CN1417289A - Double-section dry coal powder gasifying furnace - Google Patents
Double-section dry coal powder gasifying furnace Download PDFInfo
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- CN1417289A CN1417289A CN01131780A CN01131780A CN1417289A CN 1417289 A CN1417289 A CN 1417289A CN 01131780 A CN01131780 A CN 01131780A CN 01131780 A CN01131780 A CN 01131780A CN 1417289 A CN1417289 A CN 1417289A
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/10—Process efficiency
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Abstract
The gasifying furnace includes two, upper and lower, sections of hearth. In the lower section, 80% of the dry coal powder is subjected to gasification reaction with oxygen and steam; and in the upper section, about 20% of the dry coal powder and steam are sprayed and are subjected to thermal decomposition and gasification with the high temperature gas produced in the lower hearth section and to increase the inflammable component of gas and raise the heat value of gas while cooling high temperature gas to solidify and separate the molten slag. The furnace of the present invention has higher carbon conversion, cold gas efficiency and total heat efficiency compared with prior gasifying furnace, and its product is suitable for use in gas power generation and chemical synthesis.
Description
Content of the present invention belongs to the coal gasification apparatus field, relates to a kind of dry coal dust gasification furnace.
In the prior art, Holland Shell and German Prenflo vapourizing furnace are the gasification installation with the charging of dry coal powder form, but they have only the one-level gasification reaction, in order to allow the molten state lime-ash in the coal gas of high temperature solidify in order to avoid gas cooler is stopped up, have to adopt cooled coal gas a large amount of in the subsequent technique that coal gas of high temperature is carried out chilling, can make coal gas of high temperature be cooled to 900 ℃ by 1400 ℃, its calorific loss is very big, and indexs such as the efficiency of carbon conversion of vapourizing furnace, cold gas efficiency and overall thermal efficiency are all lower.
The objective of the invention is to overcome the shortcoming of prior art, the double-section dry coal powder gasifying furnace that a kind of rational in infrastructure, long service life is provided and has higher carbon transformation efficiency, cold gas efficiency and overall thermal efficiency.
The technical solution that adopts is so for achieving the above object: the double-section dry coal powder gasifying furnace that is provided has that the upper furnace of a upper end band gas exit and one are communicated with upper furnace and the lower hearth of lower end band cinder notch, symmetry has four fine coal, water and oxygen inlet on the lower hearth sidewall, symmetry has two secondary fine coal and water inlet on the sidewall of upper furnace, is provided with slag cooling pool and dreg removing system at bottom of furnace body.
Compared with prior art, innovative point of the present invention is: gasification hearth is divided into two sections, at lower hearth section (first reaction zone), about 80% dry coal powder and oxygen and vapor generation gasification reaction, at upper furnace section (second reaction zone), spray into about 20% dry coal powder and steam, the coal gas of high temperature that generates with the lower hearth section carries out pyrolysis and gasification reaction, the combustiblecomponents of coal gas is increased, calorific value improves, make coal gas of high temperature obtain cooling simultaneously, so that the molten state lime-ash in the coal gas solidifies also and then separates from coal gas.The efficiency of carbon conversion of this vapourizing furnace, cold gas efficiency and overall thermal efficiency be all than existing all kinds of vapourizing furnace height, coal applied widely, and its product is applicable to systems such as coal gasification power generation, chemical industry are synthetic.
Below with reference to accompanying drawing content of the present invention is described further.
Fig. 1 is the structural representation of a specific embodiment of invention.
Fig. 2 implements the schema of coal gasifying process for adopting device of the present invention.
Referring to accompanying drawing, the shell of this vapourizing furnace is a upright cylinder, burner hearth is divided into two sections of upper furnace I and lower hearth II, lower hearth II is first reaction zone, is the wide cavity in narrow centre, two ends, and gas is average the stop 5 seconds in thorax, the import 2 that four symmetric is used to import fine coal, water and oxygen is located at the two side of lower hearth, cinder notch 11 is located at lower hearth bottom high temperature section, adopts slag tap, is arranged with the coil tube type water wall 12 that is used for the recovery part heat on lower hearth II inner-wall surface; Upper furnace I is second reaction zone, and its internal diameter is little than the internal diameter of lower hearth II, and is highly longer, has two symmetric secondary fine coal and water inlet 5 on the sidewall of upper furnace I, also is provided with the water wall 9 that is used to reclaim heat simultaneously on upper furnace I inner-wall surface.During work, spray into dry coal powder, oxygen (pure oxygen or oxygen enrichment) and steam by the vapourizing furnace hypomere, the coal dust amount that is sprayed into accounts for 80～85% of total coal amount, and 5 places spray into the fine coal that superheated vapour is carried secretly in the upper furnace import, and institute's straying quatity accounts for 15～20% of total coal amount.The effect of epimere stove mainly contains two in this device: the first replaces the circulation synthetic gas to make the coal gas of temperature up to 1400 ℃ be chilled to about 900 ℃, second it is to utilize hypomere producer gas sensible heat to carry out thermo-cracking and partial gasification, improves total cold gas efficiency and thermo-efficiency.Sequence number 1 is an entrance of cooling water among Fig. 1; 3 is cooling water outlet; 4 is the feedwater import; 6 is gas exit; 7 remove drum for steam; 8 is upper header; 10 is lower collecting box.
The gasifying process flow process of implementing according to the present invention is as shown in Figure 2: at first the dry coal powder enters non-pressurized coal dust cyclone 13, makes coal dust and nitrogen separation, and coal dust enters in the normal pressure powder storehouse 14; The nitrogen that has a small amount of coal dust separates the back to coal dust by coal dust strainer 12 to be continued to use, and nitrogen then is drained; After this coal dust falls into transformation jar 16 behind fine coal weighing hopper 15, then to transformation jar 16 input highly compressed nitrogen, coal dust is pressed in the pressurized tank 17, coal dust is delivered in the high pressure nitrogen transfer lime by the quantitative relation of strictness by worm conveyor (auger) 18 again, utilized high pressure nitrogen that coal dust is delivered in the vapourizing furnace and go; In the exit of auger, coal dust sprays among the burner hearth II of vapourizing furnace hypomere and carries out gasification reaction with the oxygen G﹠W that sprays into simultaneously, and the amount of the coal dust that this reaction zone sprays into accounts for 80～85% of total amount; At the epimere reaction zone I of body of heater, the dry method coal dust supply system through similar to the above sprays into remaining 15～20% coal dusts and a part of overheated steam, and the high temperature sensible heat of using from the first reaction zone II carries out hot tearing and gasification reaction; In the vapourizing furnace burner hearth, most of ash flows into the slag ladle 23 of vapourizing furnace bottom after fusing, be condensed into particulate state in jar, pulls out by dragveyer at last.Sequence number 19 is normal pressure powder storehouse among Fig. 2; 20 is the transformation jar; 21 is pressurized tank; 22 is worm conveyor.
Claims (3)
1, a kind of double-section dry coal powder gasifying furnace, it is characterized in that having that the upper furnace (I) of a upper end band gas exit (6) and one are communicated with upper furnace (I) and the lower hearth (II) of lower end band cinder notch (11), symmetry has four fine coal, water and oxygen inlet (2) on lower hearth (II) sidewall, symmetry has two secondary fine coal and water inlet (5) on the sidewall of upper furnace (I), is provided with slag cooling pool and dreg removing system at bottom of furnace body.
2, double-section dry coal powder gasifying furnace as claimed in claim 1 is characterized in that being arranged with coil tube type water wall (12) on lower hearth (II) inner-wall surface, is provided with water wall (9) on upper furnace (I) inner-wall surface.
3, double-section dry coal powder gasifying furnace as claimed in claim 1 is characterized in that the internal diameter of the internal diameter of upper furnace (I) less than lower hearth (II).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB011317809A CN1226395C (en) | 2001-11-08 | 2001-11-08 | Double-section dry coal powder gasifying furnace |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB011317809A CN1226395C (en) | 2001-11-08 | 2001-11-08 | Double-section dry coal powder gasifying furnace |
Publications (2)
| Publication Number | Publication Date |
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| CN1417289A true CN1417289A (en) | 2003-05-14 |
| CN1226395C CN1226395C (en) | 2005-11-09 |
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| Application Number | Title | Priority Date | Filing Date |
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| CNB011317809A Expired - Fee Related CN1226395C (en) | 2001-11-08 | 2001-11-08 | Double-section dry coal powder gasifying furnace |
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Cited By (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102071065A (en) * | 2011-01-26 | 2011-05-25 | 东方电气集团东方锅炉股份有限公司 | Back flow coal gasification device |
| CN101392191B (en) * | 2008-10-15 | 2011-11-23 | 合肥工业大学 | Two stage type dry coal powder entrained flow gasifier |
| CN102660329A (en) * | 2012-05-08 | 2012-09-12 | 神华集团有限责任公司 | Two-stage entrained bed solid slagging gasifying device, gasifying method for carbon-containing substance and application of gasifying device |
| CN102911740A (en) * | 2012-09-28 | 2013-02-06 | 上海锅炉厂有限公司 | Two-section gasifying device of entrained-flow bed and gasifying method of two-section gasifying device |
| CN101547997B (en) * | 2007-01-17 | 2013-03-27 | 国际壳牌研究有限公司 | Gasification reactor |
| CN103173247A (en) * | 2013-04-12 | 2013-06-26 | 邰学林 | Compound type furnace body of slag coal gasification furnace |
| CN103703111A (en) * | 2011-07-25 | 2014-04-02 | 新日铁住金工程技术株式会社 | Method for producing coal gas and method for producing methane |
| CN104987890A (en) * | 2015-07-01 | 2015-10-21 | 安徽科达洁能股份有限公司 | Gas production method and device |
| CN105925313A (en) * | 2016-07-17 | 2016-09-07 | 昆明新能源发展有限公司 | Carbon dioxide/coal coke gasification method and device thereof |
| CN113565681A (en) * | 2021-08-09 | 2021-10-29 | 国网浙江省电力有限公司电力科学研究院 | Coupling system using electric heating gasification furnace and multi-energy conversion method thereof |
-
2001
- 2001-11-08 CN CNB011317809A patent/CN1226395C/en not_active Expired - Fee Related
Cited By (13)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101547997B (en) * | 2007-01-17 | 2013-03-27 | 国际壳牌研究有限公司 | Gasification reactor |
| CN101392191B (en) * | 2008-10-15 | 2011-11-23 | 合肥工业大学 | Two stage type dry coal powder entrained flow gasifier |
| CN102071065A (en) * | 2011-01-26 | 2011-05-25 | 东方电气集团东方锅炉股份有限公司 | Back flow coal gasification device |
| CN103703111A (en) * | 2011-07-25 | 2014-04-02 | 新日铁住金工程技术株式会社 | Method for producing coal gas and method for producing methane |
| CN103703111B (en) * | 2011-07-25 | 2015-07-08 | 新日铁住金工程技术株式会社 | Method for producing coal gas and method for producing methane |
| CN102660329A (en) * | 2012-05-08 | 2012-09-12 | 神华集团有限责任公司 | Two-stage entrained bed solid slagging gasifying device, gasifying method for carbon-containing substance and application of gasifying device |
| CN102660329B (en) * | 2012-05-08 | 2013-11-20 | 神华集团有限责任公司 | Two-stage entrained bed solid slagging gasifying device, gasifying method for carbon-containing substance and application of gasifying device |
| CN102911740A (en) * | 2012-09-28 | 2013-02-06 | 上海锅炉厂有限公司 | Two-section gasifying device of entrained-flow bed and gasifying method of two-section gasifying device |
| CN103173247A (en) * | 2013-04-12 | 2013-06-26 | 邰学林 | Compound type furnace body of slag coal gasification furnace |
| CN104987890A (en) * | 2015-07-01 | 2015-10-21 | 安徽科达洁能股份有限公司 | Gas production method and device |
| CN104987890B (en) * | 2015-07-01 | 2018-07-31 | 安徽科达洁能股份有限公司 | Coal gas production method and equipment |
| CN105925313A (en) * | 2016-07-17 | 2016-09-07 | 昆明新能源发展有限公司 | Carbon dioxide/coal coke gasification method and device thereof |
| CN113565681A (en) * | 2021-08-09 | 2021-10-29 | 国网浙江省电力有限公司电力科学研究院 | Coupling system using electric heating gasification furnace and multi-energy conversion method thereof |
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| Publication number | Publication date |
|---|---|
| CN1226395C (en) | 2005-11-09 |
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Granted publication date: 20051109 |