EP0718389A2 - Process and device for the reduction of the carbon monoxide content in the flue gases of a coke oven battery, heated with lean gas - Google Patents
Process and device for the reduction of the carbon monoxide content in the flue gases of a coke oven battery, heated with lean gas Download PDFInfo
- Publication number
- EP0718389A2 EP0718389A2 EP95120307A EP95120307A EP0718389A2 EP 0718389 A2 EP0718389 A2 EP 0718389A2 EP 95120307 A EP95120307 A EP 95120307A EP 95120307 A EP95120307 A EP 95120307A EP 0718389 A2 EP0718389 A2 EP 0718389A2
- Authority
- EP
- European Patent Office
- Prior art keywords
- regenerator
- coke oven
- gas
- masonry
- lean 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.)
- Withdrawn
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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
- C10B29/00—Other details of coke ovens
- C10B29/06—Preventing or repairing leakages of the brickwork
-
- 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
- C10B27/00—Arrangements for withdrawal of the distillation gases
Definitions
- the invention relates to a method and a device for reducing the CO content in the exhaust gas of lean gas coke oven batteries.
- lean gas is often used to heat coke oven batteries. This is usually a slightly carburized blast furnace gas with a CO content of approx. 20 vol.%. With a clean combustion setting, CO contents in the range between 50 and 200 ppm are expected. In practice, however, it has been shown that values of 500 to 2000 ppm CO occur in the exhaust gas in many cases, although the combustion conditions have been set well.
- the object of the invention is therefore to find a suitable solution to this problem.
- the invention is based on the knowledge that the pronounced temperature-dependent stretching and shrinking of the silica and firebricks used for the construction of the regenerator walls can lead to hairline cracks in the mortar joints of the masonry of the regenerator partition walls and through these hairline cracks for preheating by the regenerator flowing lean gas can partly reach neighboring regenerator cells through which the combustion exhaust gases flow. These gas transfers then lead to a corresponding increase in the CO content in the exhaust gas.
- the inventive sealing of the regenerator partition walls prevents unwanted gas transfers from lean gas into the exhaust gas duct.
- the additional sealing can be carried out either on or on the media-contacting surfaces of the regenerator partition walls by means of plates made of a heat-resistant material, or an additional sealing is carried out within the masonry of the regenerator partition walls.
- the measures described above can also be used in combination with one another to seal the regenerator partition walls.
- FIGS. 2-5 show sections of the structure of regenerator partition walls 1, in which the sealing takes place by means of gas-tight films 7, which are arranged in the vertical joints behind the rectangular blocks 8. Films made of metal, for example, can be used as gas-tight films.
- FIGS. 2 and 3 relate to the regenerator wall of an underburner composite coke oven, wherein FIG. 2 shows a horizontal section and FIG. 3 shows a vertical section along the dash-dotted line in FIG. 2.
- the corresponding representations in FIG. 4 and FIG. 5 show the structure of the Regenerator wall 1 in a head-heated composite coke oven.
- the vertical high-pressure gas channels 5 are omitted here. Instead, horizontal channels are provided in this case, but these cannot be seen in FIGS. 4 and 5.
- FIGS. 6-9 show sections of the structure of regenerator partition walls 1, in which, in addition to tongue and groove, additional grooves are provided in the shaped stones used for the wall structure, so that abutting shaped stones jointly form circular channels 9 on the vertical surfaces.
- a sealing compound can be poured or pressed into these channels 9 when the regenerator partition walls 1 are bricked up. This measure can also be used to prevent gas from entering or escaping through any open gas-side butt joints.
- Refractory materials can be used as sealing material.
- FIGS. 6 and 7 in turn relate to the regenerator partition 1 of an underburner composite coke oven, wherein FIG. 6 shows a horizontal section and FIG. 7 shows a vertical section along the dash-dotted line in FIG. 6.
- FIG. 8 and FIG. 9 show the structure of the regenerator partition 1 in a head-heated composite coke oven.
Abstract
Description
Die Erfindung betrifft ein Verfahren und eine Vorrichtung zur Reduzierung des CO-Gehaltes im Abgas von mit Schwachgas beheizten Koksofenbatterien.The invention relates to a method and a device for reducing the CO content in the exhaust gas of lean gas coke oven batteries.
Für die Beheizung von Koksofenbatterien wird vielfach sogenanntes Schwachgas verwendet. Hierbei handelt es sich in der Regel um leicht aufcarboriertes Gichtgas, das einen CO-Gehalt von ca. 20 Vol.-% aufweist. Bei einer sauberen Verbrennungseinstellung werden CO-Gehalte im Bereich zwischen 50 und 200 ppm erwartet. In der Praxis hat sich allerdings gezeigt, daß in vielen Fällen Werte von 500 bis 2000 ppm CO im Abgas auftreten, obwohl eine gute Einstellung der Verbrennungsverhältnisse erfolgte.So-called lean gas is often used to heat coke oven batteries. This is usually a slightly carburized blast furnace gas with a CO content of approx. 20 vol.%. With a clean combustion setting, CO contents in the range between 50 and 200 ppm are expected. In practice, however, it has been shown that values of 500 to 2000 ppm CO occur in the exhaust gas in many cases, although the combustion conditions have been set well.
Infolge der immer strenger werdenden Umweltschutzauflagen sowie der immer genaueren Analyseverfahren wird die Forderung erhoben, den CO-Gehalt im Abgas der Koksofenbatterien möglichst niedrig zu halten.As a result of increasingly stringent environmental protection requirements and increasingly precise analysis methods, the demand is being made to keep the CO content in the exhaust gas from the coke oven batteries as low as possible.
Der Erfindung liegt deshalb die Aufgabe zugrunde, eine geeignete Lösung für dieses Problem zu finden.The object of the invention is therefore to find a suitable solution to this problem.
Zur Lösung dieses Problems wird bei einem Verfahren der eingangs genannten Art erfindungsgemäß vorgeschlagen, daß das Mauerwerk der Regeneratortrennwände der Koksofenbatterie mit einer zusätzlichen, horizontal wirksamen Abdichtung versehen wird.To solve this problem, it is proposed according to the invention in a method of the type mentioned at the outset that the masonry of the regenerator partition walls of the coke oven battery is provided with an additional, horizontally effective seal.
Weiterbildungen des Verfahrens bzw. der Vorrichtung erfolgen gemäß den Merkmalen der Ansprüche 2 bis 8.Further developments of the method and the device take place according to the features of
Der Erfindung liegt dabei die Erkenntnis zugrunde, daß das stark ausgeprägte temperaturabhängige Dehnen und Schrumpfen der für den Aufbau der Regeneratorwände verwendeten Silika- und Schamottesteine zum Auftreten von Haarrissen in den Mörtelfugen des Mauerwerks der Regeneratortrennwände führen kann und durch diese Haarrisse das zwecks Vorwärmung durch den Regenerator strömende Schwachgas zum Teil in benachbarte Regeneratorzellen, die von den Verbrennungsabgasen durchströmt werden, gelangen kann. Diese Gasübertritte führen dann zu einer entsprechenden Erhöhung des CO-Gehaltes im Abgas.The invention is based on the knowledge that the pronounced temperature-dependent stretching and shrinking of the silica and firebricks used for the construction of the regenerator walls can lead to hairline cracks in the mortar joints of the masonry of the regenerator partition walls and through these hairline cracks for preheating by the regenerator flowing lean gas can partly reach neighboring regenerator cells through which the combustion exhaust gases flow. These gas transfers then lead to a corresponding increase in the CO content in the exhaust gas.
Durch die erfindungsgemäße Abdichtung der Regeneratortrennwände werden unerwünschte Gasübertritte von Schwachgas in den Abgaskanal unterbunden. Die zusätzliche Abdichtung kann dabei entweder an bzw. auf den medienbeberührten Flächen der Regeneratortrennwänden durch Platten aus einem hitzebeständigen Material erfolgen, oder es wird eine zusätzliche Abdichtung innerhalb des Mauerwerks der Regeneratortrennwände vorgenommen.The inventive sealing of the regenerator partition walls prevents unwanted gas transfers from lean gas into the exhaust gas duct. The additional sealing can be carried out either on or on the media-contacting surfaces of the regenerator partition walls by means of plates made of a heat-resistant material, or an additional sealing is carried out within the masonry of the regenerator partition walls.
Zur Abdichtung der Regeneratortrennwände können die vorstehend beschriebenen Maßnahmen auch in Kombination miteinander zur Anwendung gelangen.The measures described above can also be used in combination with one another to seal the regenerator partition walls.
Ausführungsbeispiele der Erfindung werden nachfolgend anhand der Zeichnung erläutert. Hierin zeigen:
- Fig. 1
- einen Vertikalschnitt durch die Regeneratorkammern eines Unterbrenner-Verbundkoksofens, wobei die Abdichtung an den medienberührten Flächen der Regeneratortrennwände durch Edelstahlbleche erfolgt;
- Fig. 2
- einen Horizontalschnitt durch einen Teil einer Regeneratortrennwand eines Unterbrenner-Verbundkoksofens, wobei die Abdichtung durch im Mauerwerk angeordnete gasdichte Folien erfolgt (Schnitt entlang der Linie II - II gemäß Fig. 3);
- Fig. 3
- einen Vertikalschnitt entlang der Linie III - III von Fig. 2;
- Fig. 4
- einen Schnitt entsprechend Fig. 2, wobei es sich hier um das Mauerwerk der Regeneratortrennwand eines kopfbeheizten Verbundkoksofens handelt (Schnitt entlang der Linie IV - IV gemäß Fig. 5);
- Fig. 5
- einen Vertikalschnitt entlang der Linie V - V von Fig. 4;
- Fig. 6
- einen Horizontalschnitt durch einen Teil einer Regeneratortrennwand eines Unterbrenner-Verbundkoksofens, wobei die Abdichtung durch im Mauerwerk angeordnete vertikale Kanäle erfolgt, die mit einer Dichtungsmasse verfüllt werden (Schnitt entlang der Linie VI - VI gemäß Fig. 7);
- Fig. 7.
- einen Vertikalschnitt entlang der Linie VII - VII von Fig. 6;
- Fig. 8
- einen Schnitt entsprechend Fig. 6, wobei es sich hier um das Mauerwerk der Regeneratortrennwand eines kopfbeheizten Verbundkoksofens handelt (Schnitt entlang der Linie VIII - VIII gemäß Fig. 9) sowie
- Fig. 9.
- einen Vertikalschnitt entlang der Linie IX - IX von Fig. 8
- Fig. 1
- a vertical section through the regenerator chambers of an underburner composite coke oven, the sealing on the media-contacting surfaces of the regenerator partition walls being carried out by stainless steel sheets;
- Fig. 2
- a horizontal section through part of a regenerator partition of an underburner composite coke oven, the sealing being effected by gas-tight films arranged in the masonry (section along the line II-II according to FIG. 3);
- Fig. 3
- a vertical section along the line III - III of Fig. 2;
- Fig. 4
- a section corresponding to Figure 2, which is the masonry of the regenerator partition of a head-heated composite coke oven (section along the line IV - IV of FIG. 5).
- Fig. 5
- a vertical section along the line V - V of Fig. 4;
- Fig. 6
- a horizontal section through part of a regenerator partition of an underburner composite coke oven, the sealing being effected by vertical channels arranged in the masonry, which are filled with a sealing compound (section along the line VI-VI according to FIG. 7);
- Fig. 7.
- a vertical section along the line VII - VII of Fig. 6;
- Fig. 8
- a section corresponding to Fig. 6, which is the masonry of the regenerator partition of a head-heated composite coke oven (section along the line VIII - VIII of FIG. 9) and
- Fig. 9.
- a vertical section along the line IX - IX of Fig. 8
Die Figuren 2 - 5 zeigen ausschnittweise den Aufbau von Regeneratortrennwänden 1, bei denen die Abdichtung mittels gasdichter Folien 7 erfolgt, die in den Vertikalfugen hinter den Rechtecksteinen 8 angeordnet sind. Als gasdichte Folien können dabei Folien aus z.B. Metall verwendet werden. Die Figuren 2 und 3 betreffen dabei die Regeneratorwand eines Unterbrenner-Verbundkoksofens, wobei Figur 2 einen Horizontalschnitt zeigt und Figur 3 einen Vertikalschnitt entlang der strichpunktierten Linie in Fig. 2. Die entsprechenden Darstellungen in Figur 4 und Figur 5 zeigen den Aufbau der Regeneratorwand 1 bei einem kopfbeheizten Verbundkoksofen. Hier entfallen die vertikalen Starkgaskanäle 5. Stattdessen sind in diesem Falle horizontale Kanäle vorgesehen, die in Figur 4 und Figur 5 jedoch nicht zu erkennen sind.FIGS. 2-5 show sections of the structure of
Die Figuren 6 - 9 zeigen ausschnittsweise den Aufbau von Regeneratortrennwänden 1, bei denen in den zum Wandaufbau verwendeten Formsteinen neben Nut und Feder in den Stoßfugen zusätzliche Nuten vorgesehen sind, so daß aneinander stoßende Formsteine an den Vertikalflächen gemeinsam kreisrunde Kanäle 9 bilden. In diese Kanäle 9 kann beim Aufmauern der Regeneratortrennwände 1 eine Dichtungsmasse eingefüllt bzw. eingepreßt werden. Auch durch diese Maßnahme kann verhindert werden, daß durch eventuell offene gasseitige Stoßfugen Gas eindringt bzw. austritt. Als Dichtungsmaterial können feuerfesten Massen verwendet werden.FIGS. 6-9 show sections of the structure of
Die Figuren 6 und 7 betreffen dabei wiederum die Regeneratortrennwand 1 eines Unterbrenner-Verbundkoksofens, wobei Figur 6 einen Horizontalenschnitt zeigt und Figur 7 einen Vertikalschnitt entlang der strichpunktierten Linie in Figur 6. Die entsprechenden Darstellungen in Figur 8 und Figur 9 zeigen den Aufbau der Regeneratortrennwand 1 bei einem kopfbeheizten Verbundkoksofen. Bezüglich der Unterschiede zwischen den beiden Ofentypen wird auf die Ausführungen weiter oben zur Figur 2 bis Figur 5 verwiesen.FIGS. 6 and 7 in turn relate to the
Zur Abdichtung der Regeneratortrennwände können selbstverständlich vorstehend beschriebenen Maßnahmen gegebenenfalls auch in Kombination untereinander zur Anwendung gelangen.The measures described above can of course also be used in combination with one another, of course, for sealing the regenerator partition walls.
- 1.1.
- RegeneratortrennwandRegenerator partition
- 2.2nd
- EdelstahlblechStainless steel sheet
- 3.3rd
- ZwischenschichtIntermediate layer
- 4.4th
- SpannvorrichtungenFixtures
- 5.5.
- StarkgaskanalHeavy gas duct
- 6.6.
- RegeneratorkammernRegenerator chambers
- 7.7.
- Foliefoil
- 8.8th.
- RechtecksteineRectangular stones
- 9.9.
- Kanalchannel
Claims (8)
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE4445713 | 1994-12-21 | ||
DE4445713A DE4445713C1 (en) | 1994-12-21 | 1994-12-21 | Method and device for reducing the CO content in the exhaust gas from lean gas coke oven batteries |
Publications (2)
Publication Number | Publication Date |
---|---|
EP0718389A2 true EP0718389A2 (en) | 1996-06-26 |
EP0718389A3 EP0718389A3 (en) | 1997-03-26 |
Family
ID=6536537
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP95120307A Withdrawn EP0718389A3 (en) | 1994-12-21 | 1995-12-21 | Process and device for the reduction of the carbon monoxide content in the flue gases of a coke oven battery, heated with lean gas |
Country Status (8)
Country | Link |
---|---|
US (1) | US5705037A (en) |
EP (1) | EP0718389A3 (en) |
JP (1) | JP3182555B2 (en) |
KR (1) | KR100294788B1 (en) |
AU (1) | AU4050095A (en) |
DE (1) | DE4445713C1 (en) |
FI (1) | FI122738B (en) |
ZA (1) | ZA9510670B (en) |
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US9359554B2 (en) | 2012-08-17 | 2016-06-07 | Suncoke Technology And Development Llc | Automatic draft control system for coke plants |
WO2014105062A1 (en) | 2012-12-28 | 2014-07-03 | Suncoke Technology And Development Llc. | Systems and methods for removing mercury from emissions |
US10883051B2 (en) | 2012-12-28 | 2021-01-05 | Suncoke Technology And Development Llc | Methods and systems for improved coke quenching |
CN104884578B (en) | 2012-12-28 | 2016-06-22 | 太阳焦炭科技和发展有限责任公司 | Vent stack lid and the system and method being associated |
US10760002B2 (en) | 2012-12-28 | 2020-09-01 | Suncoke Technology And Development Llc | Systems and methods for maintaining a hot car in a coke plant |
US9273250B2 (en) | 2013-03-15 | 2016-03-01 | Suncoke Technology And Development Llc. | Methods and systems for improved quench tower design |
US10619101B2 (en) | 2013-12-31 | 2020-04-14 | Suncoke Technology And Development Llc | Methods for decarbonizing coking ovens, and associated systems and devices |
JP2017526798A (en) | 2014-09-15 | 2017-09-14 | サンコーク テクノロジー アンド ディベロップメント リミテッド ライアビリティ カンパニー | Coke oven with monolith component structure |
JP6515378B2 (en) * | 2014-10-15 | 2019-05-22 | 日本製鉄株式会社 | Gas leak prevention structure of coke oven sole flow part and construction method thereof |
EP3240862A4 (en) | 2015-01-02 | 2018-06-20 | Suncoke Technology and Development LLC | Integrated coke plant automation and optimization using advanced control and optimization techniques |
KR102445523B1 (en) | 2016-06-03 | 2022-09-20 | 선코크 테크놀러지 앤드 디벨로프먼트 엘엘씨 | Methods and systems for automatically creating remedial actions in industrial facilities |
JP7154231B2 (en) | 2017-05-23 | 2022-10-17 | サンコーク テクノロジー アンド ディベロップメント リミテッド ライアビリティ カンパニー | Systems and methods for refurbishing coke ovens |
BR112021012500B1 (en) | 2018-12-28 | 2024-01-30 | Suncoke Technology And Development Llc | UPCOMING COLLECTOR DUCT, EXHAUST GAS SYSTEM FOR A COKE OVEN, AND COKE OVEN |
BR112021012455B1 (en) | 2018-12-28 | 2023-10-24 | Suncoke Technology And Development Llc | COKE OVEN |
BR112021012459B1 (en) | 2018-12-28 | 2024-01-23 | Suncoke Technology And Development Llc | METHODS OF MAKING AND REPAIRING A TUNNEL IN A COKE PLANT AND PORTION OF WALL FOR A TUNNEL OF A COKE MAKING PLANT |
BR112021012766B1 (en) | 2018-12-28 | 2023-10-31 | Suncoke Technology And Development Llc | DECARBONIZATION OF COKE OVENS AND ASSOCIATED SYSTEMS AND METHODS |
US11098252B2 (en) | 2018-12-28 | 2021-08-24 | Suncoke Technology And Development Llc | Spring-loaded heat recovery oven system and method |
WO2020142391A1 (en) | 2018-12-31 | 2020-07-09 | Suncoke Technology And Development Llc | Methods and systems for providing corrosion resistant surfaces in contaminant treatment systems |
US11486572B2 (en) | 2018-12-31 | 2022-11-01 | Suncoke Technology And Development Llc | Systems and methods for Utilizing flue gas |
US11767482B2 (en) | 2020-05-03 | 2023-09-26 | Suncoke Technology And Development Llc | High-quality coke products |
US11946108B2 (en) | 2021-11-04 | 2024-04-02 | Suncoke Technology And Development Llc | Foundry coke products and associated processing methods via cupolas |
WO2023081821A1 (en) | 2021-11-04 | 2023-05-11 | Suncoke Technology And Development Llc | Foundry coke products, and associated systems, devices, and methods |
Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE512334C (en) * | 1927-11-22 | 1931-02-13 | Koksofenbau U Gasverwertung A | Coke oven |
US2216983A (en) * | 1937-10-16 | 1940-10-08 | Fuel Refining Corp | Underfired coke oven |
JPH06271855A (en) * | 1993-03-18 | 1994-09-27 | Nippon Steel Corp | Estimation of deterioration degree of carbonization chamber in unit coke oven group |
Family Cites Families (11)
Publication number | Priority date | Publication date | Assignee | Title |
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AT7724B (en) * | 1901-06-07 | 1902-05-26 | Josef Franz Zaruba | |
AT7725B (en) * | 1901-12-02 | 1902-05-26 | Kuhn & Cie | |
DE2327983B2 (en) * | 1973-06-01 | 1976-08-19 | HORIZONTAL COOKING FURNACE WITH TRANSVERSAL GENERATORS | |
US3963582A (en) * | 1974-11-26 | 1976-06-15 | Koppers Company, Inc. | Method and apparatus for suppressing the deposition of carbonaceous material in a coke oven battery |
US4033827A (en) * | 1976-02-02 | 1977-07-05 | White Jr Herbert A | Apparatus for sealing a coking chamber |
DE2654555C2 (en) * | 1976-12-02 | 1978-09-14 | Fa. Carl Still, 4350 Recklinghausen | Process for the operation of the two-part regenerative heating of several horizontal coking furnace batteries as well as the device for its implementation |
DE3018361C2 (en) * | 1980-05-14 | 1984-12-20 | Dr. C. Otto & Co Gmbh, 4630 Bochum | Arrangement for air regulation in regeneratively heated coking ovens |
NL8101060A (en) * | 1981-03-05 | 1982-10-01 | Estel Hoogovens Bv | HORIZONTAL COOKING OVEN BATTERY. |
US4406619A (en) * | 1981-03-30 | 1983-09-27 | Hans Oldengott | Sealing lid means for coke oven chamber |
US4533439A (en) * | 1983-05-27 | 1985-08-06 | United States Steel Corporation | Apparatus and method of using a fuel gas regulator for a coke oven battery |
US5228955A (en) * | 1992-05-22 | 1993-07-20 | Sun Coal Company | High strength coke oven wall having gas flues therein |
-
1994
- 1994-12-21 DE DE4445713A patent/DE4445713C1/en not_active Expired - Lifetime
-
1995
- 1995-12-07 US US08/568,632 patent/US5705037A/en not_active Expired - Lifetime
- 1995-12-14 ZA ZA9510670A patent/ZA9510670B/en unknown
- 1995-12-18 AU AU40500/95A patent/AU4050095A/en not_active Abandoned
- 1995-12-20 FI FI956125A patent/FI122738B/en not_active IP Right Cessation
- 1995-12-20 JP JP33200095A patent/JP3182555B2/en not_active Expired - Lifetime
- 1995-12-21 EP EP95120307A patent/EP0718389A3/en not_active Withdrawn
- 1995-12-21 KR KR1019950053752A patent/KR100294788B1/en not_active IP Right Cessation
Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE512334C (en) * | 1927-11-22 | 1931-02-13 | Koksofenbau U Gasverwertung A | Coke oven |
US2216983A (en) * | 1937-10-16 | 1940-10-08 | Fuel Refining Corp | Underfired coke oven |
JPH06271855A (en) * | 1993-03-18 | 1994-09-27 | Nippon Steel Corp | Estimation of deterioration degree of carbonization chamber in unit coke oven group |
Non-Patent Citations (1)
Title |
---|
PATENT ABSTRACTS OF JAPAN vol. 018, no. 686 (C-1292), 26.Dezember 1994 & JP-A-06 271855 (NIPPON STEEL CORP), 27.September 1994, * |
Also Published As
Publication number | Publication date |
---|---|
US5705037A (en) | 1998-01-06 |
AU4050095A (en) | 1996-06-27 |
FI956125A (en) | 1996-06-22 |
FI122738B (en) | 2012-06-15 |
JPH08218073A (en) | 1996-08-27 |
KR100294788B1 (en) | 2001-10-24 |
FI956125A0 (en) | 1995-12-20 |
ZA9510670B (en) | 1996-07-25 |
DE4445713C1 (en) | 1996-07-11 |
JP3182555B2 (en) | 2001-07-03 |
EP0718389A3 (en) | 1997-03-26 |
KR960022950A (en) | 1996-07-18 |
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