EP0421147A1 - Procédé et dispositif pour la réparation à chaud des carneaux de chauffage d'une batterie de fours de coke - Google Patents

Procédé et dispositif pour la réparation à chaud des carneaux de chauffage d'une batterie de fours de coke Download PDF

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Publication number
EP0421147A1
EP0421147A1 EP90117262A EP90117262A EP0421147A1 EP 0421147 A1 EP0421147 A1 EP 0421147A1 EP 90117262 A EP90117262 A EP 90117262A EP 90117262 A EP90117262 A EP 90117262A EP 0421147 A1 EP0421147 A1 EP 0421147A1
Authority
EP
European Patent Office
Prior art keywords
heating
transfer medium
heat exchanger
heat transfer
coke oven
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
Application number
EP90117262A
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German (de)
English (en)
Other versions
EP0421147B1 (fr
Inventor
Werner Wahlfeld
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
ThyssenKrupp Technologies AG
ThyssenKrupp Industrial Solutions AG
Original Assignee
Krupp Koppers GmbH
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Krupp Koppers GmbH filed Critical Krupp Koppers GmbH
Priority to AT90117262T priority Critical patent/ATE83000T1/de
Publication of EP0421147A1 publication Critical patent/EP0421147A1/fr
Application granted granted Critical
Publication of EP0421147B1 publication Critical patent/EP0421147B1/fr
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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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

Definitions

  • the invention relates to a method and a device for the hot repair of the heating trains of a coke oven battery.
  • the heating cables to be repaired or renewed are sealed off from the remaining, still hot parts of the coke oven by partition walls (so-called mirrors) provided with a fire-resistant coating. While the heating of the heating cables to be repaired is switched off, the remaining heating cables continue to be heated. So far, the heating trains to be repaired or renewed were initially bricked up completely from the sole of the coke oven to the ceiling. Only after this work had been completed was the new masonry heated by specially made openings in the partition walls with warm air from the non-renewed hot part of the coke oven and possibly also with additional flue gas. This means that in this phase, residual heat is transferred from the heated heating elements to the freshly bricked heating elements by convection. For the heating required after the heating, the new heating trains had to be connected again to the regenerative heating system of the coke oven.
  • the invention is therefore based on the object of improving the method for hot repair of the heating trains of a coke oven battery in such a way that the disadvantages described above are avoided, the use of the improved method should also be possible in particular in coke ovens whose chamber height is more than 5 m.
  • the method used to achieve this object is characterized in that, even while the heating cables are bricked up, the sections of the respective heating cable that have already been completed are heated to a temperature of approximately 250 ° C. and the new heating cables up to immediately after completion of the masonry work a temperature of about 500 ° C are heated, the heating and heating being carried out by means of a gaseous heat transfer ore which is blown into the heating trains and which has been appropriately heated in a heat exchanger using the heat of the hot parts of the coke oven battery.
  • the method according to the invention in contrast to the previously customary method of operation, already sees heating during the high masonry of the heating cables. It is appropriate that the already finished sections of the respective heating flue are closed at the top by a cover plate provided with a refractory coating, in the middle of which an opening with a pipe-like chimney, for example, is arranged.
  • the gaseous heat transfer medium is blown into the space below the cover plate and in this way heats up the sections of the respective heating train that have already been finished.
  • the correspondingly cooled heat transfer medium can then escape through the chimney located in the cover plate without impairing the masonry work carried out above the cover plate.
  • the cover plate With the progress of the masonry work, the cover plate is removed from its previous position and set correspondingly higher, so that the freshly bricked parts of the heating train underneath can be heated accordingly. This means that the position of the cover plate is gradually shifted from bottom to top while the heating train is bricked up.
  • the cover plate also serves as a stone protection and mortar collecting plate, so that the underlying, freshly bricked parts of the heating train cannot be damaged by falling stone rubble or mortar.
  • the cover plate is removed and the freshly bricked heating cable is heated to the desired temperature of approx. 500 ° C.
  • Compressed air can preferably be used as the gaseous heat transfer medium for heating and heating.
  • a different gas for this purpose such as flue gas or nitrogen, if this should be appropriate for certain reasons, such as when heating the heater.
  • the heating of the gaseous heat transfer medium required for the implementation of the method according to the invention takes place in indirect heat exchange with the hot parts of the coke oven battery, although there are of course different possibilities for this, which will be discussed in more detail below, for example.
  • the design of the heat exchanger used for this purpose is primarily aimed according to the local conditions in the part of the coke oven battery in which the heat exchanger is to be installed, and according to the design features of the respective coke oven battery.
  • the heat exchanger is preferably designed in the form of a tube coil which consists of one or more turns which are bent in the shape of a hairpin.
  • the inlet opening for the gaseous heat transfer medium lies at the cold end of the heat exchanger, the heat transfer medium flowing through the heat exchanger and then being fed to the heating train to be repaired at a correspondingly increased temperature.
  • This temperature can be controlled in a manner known per se by regulating the flow rate of the heat transfer medium per unit of time. Fittings such as valves, slides and / or perforated disks are provided for this purpose, which are preferably arranged at the cold end of the heat exchanger
  • One way of heating the gaseous heat transfer medium is, for example, that the heat exchanger, which in this case is designed as a hairpin-shaped tube coil, is arranged on the upper edge of the regenerator associated with the heating train to be repaired.
  • the heat transfer medium is heated accordingly as the heat emitted by the regenerator flows through the pipe coil and is then blown into the connecting channel between the regenerator and the heating train to be repaired at the hot end of the pipe coil.
  • the heat transfer medium then reaches the heating train via this connecting channel, in which it is used, as described above.
  • This method requires a separate coil for each heater train to be repaired.
  • the hairpin-shaped tube coil serving as the heat exchanger is not arranged on the regenerator but on the sole of the furnace chamber, which lies next to the heating train to be repaired.
  • the heating cables to be repaired will still be called the others Heating trains separated by a partition arranged inside the furnace chamber and provided with a fire-resistant coating.
  • This partition wall has through openings for the coil at its lower end so that it can extend into the hot part of the furnace chamber. The heat required to heat the heat transfer medium is therefore provided by the hot part of the furnace chamber.
  • Fig. 1 shows the furnace chamber 1 with the two opposite heating trains 2 and 3.
  • the left heating train 2 is to be subjected to a hot repair.
  • the pipe coil 5 serving as a heat exchanger is arranged on the upper edge of the regenerator 4 belonging to this heating train, which is on the outside of the regenerator lying inlet opening is pressurized with compressed air.
  • the outlet opening 6 of the coil 5 opens into the connecting channel 7, which connects the regenerator 4 with the heating cable 2.
  • the compressed air correspondingly heated in the coil 5 therefore passes from the connecting duct 7 into the heating duct 2.
  • the required sealing between the outlet opening 6 and the connecting duct 7 is achieved via the plate 9, which is made of VA steel and is provided with a refractory coating
  • the repair work in the lower section of the same should already be completed in the present case.
  • the cover plate 10 which separates the part that has already been repaired from the part of the heating element 2 that has not yet been repaired.
  • the heated compressed air blown into the heating cable 2 cannot therefore reach the upper part of the heating cable unhindered. Rather, this compressed air serves to heat the part of the heating train which is already finished and which is located below the cover plate 10.
  • the correspondingly cooled compressed air can then escape via the chimney 11 located in the cover plate 10 without the wall work above the cover plate 10 being impaired as a result.
  • the position of the cover plate 10 is gradually shifted upward, so that the sections of the heating cable 2 that have already been completed can each be heated to approximately 250 ° C., although the heating cable repair has not yet been completed.
  • the cover plate 10 is removed and the temperature of the compressed air supplied is increased so that the heating cable is heated to a temperature of approximately 500 ° C.
  • a configuration of the pipe coil 5 that is particularly suitable for this purpose will be discussed further below in connection with FIG. 3.
  • the reference number 12 denotes the transition to the adjacent heating train.
  • the structure of the heating element 3 corresponds in principle to the structure of the heating element 2, so that there is no need to go into details again here.
  • the coil 5 is arranged on the bottom of the furnace chamber 1.
  • the front heating cables 13, 14 and 15 in the area of the heating cable head are to be repaired at the same time.
  • the rear, hot part of the furnace chamber 1 is therefore separated from the front part by the partition 16, which is provided with a refractory coating 17.
  • the partition 16 has at its lower end through openings for the coil 5, so that it can penetrate into the hot part.
  • the compressed air blown into the coil 5 via the inlet opening 18 is therefore correspondingly heated in the hot rear part of the furnace chamber 1.
  • the stub lines 19, 20 and 21 are arranged through which the heated compressed air can enter the heating cables 13, 14 and 15 to be repaired.
  • the bypass lines 22, 23 and 24 are connected to the stub lines 19, 20 and 21, through which cold compressed air can be blown from the coil 5 for temperature regulation into the stub lines 19, 20 and 21.
  • the valves 25, 26 and 27 serve to regulate the compressed air supply through the bypass lines 22, 23 and 24.
  • the compressed air supply in the coil 5 can also be controlled by the slide 28.
  • the valves 25, 26 and 27 and the slide 28 are controlled via thermocouples depending on the desired temperature.
  • the illustration in FIG. 2 also shows the anchor stand 29 with the associated spring elements 30 and the wall protection plate 8.
  • the tube coil 5 serving as a heat exchanger.
  • the tube coil 5 serving as a heat exchanger.
  • the heat transfer medium used is used open valve 32 introduced into the coil 5 via the connection 31. Since the valve 34 remains closed, by the heat transfer medium flows only the pipe section A and then passes through the outlet opening 6 into the heating train, not shown in the figure.
  • the valve 32 is closed and the valve 34 is opened, so that the heat transfer medium initially enters the pipe section B via the connection 33 and both the pipe section B and subsequently flows through the pipe section A. Because of the longer flow path associated therewith, there is of course a greater heating of the heat carrier in the coil 5, so that it has the higher temperature required for heating the heating train.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Organic Chemistry (AREA)
  • Furnace Housings, Linings, Walls, And Ceilings (AREA)
  • Secondary Cells (AREA)
  • Coke Industry (AREA)
  • Control Of Resistance Heating (AREA)
  • Resistance Heating (AREA)
EP90117262A 1989-10-06 1990-09-07 Procédé et dispositif pour la réparation à chaud des carneaux de chauffage d'une batterie de fours de coke Expired - Lifetime EP0421147B1 (fr)

Priority Applications (1)

Application Number Priority Date Filing Date Title
AT90117262T ATE83000T1 (de) 1989-10-06 1990-09-07 Verfahren und vorrichtung zur heissreparatur der heizzuege einer koksofenbatterie.

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
DE3933364A DE3933364A1 (de) 1989-10-06 1989-10-06 Verfahren und vorrichtung zur heissreparatur der heizzuege einer koksofenbatterie
DE3933364 1989-10-06

Publications (2)

Publication Number Publication Date
EP0421147A1 true EP0421147A1 (fr) 1991-04-10
EP0421147B1 EP0421147B1 (fr) 1992-12-02

Family

ID=6390933

Family Applications (1)

Application Number Title Priority Date Filing Date
EP90117262A Expired - Lifetime EP0421147B1 (fr) 1989-10-06 1990-09-07 Procédé et dispositif pour la réparation à chaud des carneaux de chauffage d'une batterie de fours de coke

Country Status (11)

Country Link
US (1) US5092765A (fr)
EP (1) EP0421147B1 (fr)
JP (1) JP2960518B2 (fr)
AT (1) ATE83000T1 (fr)
AU (1) AU632974B2 (fr)
CA (1) CA2026536C (fr)
DE (2) DE3933364A1 (fr)
ES (1) ES2036877T3 (fr)
FI (1) FI97477C (fr)
MX (1) MX174451B (fr)
RU (1) RU2062282C1 (fr)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE19910300C1 (de) * 1999-03-09 2000-09-07 Thyssen Krupp Encoke Gmbh Verfahren zur Heißreparatur der Heizzüge einer Koksofenbatterie und Vorrichtung zum Durchführen dieses Verfahrens
CN107366780A (zh) * 2016-05-12 2017-11-21 鞍钢股份有限公司 一种更换焦炉高压氨水泵出水口管道的方法

Families Citing this family (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6494979B1 (en) 2000-09-29 2002-12-17 The Boeing Company Bonding of thermal tile insulation
US6613255B2 (en) 2001-04-13 2003-09-02 The Boeing Company Method of making a permeable ceramic tile insulation
CN102559212A (zh) * 2010-12-15 2012-07-11 五冶集团上海有限公司 七点六三米焦炉上升管内壁浇注料热修补方法
CN102102020B (zh) * 2010-12-29 2013-05-29 中冶焦耐(大连)工程技术有限公司 一种助燃空气与焦炉高温废气的换热装置
WO2012128654A1 (fr) * 2011-03-24 2012-09-27 Закрытое Акционерное Общество "Огнеупоркокссервис" (Зао "Okoc") Procédé de réchauffement d'un maçonnage réfractaire d'une baterie à coke
RU2509795C1 (ru) * 2012-07-24 2014-03-20 Закрытое акционерное общество "ОГНЕУПОРКОКССЕРВИС" (ЗАО "ОКОС") Способ разогрева огнеупорной кладки коксовой батареи
CN102851040B (zh) * 2012-08-14 2014-01-01 宣化钢铁集团有限责任公司 一种不降温修补炭化室墙面熔洞的方法
CN108728124B (zh) * 2018-07-05 2024-03-19 华泰永创(北京)科技股份有限公司 换热式焦炉

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE2124618A1 (en) * 1971-05-18 1972-11-30 Heinrich Koppers Gmbh, 4300 Essen Refractory linings renewal - with reduced risk of damage after relighting
US4190497A (en) * 1975-11-14 1980-02-26 Krupp-Koppers Gmbh Apparatus for heating up a chamber of a coking battery
EP0065328A2 (fr) * 1981-05-11 1982-11-24 Hoogovens Groep B.V. Procédé de réparation d'une batterie de fours à coke et paroi pour la mise en oeuvre du procédé

Family Cites Families (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE1274552B (de) * 1965-05-20 1968-08-08 Koppers Gmbh Heinrich Verfahren und Vorrichtung zum Ausbessern der Heizwaende von Verkokungsoefen
GB1572902A (en) * 1976-04-29 1980-08-06 Metal Box Co Ltd Closures for liquid product containers
US4189457A (en) * 1977-11-03 1980-02-19 H. L. Clement Company Method of sealing coke ovens
JPS56116718A (en) * 1980-02-19 1981-09-12 Nippon Synthetic Chem Ind Co Ltd:The Preparation of carboxyl group-type polyester resin for powder paint
JPS5798582A (en) * 1980-12-10 1982-06-18 Sumikin Coke Co Ltd Method for raising temperature of hot stacked and replaced wall of coke oven
US4364798A (en) * 1980-12-30 1982-12-21 Bmi, Inc. Rebuilt coke oven heating chamber and method of making the same
US4436678A (en) * 1981-06-23 1984-03-13 Kyusyu Refractories Co., Ltd. Method for hot repairing the inside of a furnace
JPS5871984A (ja) * 1981-10-26 1983-04-28 Kawasaki Steel Corp コ−クス炉炭化室煉瓦の熱間補修方法
FR2518239B1 (fr) * 1981-12-15 1986-06-27 Air Liquide Procede et dispositif de frittage de parois refractaires
US4452749A (en) * 1982-09-14 1984-06-05 Modern Refractories Service Corp. Method of repairing hot refractory brick walls
JPS59187081A (ja) * 1983-04-08 1984-10-24 Nippon Steel Corp コ−クス炉燃焼室の熱間補修方法
DE3619519C1 (de) * 1986-06-10 1987-07-23 Hamba Maschf Becherfuellwerk fuer Nahrungs- und Genussmittel,insbesondere fuer Molkereiprodukte

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE2124618A1 (en) * 1971-05-18 1972-11-30 Heinrich Koppers Gmbh, 4300 Essen Refractory linings renewal - with reduced risk of damage after relighting
US4190497A (en) * 1975-11-14 1980-02-26 Krupp-Koppers Gmbh Apparatus for heating up a chamber of a coking battery
EP0065328A2 (fr) * 1981-05-11 1982-11-24 Hoogovens Groep B.V. Procédé de réparation d'une batterie de fours à coke et paroi pour la mise en oeuvre du procédé

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE19910300C1 (de) * 1999-03-09 2000-09-07 Thyssen Krupp Encoke Gmbh Verfahren zur Heißreparatur der Heizzüge einer Koksofenbatterie und Vorrichtung zum Durchführen dieses Verfahrens
WO2000053694A1 (fr) * 1999-03-09 2000-09-14 Thyssen Krupp Encoke Gmbh Procede de reparation a chaud des carneaux de chauffage d'une batterie de fours a coke
US7037409B1 (en) 1999-03-09 2006-05-02 Thyssen Krupp Encoke Gmbh Method of hot-repairing the heating flues of a coke-oven battery and device for carrying out said method
CN107366780A (zh) * 2016-05-12 2017-11-21 鞍钢股份有限公司 一种更换焦炉高压氨水泵出水口管道的方法

Also Published As

Publication number Publication date
JP2960518B2 (ja) 1999-10-06
FI903646A0 (fi) 1990-07-19
CA2026536C (fr) 2000-01-18
JPH03126788A (ja) 1991-05-29
AU6382590A (en) 1991-04-11
US5092765A (en) 1992-03-03
CA2026536A1 (fr) 1991-04-07
ES2036877T3 (es) 1993-06-01
RU2062282C1 (ru) 1996-06-20
FI97477B (fi) 1996-09-13
DE59000544D1 (de) 1993-01-14
DE3933364A1 (de) 1991-04-18
ATE83000T1 (de) 1992-12-15
FI97477C (fi) 1996-12-27
MX174451B (es) 1994-05-17
AU632974B2 (en) 1993-01-14
EP0421147B1 (fr) 1992-12-02

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