CN101984018A - External heating internal coal decomposing equipment - Google Patents
External heating internal coal decomposing equipment Download PDFInfo
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- CN101984018A CN101984018A CN 201010527779 CN201010527779A CN101984018A CN 101984018 A CN101984018 A CN 101984018A CN 201010527779 CN201010527779 CN 201010527779 CN 201010527779 A CN201010527779 A CN 201010527779A CN 101984018 A CN101984018 A CN 101984018A
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Abstract
The invention discloses external heating internal coal decomposing equipment, comprising a sealed kiln body, wherein the kiln body is internally provided with coal propelling and decomposing pipes; the coal propelling and decomposing pipes are provided with a coal inlet, a coal outlet and a decomposed gas collecting pipe; heat exchange bins are arranged between the coal propelling and decomposing pipes and the inner wall of the kiln body; the heat exchange bins are connected with a high temperature gas heating mechanism by a gas inlet pipe; and the heat exchange bins are provided with a heated gas delivery pipe at the side far away from the high temperature gas heating mechanism. As the high temperature kiln body is internally provided with the coal propelling and decomposing pipes, plenty of hot air in the high temperature kiln body surrounds the coal propelling and decomposing pipes and conducts and radiates heat to the coal dust in the coal propelling and decomposing pipes, and the coal dust fully absorbs the heat and is heated and decomposed into gases, tar gases and coal with higher heat value in the coal propelling and decomposing pipes.
Description
Technical field
The invention belongs to the comprehensive utilization of coal material, energy-conserving and emission-cutting technology field, be specifically related to a kind of interior coal external-heat coal material decomposition equipment.
Background technology
In known technology, the coal system of utilization coal gas is arranged, have and utilize the coal preparing natural gas, utilize coal to carry out high temperature, middle temperature, semi-coking, system gas in addition, but above-mentioned processing method if not being rolled into a ball into piece, coal dust to be screened the piece material exactly, cause raw materials cost to increase, perhaps institute's aerogenesis calorific value is not high, and added value is not high, and economic benefit and social benefit are not remarkable.It is hybrid that the type of heating of stove can be divided into external-heat, internal heat type and the outer heat of interior heat.The heating medium of external-heat stove does not directly contact with raw material, and heat is imported into by the furnace wall; The heating medium of internal heat type stove directly contacts with raw material, because of the difference of heating medium has two kinds of the gentle body heat support methods of solid heat carrier method.
Internal heat type gaseous heat-carrier method is the industrial typical method that has adopted.This method adopts gaseous heat-carrier internal heat type vertical continuous stove, promptly comprises dryer section from top to down, decomposes section and cooling section three parts.(about 25～60mm) from top to bottom move, and directly contact with the burning gas adverse current and are heated for coal low-temperature decomposition brown coal or the type piece that is pressed into by brown coal.About 15% o'clock of the water content of furnace roof raw material removes below the moisture to 1.0% in dryer section, and upstream about 250 ℃ of hot gass are chilled to 80～100 ℃.Dry back raw material is heated to about 500 ℃ in the decomposition section by 600～700 ℃ of oxygen-free burning gas, and thermolysis takes place; Hot gas is chilled to about 250 ℃, and the semicoke of generation enters cooling section and cooled off by cold air.Semicoke is discharged back further water and air cooling.From decomposing section volatile matter of overflowing, obtain tar and pyrolysis water through steps such as condensation, coolings.Germany, the U.S., the Soviet Union, Czechoslovakia, new two blue and day these type of type of furnaces of the Ceng Jianhang of our department.
The internal heat type solid heat carrier method is the typical method of solid thermal carriers internal heat type.Raw material is brown coal, noncaking coal, weak caking coal and resinous shale.Be the pilot plant of 10t/h coal in this Teng Jianyou one cover processing power of Germany Dorr the 1950's, and the thermal barrier of use is solid particulate (little porcelain ball, sand or a semicoke).Because the process product gas does not contain waste gas, so the equipment size of after-treatment system is less, caloric power of gas is higher, can reach 20.5～40.6MJ/m
3Therefore this method has very big processing power because the temperature difference is big, and particle is little, and heat transfer is exceedingly fast.The gained liquid product is more, during the processing high volatile coal, productive rate can reach 30%.L-R method technical process coal low-temperature decomposition is at first with the fritter feed coal of preliminary preheating, mixes in mixing tank with the hot semicoke from separator, and the thermolysis effect takes place.Fall into then in the snubber, stop certain hour, finish thermolysis.The semicoke that comes out from snubber enters the riser tube bottom, is submitted by warm air, and burning-off carbon residue wherein in riser tube elevates the temperature simultaneously, enters then and carries out gas solid separation in the separator.Semicoke returns mixing tank again, so circulation.Volatile matter from mixing tank is overflowed through dedusting, condensation and cooling, recovery oils, obtains the higher coal gas of calorific value.
Current, coal resolving device commonly used mainly is to have two kinds, and row is a kind of to be the shaft furnace structure, and the inflammable gas that this structure combustion product gases and coal produce makes that the purity of combustible gas is low, and added value is low, also has part to discharge, and causes a large amount of wastes of resource and the pollution of environment.Another kind of shaft kiln is that coal cinder is placed on the dividing plate with holes, coal cinder top row well heater, because of the coal cinder on the dividing plate has certain ulking thickness, can not be by even heating, decomposition, need heat, decompose with the gas circulation that is decomposed, what is more important, because a large amount of existence of coal dividing plate cocycle ventilating pit, coal dust can leak down from ventilating pit, so coal dust need be processed coal-forming group earlier when coal dust need enter shaft kiln, separate so coal dust can not be directly used in the kiln body, this has just correspondingly increased the cost that coal dust decomposes, and has reduced economic benefit.
Summary of the invention
The present invention is for solving the problem that exists in above-mentioned technology and the method, proposed a kind of can be directly with the coal dust separating substances, improve its comprehensive utilization value, energy-saving and emission-reduction, thereby the interior coal external-heat coal material decomposition equipment that improves the economic and social benefits.
Coal external-heat coal material decomposition equipment in a kind of, comprise a sealing kiln body, the coal material is set in the described kiln body advances the decomposition pipeline, described coal material advances and decomposes pipeline coal inlet, coal outlet and the branch collection tube of venting one's spleen is set, described coal material advances to decompose between pipeline and the kiln body inwall heat exchange storehouse is set, described heat exchange storehouse is communicated with the high-temperature gas heating arrangements, and described heat exchange storehouse is provided with the heat air delivery line.
Described high-temperature gas heating arrangements comprises fuel supply pipe, air supply pipe and combustion chamber.
Described high-temperature gas heating arrangements is arranged in the kiln body.
It is external that described high-temperature gas heating arrangements is arranged on kiln.
Described high-temperature gas heating arrangements is an electrically heated mechanism.
Described coal material advances the decomposition pipeline to be made up of many parallel solid matter pipelines, and described many parallel solid matter pipeline one ends are provided with distribution plate, and described distribution plate is communicated with described coal inlet, and dish is converged in the other end setting, and the described dish that converges is communicated with coal outlet.
The described branch collection tube gas aftertreatment mechanism external with being arranged on kiln of venting one's spleen is connected.
Because the present invention will establish back of the body coal material and advance the decomposition pipeline in high temperature kiln body, a large amount of high-temperature gases surrounds the coal material and advances decomposition pipeline and conduction in the high temperature kiln body, being radiated the coal material advances on the coal dust that decomposes in the pipeline, coal dust absorbs fully, coal dust heats up and decomposes, and in advancing separating pipe, the coal material resolves into combustion gas, the coal that tar gas and calorific value are higher, combustion gas and tar gas are connected by the described branch external gas aftertreatment mechanism of collection tube and kiln of venting one's spleen, with the combustion gas that decomposes, tar gas is collected, dedusting, separate, pressurized liquefied, perhaps otherwise utilize, the higher coal of calorific value flows out from coal outlet.
The high-temperature gas heating arrangements is arranged on the outside of kiln body, reach the operation of controlledization of dangerous position, improved device ', easy access and maintenance, it is produced in addition and packaging technology is the simplification state than prior art, and reliability and stability further strengthens.Gas to the coal material heats heats the intravital coal of kiln with the form circulation of gas, and heat energy further makes full use of on the one hand, has also reduced the exhaust gas discharging amount in addition.The high-temperature gas heating arrangements is arranged on the inside of kiln body, and the heat energy of generation directly advances separating pipe to contact with the coal material, and heat scatters and disappears few.Help improving the utilization ratio of heat energy.
The energy is fully saved and utilized to device disclosed by the invention with fine coal decomposition and separation quickly and efficiently, improved the utilization ratio of coal resource widely and utilized level, will bring a large amount of economic benefits and social benefit for entire society.
Description of drawings:
The present invention is described further below in conjunction with accompanying drawing:
Fig. 1 is the structural representation of embodiments of the invention one.
Fig. 2 is the structural representation of embodiments of the invention two.
Embodiment:
Embodiment one
As shown in Figure 1: coal external-heat coal material decomposition equipment in a kind of, comprise a sealing rotary kiln body 1, the coal material is set in the described kiln body 1 advances decomposition pipeline 4, described coal material advances and decomposes pipeline 4 coal inlet 2, coal outlet 3 and the branch collection tube 5 of venting one's spleen is set, described coal material advances to decompose between pipeline 4 and kiln body 1 inwall heat exchange storehouse 6 is set, and described heat exchange storehouse 6 is provided with heat air delivery line 7.Described high-temperature gas heating arrangements comprises fuel supply pipe 8, air supply pipe 9 and combustion chamber 10.It is external that described high-temperature gas heating arrangements is arranged on kiln.Combustion chamber 10 is communicated with heat exchange storehouse 6.The described branch collection tube 5 gas aftertreatment mechanism 11 outer with being arranged on kiln body 1 of venting one's spleen is connected, and gas aftertreatment mechanism 1 makes gas fitting, also can be dedusting, removal of impurities, desulfurization, pressurized liquefied device.Described coal material advances and decomposes pipeline 4 and is made up of many parallel solid matter pipelines, and described many parallel solid matter pipeline one ends are provided with distribution plate 12, and described distribution plate 12 is communicated with described coal inlet 2, and the other end setting is converged and coiled 13, and described converging coiled 13 and be communicated with coal outlet 3.Described coal material advances to decompose outside the pipeline 4 can set up heat-conducting plate to improve its thermal conduction capability.
Embodiment two
As shown in Figure 2: coal external-heat coal material decomposition equipment in a kind of, comprise a sealing rotary kiln body 1, the coal material is set in the described kiln body 1 advances decomposition pipeline 4, described coal material advances and decomposes pipeline 4 coal inlet 2, coal outlet 3 and the branch collection tube 5 of venting one's spleen is set, described coal material advances to decompose between pipeline 4 and kiln body 1 inwall heat exchange storehouse 6 is set, and described heat exchange storehouse 6 is provided with heat air delivery line 7.Described high-temperature gas heating arrangements comprises fuel supply pipe 8, air supply pipe 9 and combustion chamber 10.Described high-temperature gas heating arrangements is arranged on kiln body inside, and described combustion chamber 10 is communicated with heat exchange storehouse 6, and fuel supply pipe 8, that air supply pipe 9 stretches out kiln is external.The described branch collection tube 5 gas aftertreatment mechanism 11 outer with being arranged on kiln body 1 of venting one's spleen is connected, and gas aftertreatment mechanism 1 makes gas fitting, also can be dedusting, removal of impurities, desulfurization, pressurized liquefied device.Described coal material advances and decomposes pipeline 4 and is made up of many parallel solid matter pipelines, and described many parallel solid matter pipeline one ends are provided with distribution plate 12, and described distribution plate 12 is communicated with described coal inlet 2, and the other end setting is converged and coiled 13, and described converging coiled 13 and be communicated with coal outlet 3.Described coal material advances to decompose outside the pipeline 4 can set up heat-conducting plate to improve its thermal conduction capability.
Claims (8)
1. coal external-heat coal material decomposition equipment in one kind, comprise a sealing kiln body, it is characterized in that: the coal material is set in the described kiln body advances the decomposition pipeline, described coal material advances and decomposes pipeline coal inlet, coal outlet and the branch collection tube of venting one's spleen is set, described coal material advances to decompose between pipeline and the kiln body inwall heat exchange storehouse is set, described heat exchange storehouse is communicated with the high-temperature gas heating arrangements, and described heat exchange storehouse is provided with the heat air delivery line.
2. coal external-heat coal material decomposition equipment in as claimed in claim 1, it is characterized in that: described high-temperature gas heating arrangements comprises fuel supply pipe, air supply pipe and combustion chamber.
3. coal external-heat coal material decomposition equipment in as claimed in claim 1 or 2, it is characterized in that: described high-temperature gas heating arrangements is arranged in the kiln body.
4. coal external-heat coal material decomposition equipment in as claimed in claim 1 or 2, it is characterized in that: it is external that described high-temperature gas heating arrangements is arranged on kiln.
5. coal external-heat coal material decomposition equipment in as claimed in claim 1 or 2, it is characterized in that: described coal material advances the decomposition pipeline to be made up of many parallel solid matter pipelines, described many parallel solid matter pipeline one ends are provided with distribution plate, described distribution plate is communicated with described coal inlet, dish is converged in the other end setting, and the described dish that converges is communicated with coal outlet.
6. coal external-heat coal material decomposition equipment in as claimed in claim 3, it is characterized in that: described coal material advances the decomposition pipeline to be made up of many parallel solid matter pipelines, described many parallel solid matter pipeline one ends are provided with distribution plate, described distribution plate is communicated with described coal inlet, dish is converged in the other end setting, and the described dish that converges is communicated with coal outlet.
7. coal external-heat coal material decomposition equipment in as claimed in claim 4, it is characterized in that: described coal material advances the decomposition pipeline to be made up of many parallel solid matter pipelines, described many parallel solid matter pipeline one ends are provided with distribution plate, described distribution plate is communicated with described coal inlet, dish is converged in the other end setting, and the described dish that converges is communicated with coal outlet.The described branch collection tube gas aftertreatment mechanism external with being arranged on kiln of venting one's spleen is connected.
8. coal external-heat coal material decomposition equipment in as claimed in claim 4, it is characterized in that: described high-temperature gas heating arrangements is an electrically heated mechanism.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201010527779A CN101984018B (en) | 2010-10-26 | 2010-10-26 | External heating internal coal decomposing equipment |
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| Application Number | Priority Date | Filing Date | Title |
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| CN201010527779A CN101984018B (en) | 2010-10-26 | 2010-10-26 | External heating internal coal decomposing equipment |
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| CN101984018A true CN101984018A (en) | 2011-03-09 |
| CN101984018B CN101984018B (en) | 2012-08-29 |
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| CN201010527779A Active CN101984018B (en) | 2010-10-26 | 2010-10-26 | External heating internal coal decomposing equipment |
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Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104017592A (en) * | 2014-05-27 | 2014-09-03 | 中国重型机械研究院股份公司 | Multitube heating rotary pulverized coal pyrolysis system |
| CN104789241A (en) * | 2015-03-31 | 2015-07-22 | 长安大学 | Rotary furnace for pyrolyzing pulverized coal |
| CN104845648A (en) * | 2015-05-05 | 2015-08-19 | 郭秀梅 | Internal-coal external-heating type low-rank coal quality-improving pyrolysis equipment |
| CN104845647A (en) * | 2015-05-05 | 2015-08-19 | 郭秀梅 | Low-rank coal quality-improving pyrolysis equipment |
| CN105316015A (en) * | 2014-05-31 | 2016-02-10 | 肖自江 | Upper-heating down-moving low-temperature pyrolysis furnace for powdered coal and oil shale powder |
| CN106281381A (en) * | 2016-09-12 | 2017-01-04 | 新疆广汇中化能源技术开发有限公司 | Rotatable radiation bed |
| CN106584703A (en) * | 2016-11-30 | 2017-04-26 | 重庆精榜高分子材料有限公司 | Powder processing device |
| CN112299416A (en) * | 2019-08-02 | 2021-02-02 | 中冶长天国际工程有限责任公司 | Rotary activation furnace, activated carbon production system and activated carbon production method |
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| CN2676124Y (en) * | 2004-02-18 | 2005-02-02 | 中国石油化工股份有限公司 | Continuous rotary-drum furnace |
| JP2005213591A (en) * | 2004-01-29 | 2005-08-11 | Jfe Steel Kk | Method for blowing solid fuel into blast furnace and blowing lance |
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| CN2229455Y (en) * | 1995-05-12 | 1996-06-19 | 荆太安 | Coal dry distillation furnace |
| JP2005213591A (en) * | 2004-01-29 | 2005-08-11 | Jfe Steel Kk | Method for blowing solid fuel into blast furnace and blowing lance |
| CN2676124Y (en) * | 2004-02-18 | 2005-02-02 | 中国石油化工股份有限公司 | Continuous rotary-drum furnace |
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Cited By (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104017592A (en) * | 2014-05-27 | 2014-09-03 | 中国重型机械研究院股份公司 | Multitube heating rotary pulverized coal pyrolysis system |
| CN105316015A (en) * | 2014-05-31 | 2016-02-10 | 肖自江 | Upper-heating down-moving low-temperature pyrolysis furnace for powdered coal and oil shale powder |
| CN105316015B (en) * | 2014-05-31 | 2017-12-01 | 肖自江 | The descending low temperature pyrogenation stove of heat on fine coal oil shale powder |
| CN104789241A (en) * | 2015-03-31 | 2015-07-22 | 长安大学 | Rotary furnace for pyrolyzing pulverized coal |
| CN104845648A (en) * | 2015-05-05 | 2015-08-19 | 郭秀梅 | Internal-coal external-heating type low-rank coal quality-improving pyrolysis equipment |
| CN104845647A (en) * | 2015-05-05 | 2015-08-19 | 郭秀梅 | Low-rank coal quality-improving pyrolysis equipment |
| CN106281381A (en) * | 2016-09-12 | 2017-01-04 | 新疆广汇中化能源技术开发有限公司 | Rotatable radiation bed |
| CN106584703A (en) * | 2016-11-30 | 2017-04-26 | 重庆精榜高分子材料有限公司 | Powder processing device |
| CN112299416A (en) * | 2019-08-02 | 2021-02-02 | 中冶长天国际工程有限责任公司 | Rotary activation furnace, activated carbon production system and activated carbon production method |
| CN112299416B (en) * | 2019-08-02 | 2022-06-14 | 中冶长天国际工程有限责任公司 | Rotary activation furnace, activated carbon production system and activated carbon production method |
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| CN101984018B (en) | 2012-08-29 |
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Owner name: HEBEI LONGCHENG COAL COMPREHENSIVE UTILIZATION CO. Free format text: FORMER OWNER: XIXIA LONGCHENG SPECIAL MATERIAL CO., LTD. Effective date: 20150215 |
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Free format text: CORRECT: ADDRESS; FROM: 474500 NANYANG, HENAN PROVINCE TO: 063200 TANGSHAN, HEBEI PROVINCE |
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Effective date of registration: 20150215 Address after: 063200 chemical industry zone, Caofeidian Industrial Zone, Caofeidian District, Hebei, Tangshan City Patentee after: Comprehensive utilization Co. Ltd. Hebei dragon Chengmei Address before: 474500, Xixia County, Henan province Nanyang County Industrial Park Patentee before: Xixia Longcheng Special Material Co., Ltd. |
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Effective date of registration: 20200201 Address after: 474571, Henan County, Nanyang province Xixia County town of red stone village industrial agglomeration area Patentee after: Henan Dragon into Coal Technology Co.,Ltd. Address before: 063200 chemical industry zone, Caofeidian Industrial Zone, Caofeidian District, Hebei, Tangshan City Patentee before: Comprehensive utilization Co. Ltd. Hebei dragon Chengmei |