EP0427828A1 - Heating chambers in coke ovens and heating process. - Google Patents
Heating chambers in coke ovens and heating process.Info
- Publication number
- EP0427828A1 EP0427828A1 EP90906914A EP90906914A EP0427828A1 EP 0427828 A1 EP0427828 A1 EP 0427828A1 EP 90906914 A EP90906914 A EP 90906914A EP 90906914 A EP90906914 A EP 90906914A EP 0427828 A1 EP0427828 A1 EP 0427828A1
- Authority
- EP
- European Patent Office
- Prior art keywords
- heating
- internals
- gas
- combustion
- coke ovens
- 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
- 238000010438 heat treatment Methods 0.000 title claims abstract description 43
- 239000000571 coke Substances 0.000 title claims abstract description 12
- 238000002485 combustion reaction Methods 0.000 claims description 26
- 241000264877 Hippospongia communis Species 0.000 claims description 12
- 239000007789 gas Substances 0.000 claims description 9
- 239000003546 flue gas Substances 0.000 claims description 6
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 claims description 4
- 238000000034 method Methods 0.000 claims description 4
- 239000003054 catalyst Substances 0.000 claims description 2
- 239000000919 ceramic Substances 0.000 claims description 2
- 239000000463 material Substances 0.000 claims description 2
- 239000000203 mixture Substances 0.000 claims description 2
- 230000000630 rising effect Effects 0.000 claims 1
- 206010022000 influenza Diseases 0.000 abstract 1
- 238000009434 installation Methods 0.000 description 7
- 238000006243 chemical reaction Methods 0.000 description 2
- 239000003344 environmental pollutant Substances 0.000 description 2
- 230000017525 heat dissipation Effects 0.000 description 2
- 238000005338 heat storage Methods 0.000 description 2
- 231100000719 pollutant Toxicity 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 1
- 239000004566 building material Substances 0.000 description 1
- 239000003245 coal Substances 0.000 description 1
- 238000004939 coking Methods 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000007717 exclusion Effects 0.000 description 1
- 238000012856 packing Methods 0.000 description 1
- 239000000779 smoke Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
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
-
- 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
- C10B21/20—Methods of heating ovens of the chamber oven type
-
- 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
- C10B5/00—Coke ovens with horizontal chambers
- C10B5/02—Coke ovens with horizontal chambers with vertical heating flues
Definitions
- coke ovens In coke ovens, coking of coal takes place with the exclusion of air through indirect heating.
- heating rooms and heating trains are provided in the coke oven walls.
- the combustion media are supplied with gas and air, where they are mixed and burned.
- the supply is preferably arranged to reduce the pollutants NO contained in the resulting flue gases so that the combustion air is introduced at different heights into the combustion chamber in order to achieve an initially substoichiometric combustion with the lowest possible temperatures at the tip of the flame.
- Substances such as N0 / N0 2 accelerate the flame reaction.
- flue gas can be added.
- the flue gas can be added to the combustion air.
- the object of the invention is to improve the heating and flow conditions in the heating rooms of coke ovens. According to the invention, this is achieved by internals.
- the internals are made of fireproof building materials, which in the Atmosphere of the boiler room are stable and can withstand temperatures up to 1800 ° C.
- the internals are formed by honeycomb grids and / or ball beds.
- honeycomb grids cause one
- Flow equalization and may even cause a separate routing of gas and air over a distance to be determined, which depends in detail on the furnace height and the geometric dimensions of the heating room.
- the heating space or the heating device is preferably divided into different zones, into which gas and combustion air are separated, and also introduced at different heights.
- the gas is supplied with the amount of air required for significant sub-stoichiometric combustion, and in a further stage the gas-smoke mixture that has not yet been burned is burned with air supplied from outside again. In this way, individual combustion reactions occur, which are acted upon separately by air. As a result, an almost uniform combustion with a low flame tip temperature can also be carried out over great heights.
- the type of combustion can be set selectively depending on the heat required at the respective height. This turns one on or Double-sided, pyramid-shaped flame progress possible over the height. With such graded flame progress, it is no longer necessary to supply the combustion air at different heights.
- the surfaces of the honeycombs can also be acted upon by catalyst material that the resulting pollutants, for. B. NO, at the location of
- the web thickness can have an additional influence on the heat storage capacity, which can compensate for the drop in temperature with currently increased heat dissipation.
- combustion can be influenced by changing the cross-section.
- REPLACEMENT LEAF Figure 1 shows a single view of a heating train of a coke oven.
- the coke oven also has a large number of other heaters which are of the same design.
- the heating cable 1 has a length of 7650 mm in the exemplary embodiment.
- the heating train 1 has a gas and air supply in a combustion chamber 7.
- two honeycomb internals 2 and 3 are arranged one above the other. Both have a length of 2000 mm.
- Installation 2 is located approx. 1165 mm above the gas and air supply.
- the distance between the two internals 2 and 3 is equal to the distance of the honeycomb-shaped installation 2 from the gas and air supply.
- Further combustion chambers 8 and 9 are located above the internals 2 and 3.
- Figure 2 shows the internals in cross section along the line A-A.
- edge lengths 1165 mm and 1498 mm result.
- the internals 2 and 3 have a distance 6 of 83 mm on all sides from the surrounding walls of the heating element 1.
- the individual honeycombs have a square cross section with an edge length of approximately 50 mm.
- FIGS. 3 to 5 show a further heating train 10 with the same dimensions as the heating train 1.
- the heating train 10 is provided with a grid honeycomb construction 11 which, under otherwise identical conditions, leaves one half of the heating train widening upwards 10 in this extends.
- the relevant boundary line 12 runs in the drawing from the top right heating edge to the bottom left heating edge.
- the honeycomb-shaped installation 11 has a multiplicity of air outlet openings in the flue gas and combustion chamber 13, the cross section of which free from the honeycomb body increases upwards.
- the course is adapted to an ideal flame control.
- the flame control is based on the local conditions, especially the supplied combustion media.
- FIG. 5 shows a cross section along the line B-B in FIG. 3.
- FIGS. 6 to 8 show a further heating train 20, which is identical to heating trains 1 and 10, but has a different installation 21.
- the other installation 21 is pyramid-shaped and extends to a height of 5660 mm. This design of the installation 21 corresponds to the optimal flame profile here.
- FIG. 8 contains a sectional illustration along the line C-C in FIG. 6.
- FIGS. 9 and 10 show the same heating train 30, which has a bed of balls 31 as an installation.
- the ball bed is different over the length of the heating cable 30.
- Cavities 32, 33, 34 and 35 are used as combustion chambers with a larger free cross section than the dense ball bed 31 educated.
- the upper cavity 35 and the lower cavity 32 have the same length of 1165 mm and the same distance from the nearest heating cable end of 500 mm.
- the cavity 33 has a length of 333 mm, the cavity 34 has a length of 1498 mm.
- the width of all cavities is approximately 1166 mm.
- Combustion air is fed in at the bottom and into the rooms 33 and 35 via devices 36, 37, which are not shown in detail.
- devices 36, 37 which are not shown in detail.
- the formation of cavities and combustion air supply are designed in the sense of optimal flame control.
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Organic Chemistry (AREA)
- Combustion & Propulsion (AREA)
- Coke Industry (AREA)
- Solid-Fuel Combustion (AREA)
- Incineration Of Waste (AREA)
Abstract
Selon la présente invention, les chambres de chauffage dans des fours à coke sont pourvues de chicanes pour optimiser le guidage des flammes et le transfert de chaleur sur la hauteur des carneaux de chauffage.According to the present invention, the heating chambers in coke ovens are provided with baffles to optimize the guiding of the flames and the heat transfer over the height of the heating flues.
Description
Claims
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
AT90906914T ATE86648T1 (en) | 1989-05-23 | 1990-05-23 | HEATING ROOMS IN COKE OVENS AND HEATING METHODS. |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE3916728 | 1989-05-23 | ||
DE3916728A DE3916728C1 (en) | 1989-05-23 | 1989-05-23 |
Publications (2)
Publication Number | Publication Date |
---|---|
EP0427828A1 true EP0427828A1 (en) | 1991-05-22 |
EP0427828B1 EP0427828B1 (en) | 1993-03-10 |
Family
ID=6381210
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP90906914A Expired - Lifetime EP0427828B1 (en) | 1989-05-23 | 1990-05-23 | Heating chambers in coke ovens and heating process |
Country Status (6)
Country | Link |
---|---|
US (1) | US5137602A (en) |
EP (1) | EP0427828B1 (en) |
JP (1) | JPH04500093A (en) |
DE (2) | DE3916728C1 (en) |
ES (1) | ES2040121T3 (en) |
WO (1) | WO1990014407A1 (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US7243502B2 (en) | 2002-12-19 | 2007-07-17 | Kabushiki Kaisha Toyota Jidoshokki | Control system for variable displacement compressor |
Families Citing this family (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0742276A1 (en) * | 1995-05-12 | 1996-11-13 | Krupp Koppers GmbH | Method for operating a coke oven |
DE10233819A1 (en) * | 2002-07-25 | 2004-02-12 | Thyssenkrupp Encoke Gmbh | Claus processing of hydrogen sulfide in coke oven gas achieves high removal efficiency operating with a single furnace and at lower temperatures than is usual practice |
DE10233820A1 (en) * | 2002-07-25 | 2004-02-12 | Thyssenkrupp Encoke Gmbh | Cracking reactor, for a Claus reactor to convert hydrogen sulfide into pure sulfur, has a horizontal cylindrical boiler, to take the hot gas into a combustion chamber and through a catalyst zone giving a hot process gas |
JP5428828B2 (en) * | 2009-12-18 | 2014-02-26 | 新日鐵住金株式会社 | Coke oven and operating method thereof |
DE102017216439A1 (en) | 2017-09-15 | 2019-03-21 | Thyssenkrupp Ag | Coke oven apparatus with circulating flow path around it for producing coke and method for operating the coke oven apparatus, as well as control means and use |
DE102017216437A1 (en) | 2017-09-15 | 2019-03-21 | Thyssenkrupp Ag | Coke oven apparatus having eccentric inlets for producing coke, and methods of operating the coke oven apparatus, and controller and use |
TWI681048B (en) | 2017-09-15 | 2020-01-01 | 德商蒂森克虜伯工業解決方案股份有限公司 | Coke oven device having a circular flow path with an encircling flow around it for the production of coke, and method for operating the coke oven device, and control installation, and use thereof |
DE102017216436A1 (en) | 2017-09-15 | 2019-03-21 | Thyssenkrupp Ag | Coke oven apparatus with centric recirculation for producing coke and method for operating the coke oven apparatus as well as controller and use |
DE102019206628B4 (en) * | 2019-05-08 | 2024-04-18 | Thyssenkrupp Ag | Coke oven device for producing coke and method for operating the coke oven device and use |
Family Cites Families (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE391501C (en) * | 1915-02-10 | 1924-03-10 | Roberts Arthur | Method for heating a coke oven or the like. |
US1891700A (en) * | 1927-01-31 | 1932-12-20 | Firm Carl Still | Method of heating coke ovens |
US1805922A (en) * | 1928-07-14 | 1931-05-19 | Otto Carl | Horizontal coke oven |
DE718962C (en) * | 1934-12-09 | 1942-03-25 | Didier Werke Ag | Device for external heating of elongated furnace walls by means of heating trains |
DE655948C (en) * | 1934-12-09 | 1938-01-26 | Didier Werke Ag | Heating cable for an elongated, externally heated object |
JPS5375201A (en) * | 1976-12-17 | 1978-07-04 | Nippon Steel Corp | Combustion in coke ovens |
DE3111476A1 (en) * | 1981-03-24 | 1982-10-07 | Dr. C. Otto & Comp. Gmbh, 4630 Bochum | "BATTERY ARRANGED CHAMBER STOVES FOR THE PRODUCTION OF COCKS AND GAS" |
-
1989
- 1989-05-23 DE DE3916728A patent/DE3916728C1/de not_active Expired - Fee Related
-
1990
- 1990-05-23 JP JP2507630A patent/JPH04500093A/en active Pending
- 1990-05-23 ES ES199090906914T patent/ES2040121T3/en not_active Expired - Lifetime
- 1990-05-23 DE DE9090906914T patent/DE59001009D1/en not_active Expired - Fee Related
- 1990-05-23 WO PCT/DE1990/000384 patent/WO1990014407A1/en active IP Right Grant
- 1990-05-23 EP EP90906914A patent/EP0427828B1/en not_active Expired - Lifetime
-
1991
- 1991-01-23 US US07/650,614 patent/US5137602A/en not_active Expired - Lifetime
Non-Patent Citations (1)
Title |
---|
See references of WO9014407A1 * |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US7243502B2 (en) | 2002-12-19 | 2007-07-17 | Kabushiki Kaisha Toyota Jidoshokki | Control system for variable displacement compressor |
Also Published As
Publication number | Publication date |
---|---|
JPH04500093A (en) | 1992-01-09 |
US5137602A (en) | 1992-08-11 |
DE3916728C1 (en) | 1990-12-20 |
DE59001009D1 (en) | 1993-04-15 |
EP0427828B1 (en) | 1993-03-10 |
WO1990014407A1 (en) | 1990-11-29 |
ES2040121T3 (en) | 1993-10-01 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
DE102008025437B4 (en) | Apparatus and method for the directional introduction of primary combustion air into the gas space of a coke oven battery | |
DE2327983C3 (en) | ||
DE1041476B (en) | Tube furnace for the preferably continuous implementation of gas reactions | |
EP0427828B1 (en) | Heating chambers in coke ovens and heating process | |
EP0093472A1 (en) | Prismatic hollow brick of refractory material for the checker work of chambers of a glass melting furnace | |
EP0174970B1 (en) | Shaft arrangement for thermal and/or material transfer processes between a gas and bulk material | |
DE3133467A1 (en) | METHOD AND DEVICE FOR PREHEATING POWDERED MATERIALS BEFORE ITS INTRODUCTION IN A Melting Furnace | |
DE2225782A1 (en) | Method of burning lime | |
EP0065944A1 (en) | Tiled stove | |
DE3410896A1 (en) | METHOD FOR THE THERMAL AND / OR CHEMICAL TREATMENT OF GRAINY, GRANULATED OR PIECEOUS GOODS | |
DE2164994C3 (en) | Recuperative coke oven | |
EP1136777A1 (en) | Firing tunnel furnace | |
DE102015117573A1 (en) | Reformer for the production of synthesis gas | |
EP0192144B1 (en) | Energy and/or particles exchange device between fines and a fluid | |
DE2237347A1 (en) | REGENERATIVE COOKER BATTERY | |
DE1796057C3 (en) | SHACHT OVEN heated with gasified oil | |
AT62278B (en) | Device for dry distillation of coal. | |
EP0398001A1 (en) | Burner for cowper | |
DE3310243C2 (en) | Heating device for regenerative coking furnace batteries | |
DE1956229C (en) | Vertically loaded regenerator for coking chamber furnace | |
DE505261C (en) | Coke oven with standing chambers | |
DE974769C (en) | Grate for fluidized bed reaction rooms | |
DE3136712A1 (en) | MULTI-STAGE FLUIDIZED LAYER REACTOR AND METHOD FOR OPERATING THE SAME | |
DE3114340C2 (en) | ||
DE695894C (en) | Horizontal or inclined retort furnace |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
PUAI | Public reference made under article 153(3) epc to a published international application that has entered the european phase |
Free format text: ORIGINAL CODE: 0009012 |
|
17P | Request for examination filed |
Effective date: 19910103 |
|
AK | Designated contracting states |
Kind code of ref document: A1 Designated state(s): AT BE DE ES FR GB IT NL SE |
|
17Q | First examination report despatched |
Effective date: 19920211 |
|
GRAA | (expected) grant |
Free format text: ORIGINAL CODE: 0009210 |
|
AK | Designated contracting states |
Kind code of ref document: B1 Designated state(s): AT BE DE ES FR GB IT NL SE |
|
REF | Corresponds to: |
Ref document number: 86648 Country of ref document: AT Date of ref document: 19930315 Kind code of ref document: T |
|
REF | Corresponds to: |
Ref document number: 59001009 Country of ref document: DE Date of ref document: 19930415 |
|
ET | Fr: translation filed | ||
ITF | It: translation for a ep patent filed |
Owner name: STUDIO JAUMANN |
|
GBT | Gb: translation of ep patent filed (gb section 77(6)(a)/1977) |
Effective date: 19930607 |
|
REG | Reference to a national code |
Ref country code: ES Ref legal event code: FG2A Ref document number: 2040121 Country of ref document: ES Kind code of ref document: T3 |
|
PLBE | No opposition filed within time limit |
Free format text: ORIGINAL CODE: 0009261 |
|
STAA | Information on the status of an ep patent application or granted ep patent |
Free format text: STATUS: NO OPPOSITION FILED WITHIN TIME LIMIT |
|
26N | No opposition filed | ||
EAL | Se: european patent in force in sweden |
Ref document number: 90906914.8 |
|
REG | Reference to a national code |
Ref country code: GB Ref legal event code: IF02 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: DE Payment date: 20040510 Year of fee payment: 15 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: GB Payment date: 20050517 Year of fee payment: 16 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: FR Payment date: 20050520 Year of fee payment: 16 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: SE Payment date: 20050524 Year of fee payment: 16 Ref country code: NL Payment date: 20050524 Year of fee payment: 16 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: AT Payment date: 20050525 Year of fee payment: 16 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: ES Payment date: 20050527 Year of fee payment: 16 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: BE Payment date: 20050606 Year of fee payment: 16 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: DE Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20051201 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: GB Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20060523 Ref country code: AT Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20060523 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: SE Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20060524 Ref country code: ES Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20060524 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: BE Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20060531 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: IT Payment date: 20060531 Year of fee payment: 17 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: NL Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20061201 |
|
EUG | Se: european patent has lapsed | ||
GBPC | Gb: european patent ceased through non-payment of renewal fee |
Effective date: 20060523 |
|
NLV4 | Nl: lapsed or anulled due to non-payment of the annual fee |
Effective date: 20061201 |
|
REG | Reference to a national code |
Ref country code: FR Ref legal event code: ST Effective date: 20070131 |
|
REG | Reference to a national code |
Ref country code: ES Ref legal event code: FD2A Effective date: 20060524 |
|
BERE | Be: lapsed |
Owner name: C. OTTO *FEUERFEST G.M.B.H. Effective date: 20060531 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: FR Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20060531 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: IT Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20070523 |