CN104312608B - Height based on charred coal organization structure go bad coking coal participate in coking blending method - Google Patents

Height based on charred coal organization structure go bad coking coal participate in coking blending method Download PDF

Info

Publication number
CN104312608B
CN104312608B CN201410628440.1A CN201410628440A CN104312608B CN 104312608 B CN104312608 B CN 104312608B CN 201410628440 A CN201410628440 A CN 201410628440A CN 104312608 B CN104312608 B CN 104312608B
Authority
CN
China
Prior art keywords
coal
coking
mosaic texture
grain mosaic
coarse grain
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
CN201410628440.1A
Other languages
Chinese (zh)
Other versions
CN104312608A (en
Inventor
鲍俊芳
宋子逵
薛改凤
盛军波
陈胜春
崔会明
陈翔
贾丽晖
詹立志
张雪红
陈细涛
陈鹏
项茹
王元生
任玉明
冯柏华
谢传斌
万基才
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 Group Corp
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 Group Corp filed Critical Wuhan Iron and Steel Group Corp
Priority to CN201410628440.1A priority Critical patent/CN104312608B/en
Publication of CN104312608A publication Critical patent/CN104312608A/en
Application granted granted Critical
Publication of CN104312608B publication Critical patent/CN104312608B/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

Abstract

The invention discloses a kind of height based on charred coal organization structure go bad coking coal participate in coke making and coal blending method, the method includes: 1) measure height rotten coking coal, other single coking coal coking charred coal organization structures, the coarse grain mosaic texture of zone size 7~10um such as coarse grain mosaic texture, optics in statistics mixed coal, middle grain mosaic texture and incomplete fibre structure sum, silk carbon and fragmentation structure sum, the ratio of complete fiber and laminated structure sum;2) chlorine adding ratio of each single grade coal is determined, guarantee in mixed coal, the ratio of the coarse grain mosaic texture of zone size 7~10um, middle grain mosaic texture and incomplete fibre structure sum, silk carbon and fragmentation structure sum, complete fiber and the laminated structure sums such as coarse grain mosaic texture, optics.The present invention selects to limit These parameters in mixed coal and carries out coal blending, and the Y value of mixed coal and Ji Shi maximum fluidity, under reduced levels, also can be produced high grade coke, thus save the fat coal resource of good fluidity.

Description

Height based on charred coal organization structure go bad coking coal participate in coking blending method
Technical field
The invention belongs to metallurgical coking technology field, be specifically related to a kind of based on charred coal organization structure High rotten coking coal participates in the blending method of coking.
Background technology
The fugitive constituent V of conventional coking coal in coking coaldafBetween 18~28%, the average maximum reflection of vitrinite RateBetween 1.15~1.50%.WhereinCoking coal between 1.35~1.50% is referred to as height Rotten coking coal, this kind of height coking coal caking index G-value that goes bad typically between 75~90, plastometer indice Y Value is general between 14~20mm, Gu-softening temperature is interval general between 50~75 DEG C, and Ji Shi max-flow Dynamic degree is between 10~500ddpm, and swelling degree b value is between 10%~50%, and coarse grain is inlayed component and contained Amount is between 38~78%.According to traditional blending method, the Y value of mixed coal need to reach 15mm with On, Ji Shi maximum fluidity reaches more than 300ddpm, just can produce high grade coke.
But, inventor finds in Coking Test for Blend and production application are put into practice:1.35~ Australian Sa Aji ore deposit coking coal, Shanxi Jinzhong area and Luliang Prefecture's part coking coal between 1.50%, one The above-mentioned coking coal of certainty ratio participates in coal-blending coking, mixed coal Y value only between 12mm~15mm, base Family name's maximum fluidity low value scope between 60ddpm~300ddpm, refines to obtain hot strength of coke CSR Also more than 65% is reached.The most conventionally to such high rotten coking coal, it will transition Consumption gel is abundant, the high-quality caking coal resource of good flowing properties, causes the wasting of resources, increases enterprise Production cost.
Summary of the invention
The technical problem to be solved is to provide a kind of height based on charred coal organization structure and goes bad The coke making and coal blending method that coking coal participates in, it is to avoid the mixed coal Y value that covets reaches more than 15mm, coordinates Coal Ji Shi maximum fluidity reaches more than 300ddpm, and gel is abundant, mobile performance to cause transition to consume The phenomenon of good high-quality caking coal resource, it is to avoid the wasting of resources, increases the performance of enterprises.
For solving above-mentioned technical problem, the blending method designed by the present invention comprises the steps:
1) measure the rotten coking coal of height, other each single grade coal coking charred coal organizations participating in coal-blending coking are tied Structure, the coarse grain mosaic texture of the zone size 7~10um such as coarse grain mosaic texture, optics in statistics mixed coal, Middle grain mosaic texture and incomplete fibre structure sum, silk carbon and fragmentation structure sum, complete fiber and sheet The ratio of shape structure sum, the described height coking coal that goes bad isBetween 1.35~1.50%, G-value 75~ Between 90, Gu-softening temperature is interval between 50~75 DEG C, swelling degree b value is between 10%~50%, slightly Grain inlays constituent content coking coal between 38~78%;
2) one group of Coal Blending Schemes is drafted according to following ranges: high rotten coking coal allocation ratio 15~45%, gas Coal allocation ratio 5~30%, 1/3 coking coal allocation ratio 10~30%, rich coal allocation ratio 10~20%, Middle iso-metamorphism coking coal allocation ratio 5~35%, lean coal allocation ratio 3~10%;Described middle iso-metamorphism coking coal For the average maximum reflectivity of vitriniteCoking coal between 1.15~1.35%;
3) testing the Coal Blending Schemes drafted, touchstone is for meeting following condition simultaneously: mixed coal Middle coarse grain mosaic texture >=20%, and coarse grain mosaic texture >=7% of the zone size 7~10um such as optics; Middle grain mosaic texture and incomplete fibre structure sum >=7%;Silk carbon and fragmentation structure sum be 25~ 35%;Fiber and laminated structure sum are 3~8% completely;
4) if drafting Coal Blending Schemes not reach touchstone, then Coal Blending Schemes is adjusted, method of adjustment: Any or which kind optical texture is unsatisfactory for requirement, then higher or lower to this optical texture Coal allocation ratio be adjusted, until meeting the touchstone of Coal Blending Schemes, complete Coal Blending Schemes Formulate.
Further, the go bad Y value of coking coal of described height between 14mm~20mm, the Y of mixed coal Value is between 12mm~15mm, and Ji Shi maximum fluidity is between 10~500ddpm.
Further, the big Giseeler fluidity of described mixed coal is between 10~240ddpm.
Further, described step 2) in, high rotten coking coal allocation ratio 15~23%, bottle coal is allocated into Ratio 10~25%, 1/3 coking coal allocation ratio 15~25%, rich coal allocation ratio 13~18%, medium Rotten coking coal allocation ratio 20~30%, lean coal allocation ratio 5~8%.
Further, described step 3) in, touchstone is: coarse grain mosaic texture >=21% in mixed coal, And coarse grain mosaic texture >=7% of the zone size 7~10um such as optics;Middle grain mosaic texture is with the most fine Dimension structure sum >=9%;Silk carbon is 28~35% with fragmentation structure sum;Completely fiber and laminated structure it With for 3~8%.
The present invention selects to limit following index: in mixed coal the zone size 7 such as coarse grain mosaic texture, optics~ The coarse grain mosaic texture of 10um, middle grain mosaic texture are tied with fragmentation with incomplete fibre structure sum, silk carbon The reason that structure sum, complete fiber carry out coal blending with laminated structure sum is: when there being high rotten coking coal ginseng During with coal-blending coking, the coarse grain edge of the zone size 7~10um such as the optics that active component coking is transformed Embedding structure STRENGTH ON COKE cold and hot state strength support effect is strong, therefore, as a restriction of mixed coal Index;Coarse grain mosaic texture, middle grain mosaic texture and not exclusively fibre structure all support hot strength of coke, Therefore, using coarse grain mosaic texture in mixed coal, middle grain mosaic texture and incomplete fibre structure sum as The another two of mixed coal limits index;Fiber and laminated structure completely all deteriorates coke quality, it is necessary in addition Limit;Silk carbon and fragmentation structure are coking centers, but with other structure combination interface existing defects, therefore, Silk carbon and fragmentation structural content sum should control in the range of suitably.
Detailed description of the invention
Below in conjunction with detailed description of the invention, the present invention is further detailed explanation.
There are 7 kinds of coking coal resources in certain factory, wherein 2 kindsHeight between 1.35~1.50% goes bad Coking coal, respectively numbered A ore deposit, B ore deposit;The height in these the two kinds of ore deposits coking coal G-value that goes bad between 75~90, Swelling degree b value is between 10%~50%, and coarse grain inlays constituent content between 38~78%.Other coals Kind of 5 ore deposit points, respectively numbered E ore deposit (bottle coal), F ore deposit (rich coal), G ore deposit (1/3 coking coal), H ore deposit (middle iso-metamorphism coking coal), I ore deposit (lean coal);Determine each single grade coal coking charred coal group respectively Knit structure, the coarse grain mosaic texture of the zone sizes such as optics 7~10um is added up.
Coal Blending Schemes is drafted: high rotten coking coal allocation ratio 15~45%, bottle coal is allocated into according to following ranges Ratio 5~30%, 1/3 coking coal allocation ratio 10~30%, rich coal allocation ratio 10~20%, medium Rotten coking coal allocation ratio 5~35%, lean coal allocation ratio 3~10%;
Testing the Coal Blending Schemes drafted, touchstone is: in mixed coal, coarse grain mosaic texture >= 20%, and coarse grain mosaic texture >=7% of the zone size 7~10um such as optics;Middle grain mosaic texture with not Fibre structure sum >=7% completely;Silk carbon is 25~35% with fragmentation structure sum;Fiber and lamellar completely Structure sum is 3~8%;
If drafting Coal Blending Schemes not reach touchstone, then Coal Blending Schemes is adjusted, method of adjustment: Any or which kind optical texture is unsatisfactory for requirement, then higher or lower to this optical texture Coal allocation ratio be adjusted, until meeting the touchstone of Coal Blending Schemes.
Each single grade coal coking charred coal organization structural content the results are shown in Table 1, refines according to the inventive method The specific embodiment of burnt coal blending is shown in Table 2.
Table 1 each single grade coal reflectance, coking optical texture index
Wherein, Gu softening temperature is interval: 51 DEG C of A ore deposit, 73 DEG C of B ore deposit;Ji Shi maximum fluidity A ore deposit 19ddpm, B ore deposit 326ddpm.
Table 2 embodiment 1~4, the Coal Blending Schemes of 1-1,4-1
Blending ratio is adjusted as follows:
In embodiment 1-1, although each coal blend ratio meets area requirement, but optics isochrome in mixed coal The coarse grain mosaic texture content of district's size 7~10um is less than 7%, and hot strength of coke CSR is less than 65%. Because in A ore deposit, the coarse grain mosaic texture content of the zone size 7~10um such as optics is the highest, by its proportioning by 15% improves to 20%, and G ore deposit proportioning reduces by 5% accordingly, sees embodiment 1, the zone such as optics in mixed coal The coarse grain mosaic texture content of size 7~10um is brought up to 8.29% by 6.54%, completes Coal Blending Schemes Adjusting, hot strength of coke CSR is brought up to 66.63% by 64.35%.
In embodiment 4-1, although each coal blend ratio meets area requirement, but optics isochrome in mixed coal The coarse grain mosaic texture content of district's size 7~10um is less than 7%, and coarse grain is inlayed content and is less than 20%, Jiao Charcoal calorific intensity CSR is less than 65%.Because in B ore deposit, the coarse grain of the zone size 7~10um such as optics inlays knot Structure content is higher, its proportioning is improved to 30% by 20%, and G ore deposit proportioning reduces by 10% accordingly, sees enforcement Example 4, in mixed coal, the coarse grain mosaic texture content of the zone size 7~10um such as optics is improved by 5.93% To 8.43%, completing the adjustment of Coal Blending Schemes, hot strength of coke CSR is brought up to 67.12% by 64.06%.
Powder craft after tradition is first joined, without precomminution and selective molecular attraction, without coal damping, without moulded coal, passes Unite under the conditions of more than 4.3 meters top dress coke oven dry coke quenching, use the inventive method gained hot strength of coke CSR 65~70%, M40 is 87~89%, and M10 is 5.5~6%, and relatively prior art reduces coal blending cost About 4,000,000 yuan/month.
According to existing blending method, in order to ensure that mixed coal Y value reaches more than 15mm, mixed coal Ji Shi Maximum fluidity reaches more than 300ddpm, need to reduce weakly caking bottle coal, lean coal consumption, increases colloid 1/3 coking coal of body relative abundance, coking coal and rich coal consumption.
The Coal Blending Schemes of comparative example 1,2,3,4 is shown in Table 3.
The cold and hot state intensity of 1,2,3,4 coking charcoals of comparative example is shown in Table 4.
From table 3 and 4 column data of table it can be seen that comparative example 1,2,3,4 and embodiment 1,2,3, 4 compare, and coke quality is in peer-level, and mixed coal cost is the highest 5.54 yuan/ton, affects enterprise's warp Ji benefit.
The Coal Blending Schemes of table 3 comparative example 1,2,3,4
1,2,3,4 coking charcoal cold and hot state intensity of table 4 comparative example
Embodiment M25/% M10/% CRI/% CSR/%
Comparative example 1 88.78 9.25 20.02 66.71
Comparative example 2 90.33 8.53 18.77 68.64
Comparative example 3 89.57 9.38 19.15 66.52
Comparative example 4 90.29 9.13 19.76 67.34

Claims (6)

1. height based on charred coal organization structure goes bad the coke making and coal blending method that coking coal participates in, and it is special Levy and be: this blending method comprises the steps:
1) measure the rotten coking coal of height, other each single grade coal coking charred coal organizations participating in coal-blending coking are tied Structure, the coarse grain mosaic texture of the zone size 7~10um such as coarse grain mosaic texture, optics in statistics mixed coal, Middle grain mosaic texture and incomplete fibre structure sum, silk carbon and fragmentation structure sum, complete fiber and sheet The ratio of shape structure sum, the described height coking coal that goes bad isBetween 1.35~1.50%, G-value 75~ Between 90, Gu-softening temperature is interval between 50~75 DEG C, swelling degree b value is between 10%~50%, slightly Grain inlays constituent content coking coal between 38~78%;
2) coal blending is carried out according to following Coal Blending Schemes: high rotten coking coal allocation ratio 15~45%, bottle coal is joined Enter ratio 5~30%, 1/3 coking coal allocation ratio 10~30%, rich coal allocation ratio 10~20%, in Iso-metamorphism coking coal allocation ratio 5~35%, lean coal allocation ratio 3~10%;Described middle iso-metamorphism coking coal is The average maximum reflectivity of vitriniteCoking coal between 1.15~1.35%;
And meet: in mixed coal, coarse grain mosaic texture >=20%, and the zone size 7~10um such as optics Coarse grain mosaic texture >=7%;Middle grain mosaic texture and incomplete fibre structure sum >=7%;Silk carbon is with broken Chip architecture sum is 25~35%;Fiber and laminated structure sum are 3~8% completely.
Height based on charred coal organization structure the most according to claim 1 go bad coking coal participate in refining Burnt blending method, it is characterised in that: the go bad Y value of coking coal of described height between 14mm~20mm, The Y value of mixed coal is between 12mm~15mm, and Ji Shi maximum fluidity is between 10~500ddpm.
Height based on charred coal organization structure the most according to claim 1 and 2 go bad coking coal participate in Coke making and coal blending method, it is characterised in that: the Ji Shi maximum fluidity of described mixed coal is 10~240ddpm Between.
Height based on charred coal organization structure the most according to claim 1 and 2 go bad coking coal participate in Coke making and coal blending method, it is characterised in that: described step 2) in, high rotten coking coal allocation ratio 15~ 23%, bottle coal allocation ratio 10~25%, 1/3 coking coal allocation ratio 15~25%, rich coal allocation ratio 13~18%, middle iso-metamorphism coking coal allocation ratio 20~30%, lean coal allocation ratio 5~8%.
Height based on charred coal organization structure the most according to claim 1 and 2 go bad coking coal participate in Coke making and coal blending method, it is characterised in that: described step 2) in, coarse grain mosaic texture >=21% in mixed coal, And coarse grain mosaic texture >=7% of the zone size 7~10um such as optics;Middle grain mosaic texture is with the most fine Dimension structure sum >=9%;Silk carbon is 28~35% with fragmentation structure sum;Completely fiber and laminated structure it With for 3~8%.
Height based on charred coal organization structure the most according to claim 3 go bad coking coal participate in refining Burnt blending method, it is characterised in that: described step 2) in, coarse grain mosaic texture >=21% in mixed coal, And coarse grain mosaic texture >=7% of the zone size 7~10um such as optics;Middle grain mosaic texture is with the most fine Dimension structure sum >=9%;Silk carbon is 28~35% with fragmentation structure sum;Completely fiber and laminated structure it With for 3~8%.
CN201410628440.1A 2014-11-10 2014-11-10 Height based on charred coal organization structure go bad coking coal participate in coking blending method Active CN104312608B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201410628440.1A CN104312608B (en) 2014-11-10 2014-11-10 Height based on charred coal organization structure go bad coking coal participate in coking blending method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201410628440.1A CN104312608B (en) 2014-11-10 2014-11-10 Height based on charred coal organization structure go bad coking coal participate in coking blending method

Publications (2)

Publication Number Publication Date
CN104312608A CN104312608A (en) 2015-01-28
CN104312608B true CN104312608B (en) 2016-08-17

Family

ID=52367930

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201410628440.1A Active CN104312608B (en) 2014-11-10 2014-11-10 Height based on charred coal organization structure go bad coking coal participate in coking blending method

Country Status (1)

Country Link
CN (1) CN104312608B (en)

Families Citing this family (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104655818B (en) * 2015-02-13 2016-04-13 武汉钢铁(集团)公司 The Forecasting Methodology of coal-blending coking coke shatter strength
CN104745217A (en) * 2015-04-01 2015-07-01 武汉钢铁(集团)公司 Blending method of high-metamorphous coking coal
CN105062532B (en) * 2015-09-02 2017-05-10 武汉钢铁(集团)公司 Coal blending method for controlling coke quality
CN110746997B (en) * 2019-10-29 2021-03-19 武汉钢铁有限公司 Method for refining metallurgical coke
CN111029576B (en) * 2019-11-12 2023-09-29 山西沁新能源集团股份有限公司 Method for blending crystalline carbon precursor coal
CN113621393B (en) * 2021-07-21 2022-11-01 武汉钢铁有限公司 Classification matching method of coking coal with 18-22% of volatile matter

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR20000019095A (en) * 1998-09-08 2000-04-06 윤대근 Preparation method of coke with high crystallization
CN103184058A (en) * 2013-04-15 2013-07-03 武汉钢铁(集团)公司 Coal coking and blending method beneficial to cold coke strength
CN103923678A (en) * 2014-04-24 2014-07-16 武汉钢铁(集团)公司 Coking coal blending method of improving homogeneity coefficient of coke size

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR20000019095A (en) * 1998-09-08 2000-04-06 윤대근 Preparation method of coke with high crystallization
CN103184058A (en) * 2013-04-15 2013-07-03 武汉钢铁(集团)公司 Coal coking and blending method beneficial to cold coke strength
CN103923678A (en) * 2014-04-24 2014-07-16 武汉钢铁(集团)公司 Coking coal blending method of improving homogeneity coefficient of coke size

Also Published As

Publication number Publication date
CN104312608A (en) 2015-01-28

Similar Documents

Publication Publication Date Title
CN104312608B (en) Height based on charred coal organization structure go bad coking coal participate in coking blending method
CN104330542B (en) Height based on charred coal organization structure goes bad the coal property evaluation of coking coal and application method
CN103865554B (en) A kind of vast scale uses the blending method of high volatile coking coal
CN104312607B (en) High rotten coking coal participates in the blending method of coking
CN102604659B (en) Coking coal blending method using high-expansion coking coal
CN104359864B (en) The coal-blending coking method that high rotten coking coal participates in
CN102676191A (en) Method for sorting coking coal with 32-37% volatile component and coking blending method
CN102690669A (en) Coking coal quality classification method and coal blending and coking method with participation of coking coal
CN101735840A (en) Method for coking and mixing coal by participation of coking coal
CN105778962B (en) The coal-blending coking method of coke is produced under high fine coal ratio
CN106501481B (en) A kind of evaluation method of rich coal coal quality
CN104804755B (en) Coal blending method for coking 1/3 coking coal having solid softening temperature interval below 85 DEG C
CN104140833A (en) Coal-blending and coke-making method involved with low G value 1/3 coking coal
CN103923678B (en) Coking coal blending method of improving homogeneity coefficient of coke size
CN105802649B (en) A kind of middle volatile matter low bulk high convergency coking coal application method
CN105331381B (en) A kind of coke making and coal blending method
CN104845650B (en) Control coke M10The coke making and coal blending method of index
CN104140835B (en) The coal-blending coking method that the low flowing coking coal of high expansion lower shrinkage degree participates in
CN105255509B (en) A kind of coke making and coal blending method
CN104830360B (en) Coal blending coking method of 1/3 coking coal with 34% or above of volatile
CN104140836B (en) The coal-blending coking method that low flowing high expansion lower shrinkage degree coking coal participates in
CN104479708B (en) The regulation and control method of coke strenth
CN101864323B (en) Coal blending and coking method for utilizing coal petrography to produce coke with low reactivity and high heat intensity
CN102942944B (en) Coal coking and blending method with Anhui 1/3 coking coal involved
CN104109548A (en) Coking and coal blending method participated by gas coal with fluidity of no less than 1000 ddpm

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
TR01 Transfer of patent right

Effective date of registration: 20170727

Address after: 430083, Hubei Wuhan Qingshan District Factory No. 2 Gate joint stock company organs

Patentee after: Wuhan iron and Steel Company Limited

Address before: 430080 Wuchang, Hubei Friendship Road, No. A, block, floor 999, 15

Patentee before: Wuhan Iron & Steel (Group) Corp.

TR01 Transfer of patent right