 A CN 107686737A
Authority
CN
China
Prior art keywords
coal
coking
coking coal
classes
softening temperature
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.)
Pending
Application number
CN201710868809.XA
Other languages
Chinese (zh)
Inventor
宋子逵
薛改凤
项茹
任玉明
詹立志
鲍俊芳
陈鹏
张雪红
陈细涛
王元生
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.)
Wuhan Iron and Steel Co Ltd
Original Assignee
Wuhan 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 Wuhan Iron and Steel Co Ltd filed Critical Wuhan Iron and Steel Co Ltd
Priority to CN201710868809.XA priority Critical patent/CN107686737A/en
Publication of CN107686737A publication Critical patent/CN107686737A/en
Pending legal-status Critical Current

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)
  • Solid Fuels And Fuel-Associated Substances (AREA)

Abstract

The invention discloses the coke making and coal blending method that a kind of solid softening temperature section is more than 90 DEG C 1/3 coking coal, belong to coal-blending coking technical field.This method comprises the following steps:1) Giseeler fluidity measure is carried out to 1/3 coking coal:1/3 coking coal for choosing solid softening temperature section >=90 DEG C is designated as the coking coal of A classes 1/3, Gu 90 DEG C of softening temperature section < 1/3 coking coal is designated as the coking coal of B classes 1/3;2) coking coal of A classes 1/3 is subjected to coal blending by following mass percent:Bottle coal:5%, rich coal:The coking coal of 0~30%, A class 1/3:The coking coal of 0~30%, B class 1/3:25%, coking coal:40%, lean coal:10%.Subdivision collocation is optimized by the solid softening temperature section being introduced into Giseeler fluidity index 1/3 coking coal partially fertile to ature of coal to use, and is partly substituted high-quality rich coal, on the premise of coke quality is stablized, is reached the purpose for reducing coal blending cost.

Description

Gu-softening temperature section is the coke making and coal blending method of more than 90 DEG C 1/3 coking coal
Technical field
The present invention relates to the coke making and coal blending method of 1/3 coking coal, belongs to coal-blending coking technical field, is specifically related to one kind Gu-softening temperature section is the coke making and coal blending method of more than 90 DEG C 1/3 coking coal.
Background technology
China's coal resource enriches, but coking coal resource is in short supply, and skewness weighs in limited coking coal resource. In the coal reserves verified, coking coal reserves only accounts for the 26% of coal gross reserves, and coking coal only accounts for coking coal reserves 17.57%, wherein, rich coal accounts for the 10% of coking coal reserves.And in coal-blending coking, burnt rich coal should typically account for 50%-60%, because This, contradiction is serious between coking coal resource and the demand of coke making and coal blending.
In order to improve coke quality and reduce production cost, coking worker in various countries' gradually starts to pay attention to non-master Come in the application study of coking coal, and the coal that 1/3 coking coal is higher as content in China's coal resource deposit, how to use 1/3 Jiao Coal has turned into the required problems faced of coking worker.1/3 coking coal is as a kind of degree of metamorphism between coking coal and rich coal Coal, its complexity are higher than burnt rich coal, and use of the China to 1/3 coking coal depend on traditional coal index and Certain lack be present in the combined index of the vitrinite reflectance of coal petrography index and its distribution, both indexs and both indexs Fall into, it is impossible to reasonable employment comprehensively is accomplished to 1/3 coking coal.
Chinese invention patent application (application publication number:CN104804755A, data of publication of application:2015-07-29) disclose Gu-soft silicon carbide is the coke making and coal blending method of less than 85 DEG C 1/3 coking coal, Coal Blending Schemes disclosed in the application for a patent for invention are: 1) Giseeler fluidity measure is carried out to 1/3 coking coal, selection wherein consolidates 1/3 coking coal that softening temperature section is 70~85 DEG C and is designated as I class 1/3 coking coal, 85 DEG C of temperature range > 1/3 coking coal are designated as other 1/3 coking coal;2) coking coal of I class 1/3 is pressed into following mass percent Carry out coal blending:Gas rich coal:1~10%, rich coal:1~10%, the coking coal of I class 1/3:1~15%, other 1/3 coking coal:10~20%, Coking coal:40~45%, lean coal:10~15%;Solid-softening temperature the section is divided into 34% for the volatilization of less than 85 DEG C 1/3 coking coal More than and.
Chinese invention patent application (application publication number:CN104804755A, data of publication of application:2015-07-29) disclose Volatilization is divided into the coke making and coal blending method of 1/3 coking coal of 34% and the above, and the Coal Blending Schemes of this method are:1) 1/3 coking coal is carried out Giseeler fluidity determines, and 1/3 coking coal for choosing wherein solid -70 DEG C of softening temperature section < is designated as the coking coal of II class 1/3, Gu Ruanwenduqu Between 85 DEG C of ﹥ 1/3 coking coal be designated as other 1/3 coking coal.2) coking coal of II class 1/3 is subjected to coal blending by following mass percent:Gas fertilizer Coal:1~10%, rich coal:1~15%, the coking coal of II class 1/3:5~10%, other 1/3 coking coal:10~20%, coking coal:40~ 45%, lean coal:10~15%.
But solid-softening temperature the section for 1/3 coking coal that above-mentioned two pieces application for a patent for invention uses is respectively less than 70 DEG C with 70 Between~85 DEG C, its maximum fluidity can not reach the standard of substituting fat.
The content of the invention
In order to solve the above technical problems, the invention discloses the refining that a kind of solid-softening temperature section is more than 90 DEG C 1/3 coking coal Burnt blending method, the coke making and coal blending method are by the solid-softening temperature section being introduced into Giseeler fluidity index partially fertile to ature of coal 1/3 coking coal optimizes subdivision collocation and used, and partly substitutes high-quality rich coal, on the premise of coke quality is stablized, reaches reduction The purpose of coal blending cost.
To achieve the above object, match somebody with somebody the invention provides a kind of solid-softening temperature section for the coking of more than 90 DEG C 1/3 coking coal Coal method, comprises the following steps:
1) Giseeler fluidity measure is carried out to 1/3 coking coal:1/3 coking coal for choosing solid-softening temperature section >=90 DEG C is designated as A classes 1/3 coking coal, Gu -90 DEG C of softening temperature section < 1/3 coking coal is designated as the coking coal of B classes 1/3;
2) coking coal of A classes 1/3 is subjected to coal blending by following mass percent:
Bottle coal:5%, rich coal:The coking coal of 0~30%, A class 1/3:The coking coal of 0~30%, B class 1/3:25%, coking coal:40%, it is thin Coal:10%.
Further, the coking coal of A classes 1/3 is subjected to coal blending by following mass percent:
Bottle coal:5%, rich coal:The coking coal of 0~20%, A class 1/3:The coking coal of 0~20%, B class 1/3:25%, coking coal:40%, it is thin Coal:10%, the mass percent of the coking coal of A classes 1/3 does not include zero.
Preferably, the coking coal of A classes 1/3 is subjected to coal blending by following mass percent:
Bottle coal:5%, rich coal:The coking coal of 18%, A class 1/3:The coking coal of 2%, B class 1/3:25%, coking coal:40%, lean coal: 10%.
Preferably, the coking coal of A classes 1/3 is subjected to coal blending by following mass percent:
Bottle coal:5%, rich coal:The coking coal of 15%, A class 1/3:The coking coal of 5%, B class 1/3:25%, coking coal:40%, lean coal: 10%.
Preferably, the coking coal of A classes 1/3 is subjected to coal blending by following mass percent:
Bottle coal:5%, rich coal:The coking coal of 13%, A class 1/3:The coking coal of 7%, B class 1/3:25%, coking coal:40%, lean coal: 10%.
Preferably, the coking coal of A classes 1/3 is subjected to coal blending by following mass percent:
Bottle coal:5%, rich coal:The coking coal of 10%, A class 1/3:The coking coal of 10%, B class 1/3:25%, coking coal:40%, lean coal: 10%.
Preferably, the coking coal of A classes 1/3 is subjected to coal blending by following mass percent:
Bottle coal:5%, rich coal:The coking coal of 8%, A class 1/3:The coking coal of 12%, B class 1/3:25%, coking coal:40%, lean coal: 10%.
Preferably, the coking coal of A classes 1/3 is subjected to coal blending by following mass percent:
Bottle coal:5%, rich coal:The coking coal of 5%, A class 1/3:The coking coal of 15%, B class 1/3:25%, coking coal:40%, lean coal: 10%.
Preferably, the coking coal of A classes 1/3 is subjected to coal blending by following mass percent:
Bottle coal:5%, rich coal:The coking coal of 3%, A class 1/3:The coking coal of 17%, B class 1/3:25%, coking coal:40%, lean coal: 10%.
Bottle coal:5%, rich coal:The coking coal of 0%, A class 1/3:The coking coal of 20%, B class 1/3:25%, coking coal:40%, lean coal: 10%.
Preferably, the coking coal of A classes 1/3 is subjected to coal blending by following mass percent:
Bottle coal:5%, rich coal:The coking coal of 15%, A class 1/3:The coking coal of 10%, B class 1/3:20%, coking coal:40%, lean coal: 10%.
Preferably, the coking coal of A classes 1/3 is subjected to coal blending by following mass percent:
Bottle coal:5%, rich coal:The coking coal of 15%, A class 1/3:The coking coal of 8%, B class 1/3:22%, coking coal:40%, lean coal: 10%.
Preferably, the coking coal of A classes 1/3 is subjected to coal blending by following mass percent:
Bottle coal:5%, rich coal:The coking coal of 15%, A class 1/3:The coking coal of 2%, B class 1/3:28%, coking coal:40%, lean coal: 10%.
Yet further, the adhesive index value of the coking coal of A classes 1/3:90, maximum thick ness of plastic layer Y value:19, max-flow Dynamic degree:12543ddpm, Gu-softening temperature section:99℃.
Further, the adhesive index value of the coking coal of B classes 1/3:88, maximum thick ness of plastic layer Y value:17, max-flow Dynamic degree:1578ddpm, Gu-softening temperature section:83℃.
Further, the adhesive index value of the rich coal:95, maximum thick ness of plastic layer Y value:27, fugitive constituent Vdaf: 31%, maximum fluidity:50000ddpm, Gu-softening temperature section:105℃.
Beneficial effect:
The method of the present invention is using Giseeler fluidity index is introduced, and to ature of coal, 1/3 partially fertile coking coal optimizes fine distribution With when solid-softening temperature section reaches 90 DEG C and the above, its maximum fluidity basically reaches or more than 10000ddpm, this explanation The gel activity of 1/3 coking coal is big, and rich content, to be in close proximity to rich coal, and its price is significantly lower than rich coal, wherein often The price difference of ton reduces the production cost of coal blending, therefore can be used by Optimized Coal Blending to a certain extent more than 26 yuan Such 1/3 coking coal part substituting fat, so as to reach stable coke quality, reduce the purpose of coal blending cost.
Embodiment
In order to preferably explain the present invention, below in conjunction with the specific embodiment main contents that the present invention is furture elucidated, but Present disclosure is not limited solely to following examples.
The invention discloses the coke making and coal blending method that a kind of solid-softening temperature section is more than 90 DEG C 1/3 coking coal, the coking is matched somebody with somebody Gu coal method is finely divided by using Giseeler fluidity index-- softening temperature section of coal to 1/3 coking coal, solid-soft temperature is chosen 1/3 coking coal of degree section >=90 DEG C is designated as the coking coal of A classes 1/3, Gu -90 DEG C of softening temperature section < 1/3 coking coal is designated as Jiao of B classes 1/3 Coal;Wherein, the coking coal of A classes 1/3, the performance parameter of the high-quality rich coal of the coking coal of B classes 1/3 and Shanxi are as shown in table 1;
The performance parameter list of the part coal of table 1
The fugitive constituent V of the above-mentioned high-quality rich coal in ShanxidafFor 31%.
In addition, partly substituting high-quality rich coal from the coking coal of A classes 1/3, table 2 has been obtained.
The mass percentage content (%) of 2 various coking coals of table
Scheme Bottle coal Rich coal The coking coal of A classes 1/3 The coking coal of B classes 1/3 Coking coal Lean coal
Contrast 5 20 0 25 40 10
1 5 18 2 25 40 10
2 5 15 5 25 40 10
3 5 13 7 25 40 10
4 5 10 10 25 40 10
5 5 8 12 25 40 10
6 5 5 15 25 40 10
7 5 3 17 25 40 10
8 5 0 20 25 40 10
9 5 15 10 20 40 10
10 5 15 8 22 40 10
11 5 15 2 28 40 10
The coking coal configured to above-mentioned contrast scheme and 1~embodiment of embodiment 11 carries out heat property test point respectively Analysis, has obtained table 3;
The heat property test analysis list of 3 various coking coals of table
As shown in Table 3, using the coking coal part substituting fat of A classes 1/3, when the mass percentage content of the coking coal of A classes 1/3 is 2 When between~17%, the post reaction strength CSR of coke is 69.95~62.89%, when the complete substituting fat of the coking coal of A classes 1/3, The post reaction strength CSR of coke is 62.00%, and 70.50% compared with rich coal is small, therefore, is substituted when using the coking coal part of A classes 1/3 During rich coal, there is no too much influence for the combination property of mixed coal.
Meanwhile in rich coal used in our factory in 2017, high-quality middle volatile matter, high fluidity rich coal cost price are 1236 yuan/ton (prices in June), 1/3 high-quality coking coal cost price are 1211 yuan/ton (prices in June), and price differential reaches 26 yuan/ton, on Half a year high-quality middle volatile matter, high fluidity rich coal dosage reach 84000 tons, the 2.1% of total dosage are accounted for, if according to this patent side Method can be implemented, and substitute high-quality rich coal with 1/3 high-quality coking coal part, replacement amount is 1% or so, according to coking coal yearly consumption 8000000 tons of calculating, it is contemplated that 2,080,000 yuan of coal blending cost can be saved.
Above example is only optimal citing, and is not the restriction to embodiments of the present invention.Except above-described embodiment Outside, the present invention also has other embodiment.All technical schemes formed using equivalent substitution or equivalent transformation, all fall within the present invention It is required that protection domain.

Claims (6)

1. a kind of solid-softening temperature section is the coke making and coal blending method of more than 90 DEG C 1/3 coking coal, it is characterised in that:Including following step Suddenly:
1) Giseeler fluidity measure is carried out to 1/3 coking coal:1/3 coking coal for choosing solid-softening temperature section >=90 DEG C is designated as A classes 1/3 Coking coal, Gu -90 DEG C of softening temperature section < 1/3 coking coal is designated as the coking coal of B classes 1/3;
2) coking coal of A classes 1/3 is subjected to coal blending by following mass percent:
Bottle coal:5%, rich coal:The coking coal of 0~30%, A class 1/3:The coking coal of 0~30%, B class 1/3:20~30%, coking coal:40%, it is thin Coal:10%.
2. solid-soft silicon carbide according to claim 1 is the coke making and coal blending method of more than 90 DEG C 1/3 coking coal, its feature It is:The coking coal of A classes 1/3 is subjected to coal blending by following mass percent:
Bottle coal:5%, rich coal:The coking coal of 0~20%, A class 1/3:The coking coal of 0~20%, B class 1/3:25%, coking coal:40%, lean coal: 10%, the mass percent of the coking coal of A classes 1/3 does not include zero.
3. solid-soft silicon carbide according to claim 2 is the coke making and coal blending method of more than 90 DEG C 1/3 coking coal, its feature It is:The coking coal of A classes 1/3 is subjected to coal blending by following mass percent:
Bottle coal:5%, rich coal:The coking coal of 15%, A class 1/3:The coking coal of 5%, B class 1/3:25%, coking coal:40%, lean coal:10%.
4. solid-soft silicon carbide according to claim 1 or 2 is the coke making and coal blending method of more than 90 DEG C 1/3 coking coal, it is special Sign is:The adhesive index value of the coking coal of A classes 1/3:90, maximum thick ness of plastic layer Y value:19, maximum fluidity: 12543ddpm, Gu-softening temperature section:99℃.
5. solid-soft silicon carbide according to claim 1 or 2 is the coke making and coal blending method of more than 90 DEG C 1/3 coking coal, it is special Sign is:The adhesive index value of the coking coal of B classes 1/3:88, maximum thick ness of plastic layer Y value:17, maximum fluidity: 1578ddpm, Gu-softening temperature section:83℃.
6. solid-soft silicon carbide according to claim 1 or 2 is the coke making and coal blending method of more than 90 DEG C 1/3 coking coal, it is special Sign is:The adhesive index value of the rich coal:95, maximum thick ness of plastic layer Y value:27, fugitive constituent Vdaf:31%, maximum fluidity Degree:50000ddpm, Gu-softening temperature section:105℃.
CN201710868809.XA 2017-09-22 2017-09-22 Gu softening temperature section is the coke making and coal blending method of more than 90 DEG C 1/3 coking coal Pending CN107686737A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201710868809.XA CN107686737A (en) 2017-09-22 2017-09-22 Gu softening temperature section is the coke making and coal blending method of more than 90 DEG C 1/3 coking coal

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201710868809.XA CN107686737A (en) 2017-09-22 2017-09-22 Gu softening temperature section is the coke making and coal blending method of more than 90 DEG C 1/3 coking coal

Publications (1)

Publication Number Publication Date
CN107686737A true CN107686737A (en) 2018-02-13

Family

ID=61155386

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201710868809.XA Pending CN107686737A (en) 2017-09-22 2017-09-22 Gu softening temperature section is the coke making and coal blending method of more than 90 DEG C 1/3 coking coal

Country Status (1)

Country Link
CN (1) CN107686737A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108641739A (en) * 2018-04-28 2018-10-12 重庆大学 A method of improving coke quality coal blending

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104804755A (en) * 2015-05-14 2015-07-29 武汉钢铁(集团)公司 Coal blending method for coking 1/3 coking coal having solid softening temperature interval below 85 DEG C

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104804755A (en) * 2015-05-14 2015-07-29 武汉钢铁(集团)公司 Coal blending method for coking 1/3 coking coal having solid softening temperature interval below 85 DEG C

Non-Patent Citations (3)

* Cited by examiner, † Cited by third party
Title
吴占松等: "《煤炭清洁有效利用技术》", 31 July 2007, 化学工业出版社 *
张双全等: "《煤化学》", 31 January 2015, 中国矿业大学出版社 *
潘立慧等: "《炼焦技术问答》", 31 January 2007, 冶金工业出版社 *

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108641739A (en) * 2018-04-28 2018-10-12 重庆大学 A method of improving coke quality coal blending

Similar Documents

Publication Publication Date Title
CN111621314B (en) Tamping coal blending coking method
CN111621313B (en) Tamping coal blending coking method
CN105713634A (en) Coal blending method for producing high-quality coke by high-proportion matched use of lean coal and gas coal
CN104312608B (en) Height based on charred coal organization structure go bad coking coal participate in coking blending method
CN107686737A (en) Gu softening temperature section is the coke making and coal blending method of more than 90 DEG C 1/3 coking coal
CN104804755B (en) Coal blending method for coking 1/3 coking coal having solid softening temperature interval below 85 DEG C
CN105199764A (en) Method for coal coking and blending based on organic sulfur-enriched high sulfur coke and fat coal
CN107541229B (en) Coke prepared by blending ultrahigh-sulfur coking coal and coking method
CN105603180A (en) Method for producing sinter at low cost
CN109233883B (en) Gasified coke mixed with high-proportion low-quality coal and preparation method thereof
CN104312607B (en) High rotten coking coal participates in the blending method of coking
CN104102821B (en) The method for setting up bottle coal coal property evaluation model
CN105778962A (en) Coal blending and coking method for producing coke at high pulverized coal proportion
CN102839004A (en) Coking coal blending method
CN108753332B (en) Coking coal blending method for preparing high-quality metallurgical coke
CN106047393A (en) Coking coal blending method involving low-proportion prime coking coal
CN104830360B (en) Coal blending coking method of 1/3 coking coal with 34% or above of volatile
CN104140835A (en) Coal blending and coking method with high-expansion, low-shrinkage-degree and low-flow coking coal participating in
CN1244668C (en) Coal for coking prepared from anthracite and coke produced from said coal and production method of said coke
CN107557042B (en) The method of high mixture ratio weakly caking coal control coke quality
CN109054685B (en) Coke powder adhesive, coke balls suitable for production of closed calcium carbide furnace and preparation method thereof, and production method of calcium carbide of closed calcium carbide furnace
CN102807883A (en) Gas-fat-doped coking and coal blending method
CN113621393B (en) Classification matching method of coking coal with 18-22% of volatile matter
CN109852411A (en) A kind of coal blending for coke
CN114507536B (en) Coal blending method for improving crushing strength of coke

Legal Events

Date Code Title Description
PB01 Publication
PB01 Publication
SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination
RJ01 Rejection of invention patent application after publication

Application publication date: 20180213

RJ01 Rejection of invention patent application after publication