CN1880418A - Process for producing briquette - Google Patents
Process for producing briquette Download PDFInfo
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- CN1880418A CN1880418A CN 200610012704 CN200610012704A CN1880418A CN 1880418 A CN1880418 A CN 1880418A CN 200610012704 CN200610012704 CN 200610012704 CN 200610012704 A CN200610012704 A CN 200610012704A CN 1880418 A CN1880418 A CN 1880418A
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Abstract
The invention discloses a typed coal manufacturing method, which comprises the following steps: blending 70-84 percent anthracite coal and 16-30 percent bituminous coal evenly; adding water to model at 300-580 Kg/cm2 modeling pressure with water reaching 11-13 percent; charring for 8-10 h in the cavity-vehicle tunnel cavity; cooling the charred coal through water.
Description
Technical field
The invention belongs to a kind of production method of moulded coal.
Technical background
Clean coal technology is the mainstay of coal in China industrial sustainable development, and shaped coal technology is put into the project optimization of clean coal technology.Along with country is more and more stricter to the environmental protection requirement dynamics, the regulation of the raw coal of stopping to burn is put into effect again and again, and applying of the briquette prod that seems is particularly important.
Traditional powdered coal formation, moulded coal can be divided into by end-use: industrial shaping coal and coal briquette for civillan use two big classes.Coal briquette for civillan use comprises honeycomb briquette, coal briquette etc.
In traditional briquette production technology, mainly contained adhesive cool moulding process (comprising natural curing and oven dry maintenance aftertreatment technology) and added high-adhesion binding agent moulding such as tar or pitch, unloaded in the charring furnaces such as stove, wedged bottom stove, vertical heater, box-type furnace the CARBONIZATION OF BRIQUETTES aftertreatment technology low.There is following defective in the adhesive cool moulding process: 1. briquette prod intensity is low; 2. the use of binding agent can roll up the briquette prod ash content, reduces the briquette prod quality; Defectives such as 3. fixed carbon is low, cold strength is low, immersion intensity is low, carry-over height, this also is the major cause that the decades of research briquette prod is difficult to move towards market.And the coking moulded coal has characteristics such as fixed carbon height, cold strength height, immersion property are good, has been subjected to user's favorable comment.But traditional coking moulded coal technology need be added high-adhesion binding agents such as 6～8% tar or pitch, and the production process yield rate is not really high, causes the production cost height, relatively lacks price advantage with local lump coal.
Summary of the invention
Purpose of the present invention is exactly to overcome the weak point that traditional industry briquette production Technology exists, and provides a kind of production cost low, the briquette production method that yield rate is high.
Production method of the present invention comprises the steps:
1, feed coal is prepared: it is less than 3mm that pulverized anthracite is broken into granularity, wherein less than 1mm greater than 75%, bituminous coal powder is broken into granularity for less than 1mm, wherein less than the 0.45mm amount greater than 70%, with hard coal and bituminous coal is hard coal 70-84% by weight percentage, and bituminous coal 16-30% mixes; Add after mixing entry make moulding moisture reach 11～13%, at 300～580Kg/cm
2The forming pressure compacted under;
2, carry out charing in car tunnel kiln, carbonization temperature is: room temperature～300 ℃, and temperature rise rate is 15～17 ℃/min; 300～500 ℃, temperature rise rate is 12～14 ℃/min; 500～750 ℃, temperature rise rate is 7～9 ℃/min; 750 ℃～final carbonization temperature, temperature rise rate is 7～10 ℃/min, and final carbonization temperature is 850-1000 ℃, and carbonization time is 8～10 hours;
3, charing after heat moulded coal carries out water cooling.
The shape of aforesaid moulded coal should be made cylinder shape, square pillow type or rectangle etc.
Aforesaid bituminous coal is rich coal or 1/3 coking coal.
Because the present invention does not add any binding agent, the initial strength of moulded coal is lower, therefore must select for use into the little car tunnel kiln of stove drop, as SQX-T
1Tunnel type whole-enclosed coal carbonizer.Low these CARBONIZATION OF BRIQUETTES of charing type of furnace incompatibility such as stove, wedged bottom stove, vertical heater, box-type furnace of unloading.
The present invention has following advantage:
1, technology of the present invention is simple, and is easy to operate.
Quality index such as 2, moulded coal fixed carbon height, every intensity index height, the carry-over of the present invention's preparation are low, immersion property is good.
3,, and adopted the very little and moulded coal actionless tunnel furnace charring furnace charing mode in carbonization process of stove drop owing to need not add any binding agent, the rate height that therefore manufactures a finished product, production cost is low, has very big market value advantage.
4, this moulded coal can satisfy fertilizer industry gas making and bunker coal production needs, has expanded the purposes that smokeless smalls is produced moulded coal.
Embodiment
Embodiment 1
It is less than 3mm that Jincheng hard coal (the coal analysis index sees Table 1) is ground into granularity, wherein less than 1mm greater than 75% (the size analysis data see Table 2), it is less than 1mm that rich coal (the coal analysis index sees Table 1) is ground into granularity, wherein measure greater than 70% (the size analysis data see Table 2) less than 0.45mm, with Jincheng hard coal and rich coal is hard coal 70% by weight percentage, rich coal 30% mixes, add entry make moulding moisture reach 11%, at 580Kg/cm
2The forming pressure compacted under;
Carry out charing in car tunnel kiln, carbonization temperature is: room temperature～300 ℃, and temperature rise rate is 15 ℃/min; 300～500 ℃, temperature rise rate is 13 ℃/min; 500～750 ℃, temperature rise rate is 9 ℃/min; 750 ℃～1000 ℃, temperature rise rate is 10 ℃/min, and carbonization time is 10 hours; Charing after heat moulded coal carries out water cooling.The moulded coal of producing detects index and sees Table 3
Embodiment 2
Industrial shaping coal, coal blending raw material are formed (weight percent): rich coal 16%, and the smokeless smalls 84% in Jincheng carries out charing in car tunnel kiln, and carbonization temperature is: room temperature～300 ℃, temperature rise rate is 17 ℃/min; 300～500 ℃, temperature rise rate is 14 ℃/min; 500～750 ℃, temperature rise rate is 8 ℃/min; 750 ℃～850 ℃, temperature rise rate is 7 ℃/min, and carbonization time is 8 hours; Charing after heat moulded coal carries out water cooling.All the other are with embodiment 1, and the moulded coal of producing detects index and sees Table 3.
Embodiment 3
Industrial shaping coal coal blending raw material is formed (weight percent): (the coal analysis index sees Table 1 to 1/3 coking coal, the size analysis data see Table 2) 20%, the smokeless smalls 80% in Jincheng carries out charing in car tunnel kiln, carbonization temperature is: room temperature～300 ℃, and temperature rise rate is 15 ℃/min; 300～500 ℃, temperature rise rate is 12 ℃/min; 500～750 ℃, temperature rise rate is 7 ℃/min; 750 ℃～900 ℃, temperature rise rate is 9 ℃/min, and carbonization time is 8 hours; Charing after heat moulded coal carries out water cooling.All the other are with embodiment 1, and the moulded coal of producing detects index and sees Table 4.
Embodiment 4
Industrial shaping coal coal blending raw material is formed (weight percent): 1/3 coking coal 30%, the smokeless smalls in Yangquan (the coal analysis index sees Table 1, and the size analysis data see Table 2) 70% carries out charing in car tunnel kiln, carbonization temperature is: room temperature～300 ℃, and temperature rise rate is 16 ℃/min; 300～500 ℃, temperature rise rate is 13 ℃/min; 500～750 ℃, temperature rise rate is 9 ℃/min, and 750 ℃～1000 ℃, temperature rise rate is 10 ℃/min, and carbonization time is 10 hours; Charing after heat moulded coal carries out water cooling.All the other are with embodiment 3, and the moulded coal of producing detects index and sees Table 4.
Embodiment 5
The coal blending raw material is formed (weight percent): rich coal 22%, and the smokeless smalls 78% in Yangquan carries out charing in car tunnel kiln, and carbonization temperature is: room temperature～300 ℃, temperature rise rate is 16 ℃/min; 300～500 ℃, temperature rise rate is 14 ℃/min; 500～750 ℃, temperature rise rate is 8 ℃/min; 750 ℃～900 ℃, temperature rise rate is 8 ℃/min, and carbonization time is 9 hours; Charing after heat moulded coal carries out water cooling.All the other are with embodiment 1, and the moulded coal of producing detects index and sees Table 3.
Table 1 feed coal coal analysis
| Coal | Divide bleed Mad% | Ash Aad% | Fugitive constituent Vdaf% | Fixed carbon FCad% | Full sulphur St, ad% | Gelatinous layer Ymm | Caking index | Characteristic of char residue | Thermostability % |
| Hard coal Yangquan, rich coal 1/3 coking coal Jincheng hard coal | 0.99 1.06 1.01 0.76 | 17.39 13.55 18.00 23.46 | 35.43 34.25 9.38 13.39 | 52.70 56.14 73.39 65.64 | 0.45 0.50 ＜0.3 1.12 | 24 16 | 87.68 84.09 | 7 7 | ＞95 |
Table 2 feed coal size analysis data
| Coal | +3mm | +0.9mm | +0.45mm | +0.2mm | -0.2mm |
| Hard coal Yangquan, Jincheng hard coal | 1.5％ 2.0％ | 19.0％ 22.3％ | 22.1％ 26.0％ | 57.4％ 49.7％ | |
| 1/3 coking coal rich coal | 0 0 | 0 0 | 0 19.3％ | 20％ 42.4％ | 80％ 38.3％ |
Each embodiment moulded coal index test data of table 3
Claims (3)
1, a kind of production method of moulded coal is characterized in that comprising the steps:
(1) feed coal is prepared: it is less than 3mm that pulverized anthracite is broken into granularity, wherein less than 1mm greater than 75%, bituminous coal powder is broken into granularity for less than 1mm, wherein less than the 0.45mm amount greater than 70%, with hard coal and bituminous coal is hard coal 70-84% by weight percentage, and bituminous coal 16-30% mixes; Add after mixing entry make moulding moisture reach 11～13%, at 300～580Kg/cm
2The forming pressure compacted under;
(2) carry out charing in car tunnel kiln, carbonization temperature is: room temperature～300 ℃, and temperature rise rate is 15～17 ℃/min; 300～500 ℃, temperature rise rate is 12～14 ℃/min; 500～750 ℃, temperature rise rate is 7～9 ℃/min; 750 ℃～final carbonization temperature, temperature rise rate is 7～10 ℃/min, and final carbonization temperature is 850-1000 ℃, and carbonization time is 8～10 hours;
(3) charing after heat moulded coal carries out water cooling.
2, the production method of a kind of moulded coal as claimed in claim 1 is characterized in that the shape of described moulded coal is made cylinder shape, square pillow type or rectangle.
3, the production method of a kind of moulded coal as claimed in claim 1 is characterized in that described bituminous coal is rich coal or 1/3 coking coal.
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB2006100127046A CN100567466C (en) | 2006-05-12 | 2006-05-12 | A kind of production method of moulded coal |
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| CNB2006100127046A CN100567466C (en) | 2006-05-12 | 2006-05-12 | A kind of production method of moulded coal |
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| CN1880418A true CN1880418A (en) | 2006-12-20 |
| CN100567466C CN100567466C (en) | 2009-12-09 |
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| CNB2006100127046A Active CN100567466C (en) | 2006-05-12 | 2006-05-12 | A kind of production method of moulded coal |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106929116A (en) * | 2017-04-11 | 2017-07-07 | 北京柯林斯达科技发展有限公司 | A kind of preparation technology of coal base smoke-less charcoal fuel |
| CN107216900A (en) * | 2017-07-18 | 2017-09-29 | 府谷县新亚新能源科技发展有限责任公司 | A kind of production method of moulded coal |
-
2006
- 2006-05-12 CN CNB2006100127046A patent/CN100567466C/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106929116A (en) * | 2017-04-11 | 2017-07-07 | 北京柯林斯达科技发展有限公司 | A kind of preparation technology of coal base smoke-less charcoal fuel |
| CN107216900A (en) * | 2017-07-18 | 2017-09-29 | 府谷县新亚新能源科技发展有限责任公司 | A kind of production method of moulded coal |
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| Publication number | Publication date |
|---|---|
| CN100567466C (en) | 2009-12-09 |
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