EP0427828B1 - Heating chambers in coke ovens and heating process - Google Patents
Heating chambers in coke ovens and heating process Download PDFInfo
- Publication number
- EP0427828B1 EP0427828B1 EP90906914A EP90906914A EP0427828B1 EP 0427828 B1 EP0427828 B1 EP 0427828B1 EP 90906914 A EP90906914 A EP 90906914A EP 90906914 A EP90906914 A EP 90906914A EP 0427828 B1 EP0427828 B1 EP 0427828B1
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- European Patent Office
- Prior art keywords
- heating
- combustion
- components
- air
- gas
- 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.)
- Expired - Lifetime
Links
- 238000010438 heat treatment Methods 0.000 title claims abstract description 45
- 239000000571 coke Substances 0.000 title claims abstract description 11
- 206010022000 influenza Diseases 0.000 claims abstract 2
- 238000002485 combustion reaction Methods 0.000 claims description 29
- 239000007789 gas Substances 0.000 claims description 11
- 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 5
- 239000003054 catalyst Substances 0.000 claims description 2
- 239000000919 ceramic Substances 0.000 claims description 2
- 239000000463 material Substances 0.000 claims description 2
- 238000000034 method Methods 0.000 claims description 2
- 239000000203 mixture Substances 0.000 claims description 2
- 230000000630 rising effect Effects 0.000 claims 1
- 241000264877 Hippospongia communis Species 0.000 description 8
- 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
- 239000000567 combustion gas Substances 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
Images
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 x 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 NO / NO2 accelerate the flame reaction.
- flue gas can be added.
- the flue gas can be added to the combustion air.
- GB-A-2095380 discloses a gas supply for heating rooms in coke ovens, in which the combustion gases are fed into the combustion chamber through shafts with air outlet openings at different heights and then brought to the combustion.
- the invention has for its object 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 make the flow more even and may even cause gas and air to be routed separately over a distance to be determined, which depends in particular on the furnace height and the geometric dimensions of the heating space.
- 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. So that one or Double-sided, pyramid-shaped flame progress possible over the height. With such a graded flame advance, it is no longer necessary to supply the combustion air at different heights.
- the surfaces of the honeycombs can also be charged with catalyst material that the pollutants that arise, z. B. NO x , implemented at the place of origin.
- 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.
- FIG. 1 shows a single view of a heating train of a coke oven.
- the coke oven also has a large number of further heating trains 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-shaped 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 upper right heating edge to the lower 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.
- Figures 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 next 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)
- Combustion & Propulsion (AREA)
- Materials Engineering (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Organic Chemistry (AREA)
- Coke Industry (AREA)
- Incineration Of Waste (AREA)
- Solid-Fuel Combustion (AREA)
Abstract
Description
In Koksöfen findet die Verkokung von kohle unter Luftabschluß durch indirekte Beheizung statt. Dazu sind in den Koksofenwänden Beheizungsräume, Heizzüge vorgesehen. Den Beheizungsräumen werden die Verbrennungsmedien Gas und Luft zugeführt, dort gemischt und verbrannt. Die Zuführung wird zur Verminderung der in den entstehenden Rauchgasen enthaltenen Schadstoffen NOx bevorzugt so angeordnet, daß die Verbrennungsluft in unterschiedlicher Höhe in den Verbrennungsraum eingeführt wird, um eine zunächst unterstöchiometrische Verbrennung mit möglichst niedrigen Temperaturen an der Flammenspitze zu erzielen.In coke ovens, coking of coal takes place with the exclusion of air through indirect heating. For this purpose, 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 x 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.
Stoffe wie NO/NO₂ beschleunigen dabei die Flammreaktion. Um diesen Effekt zu kompensieren beziehungsweise die Flammenreaktion zu verlangsamen, kann Rauchgas zugeführt werden. Das Rauchgas kann der Verbrennungsluft zugemischt werden.Substances such as NO / NO₂ accelerate the flame reaction. To compensate for this effect or to slow down the flame reaction, flue gas can be added. The flue gas can be added to the combustion air.
Allen bekannten Beheizungsräumen in Koksöfen sind jedoch unkontrollierte Strömungsverhältnisse gemeinsam. Zum Teil bestehen ausgeprägte Rezirkulationsströmungen.However, uncontrolled flow conditions are common to all known heating rooms in coke ovens. In some cases there are pronounced recirculation currents.
In der GB-A-2095380 ist eine Gaszuführung für Beheizugsräume in Koksöfen offenbart, bei der die Verbrennungsgase durch Schächte mit Luftaustrittsöffnungen in verschiedenen Höhen in die Verbrennungkammer zugeführt und dann zur Verbrennung gebracht werden.GB-A-2095380 discloses a gas supply for heating rooms in coke ovens, in which the combustion gases are fed into the combustion chamber through shafts with air outlet openings at different heights and then brought to the combustion.
Der Erfindung liegt die Aufgabe zugrunde, die Heizungs- und Strömungsverhältnisse in Beheizungsräumen von Koksöfen zu verbessern. Nach der Erfindung wird das durch Einbauten erreicht. Die Einbauten sind aus feuerfesten Baustoffen hergestellt, die in der Atmosphäre des Beheizungsraumes beständig sind und Temperaturen bis 1800° C standhalten. Nach der Erfindung werden die Einbauten durch Wabengitter und/oder Kugelschüttungen gebildet.The invention has for its object 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. According to the invention, the internals are formed by honeycomb grids and / or ball beds.
Die Wabengitter bewirken eine Strömungsvergleichmäßigung und können gegebenenfalls sogar eine getrennte Führung von Gas und Luft über eine festzulegende Entfernung verursachen, die im einzelnen von der Ofenhöhe und den geometrischen Abmessungen des Beheizungsraumes abhängt.The honeycomb grids make the flow more even and may even cause gas and air to be routed separately over a distance to be determined, which depends in particular on the furnace height and the geometric dimensions of the heating space.
Vorzugsweise ist der Beheizungsraum beziehungsweise die Beheizungsvorrichtung in unterschiedliche Zonen eingeteilt, in die Gas und Verbrennungsluft getrennt, auch in unterschiedlicher Höhe eingeführt werden. Dem Gas wird in einer ersten Stufe eine zur deutlichen unterstöchiometrischen Verbrennung benötigte Luftmenge zugeführt, danach in einer weiteren Stufe das noch nicht verbrannte Gas-Rauchgemisch, mit erneut von außen zugeführter Luft verbrannt. Auf diese Weise entstehen einzelne Verbrennungsreaktionen, die gesondert mit Luft beaufschlagt werden. Im Ergebnis kann auf diese Weise auch über große Höhen eine annähernd gleichmäßige Verbrennung mit niedriger Flammenspitzentemperatur durchgeführt werden.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. In a first stage, 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.
Durch die unterschiedliche Höhe des Wabengitters über den Querschnitt, die Höhe des Beheizungsraumes und getrennte Führungen der Verbrennungsmedien bis zum Gitteraustritt kann die Verbrennungsart abhängig von der in der jeweiligen Höhe benötigten Wärme selektiv eingestellt werden. Damit wird ein ein- oder zweiseitiger, pyramidenförmiger, über die Höhe abgestufter Flammenfortschritt möglich. Bei solchermaßen gestuftem Flammenförtschritt ist es nicht mehr notwendig, die Verbrennungsluft in unterschiedlichen Höhen zuzuführen.Due to the different height of the honeycomb grille over the cross-section, the height of the heating room and separate guides of the combustion media up to the grille outlet, the type of combustion can be set selectively depending on the heat required at the respective height. So that one or Double-sided, pyramid-shaped flame progress possible over the height. With such a graded flame advance, it is no longer necessary to supply the combustion air at different heights.
Die Oberflächen der Waben können zusätzlich mit Katalysatormaterial beaufachlagt sein, das die entstehenden Schadstoffe, z. B. NOx, am Ort der Entstehung umsetzt.The surfaces of the honeycombs can also be charged with catalyst material that the pollutants that arise, z. B. NO x , implemented at the place of origin.
Über die Stegstärke kann ein zusätzlicher Einfluß auf die Wärmespeicherkapazität genommen werden, die bei momentan erhöhter Wärmeabfuhr den Temperaturabfall ausgleichen kann. Außerdem kann auf die Verbrennung durch Querschnittsänderung Einfluß genommen werden.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. In addition, combustion can be influenced by changing the cross-section.
Bei erfindungsgemäßer Verwendung von Kugeln als Einbauten besteht die Möglichkeit der Füllung des Beheizungsraumes mit gleich groben keramischen Kugeln, so daß ein Freiraum von ca. 25 % (hexagonale, dichteste Kugelpackung) verbleibt. In diesem Fall wird neben der ausgeprägten Führung mit intensiver Vermischung der Verbrennungsmedien die Wärmespeicherkapazität des Beheizungsraumes wesentlich erhöht, so daß auch eine verfahrenstechnisch bedingte momentan erhöhte Wärmeabfuhr nicht zu Temperatursenkungen im Heizzug führt.When using balls as internals according to the invention, there is the possibility of filling the heating space with ceramic balls of the same size, so that there is a free space of approximately 25% (hexagonal, densest ball packing). In this case, in addition to the pronounced guidance with intensive mixing of the combustion media, the heat storage capacity of the heating room is significantly increased, so that even a heat dissipation which is currently caused by the process technology does not lead to temperature drops in the heating train.
In der Zeichnung sind verschiedene Ausführungsbeispiele der Erfindung dargestellt.Various exemplary embodiments of the invention are shown in the drawing.
Figur 1 zeigt in einer Einzelansicht einen Heizzug eines Koksofens. Der Koksofen besitzt neben dem dargestellten Heizzug 1 noch eine Vielzahl weiterer Heizzüge, die gleich ausgebildet sind. Der Heizzug 1 hat im Ausführungsbeispiel eine Länge von 7650 mm. Unten besitzt der Heizzug 1 eine Gas- und Luftzuführung in einem Verbrennungsraum 7. Im Heizzug 1 sind zwei wabenförmige Einbauten 2 und 3 übereinander angeordnet. Beide besitzen eine Länge von 2000 mm. Der Einbau 2 ist ca. 1165 mm über der Gas- und Luftzuführung angeordnet. Der Abstand beider Einbauten 2 und 3 ist gleich dem Abstand des wabenförmigen Einbaus 2 von der Gas- und Luftzuführung. Oberhalb der Einbauten 2 und 3 befinden sich weitere Verbrennungsräume 8 und 9.Figure 1 shows a single view of a heating train of a coke oven. In addition to the
Im Heizzug 1 wird Luft jeweils oberhalb der wabenförmigen Einbauten bei 4 und 5 durch geeignete Einrichtungen zugeführt.In the
Figur 2 zeigt die Einbauten im Querschnitt entlang der Linie A-A. Im Querschnitt ergeben sich Kantenlängen von 1165 mm und 1498 mm. Die Einbauten 2 und 3 besitzen einen allseitigen Abstand 6 von 83 mm von den Umgebungswänden des Heizzuges 1. Die einzelnen Waben haben quadratischen Querschnitt mit ca. 50 mm Kantenlänge.Figure 2 shows the internals in cross section along the line A-A. In cross-section, edge lengths of 1165 mm and 1498 mm result. The
Die Figuren 3 bis 5 zeigen einen weiteren Heizzug 10 mit gleichen Abmessungen wie der Heizzug 1. Im Unterschied zu dem Heizzug 1 ist der Heizzug 10 mit einer Gitterwabenkonstruktion 11 versehen, die sich bei sonst gleichen Verhältnissen unter Freilassung einer sich nach oben erweiternden Hälfte des Heizzuges 10 in diesem erstreckt. Die hier relevante Grenzlinie 12 verläuft in der Zeichnung von der rechten oberen Heizzugkante zur linken unteren Heizzugkante. Entlang der durch die Grenzlinie 12 markierten Fläche weist der wabenförmige Einbau 11 eine Vielzahl von Luftaustrittsöffnungen in dem Rauchgas- und Verbrennungsraum 13 auf, dessen vom Wabenkörper freier Querschnitt nach oben zunimmt.FIGS. 3 to 5 show a
Der Verlauf ist einer idealen Flammenführung angepaßt. Die Flammenführung basiert auf den örtlichen Gegebenheiten, insbesondere den zugeführten Verbrennungsmedien.The course is adapted to an ideal flame control. The flame control is based on the local conditions, especially the supplied combustion media.
Figur 5 zeigt einen Querschnitt entlang der Linie B-B in Figur 3.FIG. 5 shows a cross section along the line B-B in FIG. 3.
Die Figuren 6 bis 8 zeigen einen weiteren Heizzug 20, der identisch mit den Heizzügen 1 und 10 ist, jedoch einen anderen Einbau 21 besitzt. Der andere Einbau 21 ist pyramidenförmig ausgebildet und erstreckt sich bis zu einer Höhe von 5660 mm. Diese Ausbildung des Einbaus 21 entspricht dem hier optimalen Flammenverlauf.FIGS. 6 to 8 show a
Figur 8 beinhaltet eine Schnittdarstellung entlang der Linie C-C in Figur 6.FIG. 8 contains a sectional illustration along the line C-C in FIG. 6.
Die Figuren 9 und 10 zeigen einen gleichen Heizzug 30, der als Einbau eine Schüttung von kugeln 31 besitzt. Die Kugelschüttung ist über die Länge des Heizzuges 30 unterschiedlich. Es werden Hohlräume 32, 33, 34 und 35 als Verbrennungsräume mit einem im Vergleich zur dichten Kugelschüttung 31 frößeren freien Querschnitt gebildet. Der obere Hohlraum 35 und der untere Hohlraum 32 haben gleiche Länge von 1165 mm und gleichen Abstand von dem nachstliegenden Heizzugende von 500 mm.Figures 9 and 10 show the
Der Hohlraum 33 hat eine Länge von 333 mm, der Hohlraum 34 eine Länge von 1498 mm. Die Breite aller Hohlräume beträgt ca. 1166 mm.The
Verbrennungsluft wird unten zugeführt sowie über nicht in Einzelheiten dargestellte Einrichtungen 36, 37 in die Räume 33 und 35. Auch hier ist die Hohlraumbildung und Verbrennungsluftzuführung im Sinne einer optimalen Flammenführung gestaltet.Combustion air is fed in at the bottom and into the
Claims (9)
- Heating chambers in coke ovens, characterised by components in the form of permeable honeycomb lattices (2, 3, 11, 21) and/or fillings of balls (31) for an optimum guidance of the flames throughout the height of the heating flue.
- Apparatus according to claim 1, characterised in that the components are formed from ceramics.
- Apparatus according to claim 1 or 2, characterised by a guidance of the flue gas in stages.
- Apparatus according to one or more of claims 1 to 3, characterised by components which taper and/or widen along the length of the heating chambers.
- Apparatus according to claim 4, characterised in that the honeycomb lattices (11, 12) have a plurality of air outlet apertures distributed over at least a portion of the height of the heating flue.
- Apparatus according to claim 4, characterised in that the honeycomb lattices contain separate guide means for guiding the combustion media to the outlet from the honeycomb lattices, and the lattice outlets are selectively disposed in dependence on the heat required at the particular height in question.
- Apparatus according to one or more of claims 1 to 6, characterised in that the components are coated with catalyst material.
- Apparatus according to claim 3, characterised in that means (4, 5, 36, 37) for supplying air for combustion are disposed above portions having honeycomb components (2, 3) or having a filling of balls (31) in combustion chambers (8, 9, 13, 33, 35) of greater free cross-section.
- Method of heating coke ovens by means of heating chambers, into which gas and air for combustion are introduced, with the utilisation of components in the heating flues in accordance with one or more of claims 1 to 8, characterised in that the gas is initially burned in a sub-stoichiometrical manner with only a small quantity of air, and additional air for combustion is supplied to the mixture of gas and flue gas, rising in the heating flue, uniformly through the components or stepwisely above the components until full combustion is achieved.
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 |
|---|---|---|---|
| DE3916728A DE3916728C1 (en) | 1989-05-23 | 1989-05-23 | |
| DE3916728 | 1989-05-23 |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| EP0427828A1 EP0427828A1 (en) | 1991-05-22 |
| EP0427828B1 true 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) |
Families Citing this family (10)
| 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 |
| 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 |
| 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 |
| JP3906796B2 (en) | 2002-12-19 | 2007-04-18 | 株式会社豊田自動織機 | Control device for variable capacity compressor |
| JP5428828B2 (en) * | 2009-12-18 | 2014-02-26 | 新日鐵住金株式会社 | Coke oven and operating method thereof |
| 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 |
| 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 |
| 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 |
| 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 |
| 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 |
| DE655948C (en) * | 1934-12-09 | 1938-01-26 | Didier Werke Ag | Heating cable for an elongated, externally heated object |
| DE718962C (en) * | 1934-12-09 | 1942-03-25 | Didier Werke Ag | Device for external heating of elongated furnace walls by means of heating trains |
| 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 WO PCT/DE1990/000384 patent/WO1990014407A1/en active IP Right Grant
- 1990-05-23 EP EP90906914A patent/EP0427828B1/en not_active Expired - Lifetime
- 1990-05-23 DE DE9090906914T patent/DE59001009D1/en not_active Expired - Fee Related
- 1990-05-23 ES ES199090906914T patent/ES2040121T3/en not_active Expired - Lifetime
- 1990-05-23 JP JP2507630A patent/JPH04500093A/en active Pending
-
1991
- 1991-01-23 US US07/650,614 patent/US5137602A/en not_active Expired - Lifetime
Also Published As
| Publication number | Publication date |
|---|---|
| ES2040121T3 (en) | 1993-10-01 |
| EP0427828A1 (en) | 1991-05-22 |
| DE59001009D1 (en) | 1993-04-15 |
| JPH04500093A (en) | 1992-01-09 |
| DE3916728C1 (en) | 1990-12-20 |
| US5137602A (en) | 1992-08-11 |
| WO1990014407A1 (en) | 1990-11-29 |
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