CN104357066A - Small flue structure with multiple independently controllable airflow channels - Google Patents
Small flue structure with multiple independently controllable airflow channels Download PDFInfo
- Publication number
- CN104357066A CN104357066A CN201410635857.0A CN201410635857A CN104357066A CN 104357066 A CN104357066 A CN 104357066A CN 201410635857 A CN201410635857 A CN 201410635857A CN 104357066 A CN104357066 A CN 104357066A
- Authority
- CN
- China
- Prior art keywords
- bottom flue
- wall
- regenerator
- small flue
- flue
- 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.)
- Granted
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10B—DESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
- C10B21/00—Heating of coke ovens with combustible gases
- C10B21/10—Regulating and controlling the combustion
- C10B21/16—Regulating and controlling the combustion by controlling or varying the openings between the heating flues and the regenerator flues
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10B—DESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
- C10B21/00—Heating of coke ovens with combustible gases
- C10B21/02—Heating of coke ovens with combustible gases with lean gas
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Combustion & Propulsion (AREA)
- Materials Engineering (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Organic Chemistry (AREA)
- Coke Industry (AREA)
Abstract
The invention relates to a small flue structure with multiple independently controllable airflow channels. The small flue structure comprises a small flue composed of a regenerative chamber main wall and a regenerative chamber single wall; the interior of the small flue is divided into a plurality of layers in the height direction; a small flue transverse partition wall is arranged in the middle of each layer; airflow channels composed of small flue lining bricks, small flue horizontal partition walls/small flue bottom pavement bricks and the small flue transverse partition walls are communicated with regenerative chamber compartments to form independent airflow channels, respectively; and a regulator is arranged at the inlet of each airflow channel. Compared with the prior art, the small flue structure with multiple independently controllable airflow channels has the following beneficial effects that 1) the small flue is divided into a plurality of air channels so as to realize accurate air division control on lean gas/air for coke oven heating at the outside, and the homogeneity and the accuracy of temperature distribution in the length direction of a combustion chamber are improved; 2) automatic control can be realized, the operating environment is improved and the labor intensity is reduced; and 3) the amount of a combustion-supporting gas going into each regenerative chamber compartment can be regulated accurately, and therefore, the energy source utilization rate is increased, the energy is saved and the consumption is reduced.
Description
Technical field
The present invention relates to inflammable gas and air side entering type coke oven technical field, particularly relate to and a kind of there is multiple bottom flue structure that independently can control gas channel.
Background technology
Along with the development that coke oven maximizes, the height of coke oven combustion chamber-coking chamber is more and more higher, and the thickness of corresponding furnace roof also increases thereupon, and the difficulty carrying out regulating from furnace roof is also increasing, even can not regulate.In addition, because throat temperature is higher, the adjustment means of normal work under the environment more than 1300 DEG C can also become the development bottleneck of this traditional regulative mode, therefore be difficult to realize carrying out coke oven length to adjustment at furnace roof.
" M " of nippon company is although Formed Coke Furnace achieves the mode accurately being controlled tolerance by outside baffle system, but because intake ducting stretches out double-edged fine-toothed comb brick, seriously corroded, within about about 5 years, just need to change pipeline, in repair that to change pipeline waste quite large, and the air supply modes in this regulative mode adopts is the mode of forced-air blast, and production cost is high, furnace roof quirk malleation is large, thermometric difficulty.In addition, this regulative mode exist uncontrollable coke oven length to the shortcoming such as air flow quantity distribution.
Mode lowered by the domestic coke oven generally adopted at present is the structure adopting double-edged fine-toothed comb brick-adjusting brick, regulates the aperture of double-edged fine-toothed comb brick adjustable port to realize controlling along the distribution of air flow in cokery side direction by regulating the thickness of adjusting brick.But it is large that the shortcoming of which is workload, due to the deposition of the dust such as blast-furnace dust cause adjustment hole to open while the heavy contamination of dust, the poor working environment of workman.
See Fig. 1, commonly use bottom flue structural representation at present, its bottom flue main structure is made up of regenerator main wall 6 and regenerator list wall 7, middle part forms the elongated gas channel of an entirety by bottom flue lining brick 4, and establish grate brick to carry out separating and regulating between regenerator, this kind of structure cannot adjust separately the gas flow entering the little lattice of regenerator.
Summary of the invention
The invention provides and a kind of there is multiple bottom flue structure that independently can control gas channel, accurate tolerance flow-dividing control can be carried out to the low-grade gas/air of heating coke-oven in outside, improve combustion chamber length to the homogeneity of temperature distribution and accuracy; The present invention is accurately easy to adjust, and can realize automatic control, improves operating environment, reduces labor intensity, and increases work efficiency and security.
In order to achieve the above object, the present invention realizes by the following technical solutions:
There is multiple bottom flue structure that independently can control gas channel, comprise the bottom flue be made up of regenerator main wall and regenerator list wall, bottom flue is inner along high to being divided into several layers, the horizontal dividing wall of bottom flue is established in every layer of centre, the gas channel be made up of bottom flue lining brick, bottom flue horizontal subdivision wall/bottom flue shop fixtures brick, the horizontal dividing wall of bottom flue respectively lattice little of regenerator is communicated with and forms individual air stream passage, and each gas channel ingress is equipped with setting device.
Described bottom flue horizontal subdivision wall is from top to bottom arranged in ladder along the corresponding little partition wall place of regenerator of gas inflow direction, arranges with bottom flue horizontal subdivision wall interval, layer both sides.
Described bottom flue horizontal subdivision wall is connected with the little partition wall of regenerator by the little partition wall of bottom flue at corresponding regenerator little partition wall place, forms gas buffer chamber in its junction by bottom flue lining brick, the little partition wall/regenerator of bottom flue little partition wall/heating system center partition, bottom flue horizontal subdivision wall/bottom flue shop fixtures brick.
Described setting device is manual regulation flap valve or self-acting valve plate valve.
Compared with prior art, the invention has the beneficial effects as follows:
1) by being separated to form multiple gas passage to bottom flue, and then realizing carrying out accurate tolerance flow-dividing control to the low-grade gas/air of heating coke-oven in outside, improve combustion chamber length to the homogeneity of temperature distribution and accuracy;
2) automatic control can be realized, improve operating environment, reduce labor intensity, increase work efficiency and security;
3) gas flow of the little lattice of each regenerator can be entered by fine adjustment, improve energy utilization rate, energy-saving and cost-reducing.
Accompanying drawing explanation
Fig. 1 is conventional bottom flue structural representation.
Fig. 2 structural representation of the present invention.
Fig. 3 is the A-A sectional view of Fig. 2;
Fig. 4 is the B-B sectional view of Fig. 2;
In figure: 1. the little partition wall of horizontal dividing wall 3. bottom flue little partition wall 4. bottom flue lining brick 5. bottom flue shop fixtures brick 6. regenerator main wall 7. regenerator list wall 8. air-flow buffer chamber 9. bottom flue gas channel 10. setting device 11. heating system center partition 12. regenerator of bottom flue horizontal subdivision wall 2. bottom flue
Embodiment
Below in conjunction with accompanying drawing, the specific embodiment of the present invention is described further:
See Fig. 2-Fig. 4, it is structural representation of the present invention, the present invention has multiple bottom flue structure that independently can control gas channel, comprise the bottom flue be made up of regenerator main wall 6 and regenerator list wall 7, bottom flue is inner along high to being divided into several layers, the horizontal dividing wall 2 of bottom flue is established in every layer of centre, the gas channel 9 be made up of bottom flue lining brick 4, bottom flue horizontal subdivision wall 1/ bottom flue shop fixtures brick 5, the horizontal dividing wall 2 of bottom flue respectively lattice little of regenerator is communicated with and forms individual air stream passage, and each gas channel 9 ingress is equipped with setting device 10.
Described bottom flue horizontal subdivision wall 1 is from top to bottom arranged in ladder along the corresponding little partition wall place 12 of regenerator of gas inflow direction, arranges with bottom flue horizontal subdivision wall 1 interval, layer both sides.
Described bottom flue horizontal subdivision wall 1 is connected by the little partition wall 12 of the little partition wall of bottom flue 3 and regenerator at corresponding regenerator little partition wall 12 place, forms gas buffer chamber in its junction by bottom flue lining brick 4, bottom flue little partition wall 3/ regenerator little partition wall 12/ heating system center partition 11, bottom flue horizontal subdivision wall/1 bottom flue shop fixtures brick 5.
Described setting device 10 is manual regulation flap valve or self-acting valve plate valve.
The present invention has multiple bottom flue structure that independently can control gas channel, bottom flue is all separated from height to longitudinal, the little lattice of each regenerator are made all to have independent air passageways 9 to be communicated with, and can low-grade gas outside bottom flue or gas inlet place establish setting device 10 to regulate separately, easily be automated adjustment, solve coke oven length to the difficult problem regulated.
Following examples are implemented under premised on technical solution of the present invention, give detailed embodiment and concrete operating process, but protection scope of the present invention are not limited to following embodiment.In following embodiment, method therefor is ordinary method if no special instructions.
[embodiment 1]
Seeing Fig. 2, is the structural representation of the present embodiment.Bottom flue forms agent structure by regenerator main wall 6 and regenerator list wall 7, therein by bottom flue horizontal subdivision wall 1 by it along high to being divided into 5 layers, and below 4 layers be divided into 2 cells by the horizontal dividing wall 2 of bottom flue in centre again.See Fig. 3, it is the A-A sectional view of Fig. 2, along coke oven length to finding out, the bottom flue horizontal subdivision wall 1 of the superiors is routed near bottom flue ingress second regenerator little partition wall 12 place, second layer bottom flue horizontal subdivision wall 1 is routed to the 4th road regenerator little partition wall 12 place, the rest may be inferred, and bottom flue horizontal subdivision wall 1 is arranged along corresponding regenerator little partition wall 12 interval of bottom flue length direction, at the medium and small air flue horizontal dividing wall 1 of sectional view in stepped appearance.See Fig. 4, it is the B-B sectional view of Fig. 2, along coke oven length to finding out, the bottom flue horizontal subdivision wall 1 of the superiors is routed near bottom flue ingress first regenerator little partition wall 12 place, second layer bottom flue horizontal subdivision wall 1 is routed to the 3rd road regenerator little partition wall 12 place, the rest may be inferred, and bottom flue horizontal subdivision wall 1 is arranged, at the medium and small air flue horizontal dividing wall 1 of sectional view equally in stepped appearance along corresponding regenerator little partition wall 12 interval of bottom flue length direction.
Low-grade gas or air enter bottom flue from multiple gas channel entrance by variable valve 10, enter the little lattice of corresponding regenerator along gas channel 9 and arrive flue and participate in burning, by the flow of adjustment gas channel inlet adjustment valve 10, the gas flow entering the little lattice of each regenerator can be controlled separately, thus realize coke oven length to adjustment.
Claims (4)
1. there is multiple bottom flue structure that independently can control gas channel, comprise the bottom flue be made up of regenerator main wall and regenerator list wall, it is characterized in that, bottom flue is inner along high to being divided into several layers, the horizontal dividing wall of bottom flue is established in every layer of centre, the gas channel be made up of bottom flue lining brick, bottom flue horizontal subdivision wall/bottom flue shop fixtures brick, the horizontal dividing wall of bottom flue respectively lattice little of regenerator is communicated with and forms individual air stream passage, and each gas channel ingress is equipped with setting device.
2. according to claim 1 have multiple bottom flue structure that independently can control gas channel, it is characterized in that, described bottom flue horizontal subdivision wall is from top to bottom arranged in ladder along the corresponding little partition wall place of regenerator of gas inflow direction, arranges with bottom flue horizontal subdivision wall interval, layer both sides.
3. according to claim 1 have multiple bottom flue structure that independently can control gas channel, it is characterized in that, described bottom flue horizontal subdivision wall is connected with the little partition wall of regenerator by the little partition wall of bottom flue at corresponding regenerator little partition wall place, forms gas buffer chamber in its junction by bottom flue lining brick, the little partition wall/regenerator of bottom flue little partition wall/heating system center partition, bottom flue horizontal subdivision wall/bottom flue shop fixtures brick.
4. according to claim 1 have multiple bottom flue structure that independently can control gas channel, and it is characterized in that, described setting device is manual regulation flap valve or self-acting valve plate valve.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201410635857.0A CN104357066B (en) | 2014-11-12 | 2014-11-12 | There is multiple bottom flue structure that can independently control air-flow passage |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201410635857.0A CN104357066B (en) | 2014-11-12 | 2014-11-12 | There is multiple bottom flue structure that can independently control air-flow passage |
Publications (2)
Publication Number | Publication Date |
---|---|
CN104357066A true CN104357066A (en) | 2015-02-18 |
CN104357066B CN104357066B (en) | 2016-06-08 |
Family
ID=52524384
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201410635857.0A Active CN104357066B (en) | 2014-11-12 | 2014-11-12 | There is multiple bottom flue structure that can independently control air-flow passage |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN104357066B (en) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN107936999A (en) * | 2017-12-22 | 2018-04-20 | 中冶焦耐(大连)工程技术有限公司 | The Bidirectional heating system and heating means of external-heat low order fine coal continuous shale oven |
CN108277022A (en) * | 2018-03-30 | 2018-07-13 | 中冶焦耐(大连)工程技术有限公司 | A kind of top dress makes integrated coking furnace shaft structure and its adjusting method firm by ramming |
CN108728126A (en) * | 2018-07-31 | 2018-11-02 | 中冶焦耐(大连)工程技术有限公司 | It is a kind of high to heating uniformity adjustable coke oven heating system and adjusting method at any time |
CN114907868A (en) * | 2021-02-10 | 2022-08-16 | 西奥多设计公司 | Thermal decomposition method and thermal decomposition apparatus |
Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4431484A (en) * | 1981-05-20 | 1984-02-14 | Firma Carl Still Gmbh & Co. Kg | Heating system for regenerative coke oven batteries |
CN87105045A (en) * | 1987-07-30 | 1988-04-06 | 冶金工业部鞍山焦化耐火材料设计研究院 | Whole lower adjustable installation for heating of coke oven |
CN2605261Y (en) * | 2003-02-14 | 2004-03-03 | 李天瑞 | Heat-accumulated clean type casting coke oven |
CN101979463A (en) * | 2010-10-26 | 2011-02-23 | 山西省化工设计院 | Clean heat reclamation tamping type coke furnace |
CN202016975U (en) * | 2011-02-23 | 2011-10-26 | 中冶焦耐(大连)工程技术有限公司 | Oven body structure capable of adjusting heating uniformity in length direction of oven coke from lower part |
CN203582805U (en) * | 2013-11-29 | 2014-05-07 | 杜晋安 | Outer-heating lignite dry distillation furnace |
CN204265687U (en) * | 2014-11-12 | 2015-04-15 | 中冶焦耐工程技术有限公司 | There is multiple bottom flue structure that independently can control gas channel |
-
2014
- 2014-11-12 CN CN201410635857.0A patent/CN104357066B/en active Active
Patent Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4431484A (en) * | 1981-05-20 | 1984-02-14 | Firma Carl Still Gmbh & Co. Kg | Heating system for regenerative coke oven batteries |
CN87105045A (en) * | 1987-07-30 | 1988-04-06 | 冶金工业部鞍山焦化耐火材料设计研究院 | Whole lower adjustable installation for heating of coke oven |
CN2605261Y (en) * | 2003-02-14 | 2004-03-03 | 李天瑞 | Heat-accumulated clean type casting coke oven |
CN101979463A (en) * | 2010-10-26 | 2011-02-23 | 山西省化工设计院 | Clean heat reclamation tamping type coke furnace |
CN202016975U (en) * | 2011-02-23 | 2011-10-26 | 中冶焦耐(大连)工程技术有限公司 | Oven body structure capable of adjusting heating uniformity in length direction of oven coke from lower part |
CN203582805U (en) * | 2013-11-29 | 2014-05-07 | 杜晋安 | Outer-heating lignite dry distillation furnace |
CN204265687U (en) * | 2014-11-12 | 2015-04-15 | 中冶焦耐工程技术有限公司 | There is multiple bottom flue structure that independently can control gas channel |
Cited By (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN107936999A (en) * | 2017-12-22 | 2018-04-20 | 中冶焦耐(大连)工程技术有限公司 | The Bidirectional heating system and heating means of external-heat low order fine coal continuous shale oven |
CN107936999B (en) * | 2017-12-22 | 2024-03-19 | 中冶焦耐(大连)工程技术有限公司 | Bidirectional heating system and heating method of external heating type low-order pulverized coal continuous carbonization furnace |
CN108277022A (en) * | 2018-03-30 | 2018-07-13 | 中冶焦耐(大连)工程技术有限公司 | A kind of top dress makes integrated coking furnace shaft structure and its adjusting method firm by ramming |
CN108277022B (en) * | 2018-03-30 | 2023-05-16 | 中冶焦耐(大连)工程技术有限公司 | Top-mounted tamping integrated coke oven body structure and adjusting method thereof |
CN108728126A (en) * | 2018-07-31 | 2018-11-02 | 中冶焦耐(大连)工程技术有限公司 | It is a kind of high to heating uniformity adjustable coke oven heating system and adjusting method at any time |
CN108728126B (en) * | 2018-07-31 | 2024-01-30 | 中冶焦耐(大连)工程技术有限公司 | High-directional heating uniformity at any time adjustable coke oven heating system and adjusting method |
CN114907868A (en) * | 2021-02-10 | 2022-08-16 | 西奥多设计公司 | Thermal decomposition method and thermal decomposition apparatus |
CN114907868B (en) * | 2021-02-10 | 2024-04-16 | 西奥多设计公司 | Thermal decomposition method and thermal decomposition device |
Also Published As
Publication number | Publication date |
---|---|
CN104357066B (en) | 2016-06-08 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US6187148B1 (en) | Downcomer valve for non-recovery coke oven | |
CN102046755B (en) | Apparatus for the directed introduction of primary combustion air into the gas space of a coke-oven battery | |
CN104357066B (en) | There is multiple bottom flue structure that can independently control air-flow passage | |
RU2371466C2 (en) | Air-delivery system for burning for coke oven | |
CN204265687U (en) | There is multiple bottom flue structure that independently can control gas channel | |
CN106190184A (en) | A kind of coke oven heating method and device reducing NOx generation | |
CN108277022B (en) | Top-mounted tamping integrated coke oven body structure and adjusting method thereof | |
CN102268266A (en) | Controllable multi-section-combustion heating molded coke oven | |
CN104449768A (en) | Down-regulated vertical flue combustion regulating method and heating system thereof for coke oven combustor | |
CN105385460A (en) | Circulating structure and method for exhaust gas of coke oven | |
CN202116492U (en) | Controllable multi-section combustion heating type coke oven | |
CN103225818B (en) | Secondary air box structure of coal-fired W-flame boiler in power station | |
CN108315022B (en) | Coke oven structure with adjustable crossing hole and crossing hole adjusting method | |
CN103673573A (en) | Straight-through drying oven with air curtain system | |
JPH0127979B2 (en) | ||
CN108329932B (en) | Coke oven structure with adjustable crossing holes and crossing hole adjusting method | |
CN105255504B (en) | A kind of regenerator bottom flue of variable cross-section | |
CN217230611U (en) | Waste gas distribution device of coke oven | |
CN103740381B (en) | Transverse continuous heating system of coke oven | |
CN103922561A (en) | Energy-saving gas glass melting furnace | |
CN204265686U (en) | A kind of heating system of lower regulatable coke oven | |
CN108774537B (en) | Low-nitrogen-emission reheating coke oven heating system and adjusting method thereof | |
CN204187976U (en) | Kiln fired by a kind of blue bricks | |
CN106675584A (en) | Structure and method for adjusting lengthwise air-flow distribution of coke oven by synergizing upper part with lower part | |
CN215250606U (en) | Regenerator small flue structure capable of being adjusted from lower part |
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: 20180731 Address after: 116085 128 high energy street, Qixian Ling high tech Industrial Park, Dalian, Liaoning Patentee after: ACRE Coking And Refractory (Dalian) Engineering Consulting Corp., MCC Address before: 116085 128 high energy street, Qixian Ling high tech Industrial Park, Dalian, Liaoning Patentee before: ACRE Coking and Refractory Engineering Consulting Corporation, MCC |
|
TR01 | Transfer of patent right |