EP0348603A2 - Système de régulation pour un four tunnel fonctionnant à contre-courant - Google Patents

Système de régulation pour un four tunnel fonctionnant à contre-courant Download PDF

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Publication number
EP0348603A2
EP0348603A2 EP89105526A EP89105526A EP0348603A2 EP 0348603 A2 EP0348603 A2 EP 0348603A2 EP 89105526 A EP89105526 A EP 89105526A EP 89105526 A EP89105526 A EP 89105526A EP 0348603 A2 EP0348603 A2 EP 0348603A2
Authority
EP
European Patent Office
Prior art keywords
temperature
zone
cooling
flue gas
pressure
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
EP89105526A
Other languages
German (de)
English (en)
Other versions
EP0348603B1 (fr
EP0348603A3 (fr
Inventor
Johann Joas
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.)
Hans Lingl Anlagenbau und Verfahrenstechnik GmbH and Co KG
Original Assignee
Hans Lingl Anlagenbau und Verfahrenstechnik GmbH and Co KG
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 Hans Lingl Anlagenbau und Verfahrenstechnik GmbH and Co KG filed Critical Hans Lingl Anlagenbau und Verfahrenstechnik GmbH and Co KG
Publication of EP0348603A2 publication Critical patent/EP0348603A2/fr
Publication of EP0348603A3 publication Critical patent/EP0348603A3/fr
Application granted granted Critical
Publication of EP0348603B1 publication Critical patent/EP0348603B1/fr
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F27FURNACES; KILNS; OVENS; RETORTS
    • F27DDETAILS OR ACCESSORIES OF FURNACES, KILNS, OVENS OR RETORTS, IN SO FAR AS THEY ARE OF KINDS OCCURRING IN MORE THAN ONE KIND OF FURNACE
    • F27D19/00Arrangements of controlling devices
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F27FURNACES; KILNS; OVENS; RETORTS
    • F27BFURNACES, KILNS, OVENS OR RETORTS IN GENERAL; OPEN SINTERING OR LIKE APPARATUS
    • F27B9/00Furnaces through which the charge is moved mechanically, e.g. of tunnel type; Similar furnaces in which the charge moves by gravity
    • F27B9/30Details, accessories or equipment specially adapted for furnaces of these types
    • F27B9/40Arrangements of controlling or monitoring devices
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F27FURNACES; KILNS; OVENS; RETORTS
    • F27BFURNACES, KILNS, OVENS OR RETORTS IN GENERAL; OPEN SINTERING OR LIKE APPARATUS
    • F27B9/00Furnaces through which the charge is moved mechanically, e.g. of tunnel type; Similar furnaces in which the charge moves by gravity
    • F27B9/12Furnaces through which the charge is moved mechanically, e.g. of tunnel type; Similar furnaces in which the charge moves by gravity with special arrangements for preheating or cooling the charge
    • F27B2009/124Cooling
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F27FURNACES; KILNS; OVENS; RETORTS
    • F27BFURNACES, KILNS, OVENS OR RETORTS IN GENERAL; OPEN SINTERING OR LIKE APPARATUS
    • F27B9/00Furnaces through which the charge is moved mechanically, e.g. of tunnel type; Similar furnaces in which the charge moves by gravity
    • F27B9/30Details, accessories or equipment specially adapted for furnaces of these types
    • F27B9/3005Details, accessories or equipment specially adapted for furnaces of these types arrangements for circulating gases
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F27FURNACES; KILNS; OVENS; RETORTS
    • F27DDETAILS OR ACCESSORIES OF FURNACES, KILNS, OVENS OR RETORTS, IN SO FAR AS THEY ARE OF KINDS OCCURRING IN MORE THAN ONE KIND OF FURNACE
    • F27D19/00Arrangements of controlling devices
    • F27D2019/0006Monitoring the characteristics (composition, quantities, temperature, pressure) of at least one of the gases of the kiln atmosphere and using it as a controlling value
    • F27D2019/0018Monitoring the temperature of the atmosphere of the kiln
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F27FURNACES; KILNS; OVENS; RETORTS
    • F27DDETAILS OR ACCESSORIES OF FURNACES, KILNS, OVENS OR RETORTS, IN SO FAR AS THEY ARE OF KINDS OCCURRING IN MORE THAN ONE KIND OF FURNACE
    • F27D19/00Arrangements of controlling devices
    • F27D2019/0028Regulation
    • F27D2019/0031Regulation through control of the flow of the exhaust gases

Definitions

  • the invention relates to a control system for a tunnel kiln operated in countercurrent, preferably in the ceramic industry, according to the preamble of claim 1.
  • the heating curve can be adapted relatively easily to the fluctuations in the mass flow of the firing material; however, it is difficult to optimally set the cooling curve at the same time. It was therefore necessary to develop a control system to optimize the cooling curve.
  • Tunnel stoves are operated in countercurrent and consist of a heating zone with a flue gas outlet at the beginning and burners at the end, a combustion zone with differently divided burner groups as required, and also a cooling zone, usually with rapid cooling at the beginning, with the cold air is fed directly into the furnace in order to bring about a faster drop in temperature, subsequently - as a rule - with one or more direct extraction systems, with which air is extracted from the cooling zone, in order to control the shape of the cooling curve by changing the mass flow, and from a supply air fan on the exit side of the cooling zone, with which the differential mass resulting from the air mass balance of the furnace is fed into the furnace.
  • the amount of smoke gas to be extracted in older ovens is usually via the negative pressure in the heating zone certainly.
  • the amount of flue gas to be extracted in the heating zone of the furnace is usually regulated via the temperature at a point in the heating zone of the furnace, which is established there by the ratio of the heat capacity flows of fuel and air, or via the flue gas temperature.
  • the temperature curve in the heating zone is kept constant despite different mass flows of firing material.
  • this has the consequence that the mass flow in the cooling zone changes continuously and, at least in the region up to the first direct extraction in the direction of advance of the combustion material, cannot be influenced by the known means.
  • An increase in the performance of the rapid cooling would only lead to the fact that the temperature curve in this area flattens or even rises again in this area due to the associated reduction in the amount of cooling air, which can lead to considerable disadvantages for the quality of the ceramic product to be cooled .
  • With the subsequent direct extraction only the cooling section behind it can be influenced, but not the critical area between rapid cooling and the first direct extraction.
  • This control system which depends on the maximum and minimum temperature gradients in the heating zone an optimization of the temperature gradient in the critical area of the cooling zone enables, at the same time, a better recuperation of the heat capacity of the fuel mass flow in the cooling zone and thus a lower heat requirement of the furnace.
  • Another advantage of the invention is that a noticeable energy saving can be achieved.
  • the firing material 2 is pushed from the entrance 3 to the exit 4 while the furnace gases are drawn in counterflow from the exit side 4 of the furnace to the flue gas extractor 5, near the entrance 3.
  • the output of the flue gas fan 6 is constantly regulated via the negative pressure which is measured at any point in the heating zone A.
  • maximum / minimum temperature limit values detected by thermocouples are provided at any point in the heating zone A or in the flue gas outlet 5, which serve as reference variables when the temperature limit values are reached.
  • the burners 7 in the combustion zone B and the rapid cooling 8 at the beginning of the cooling zone C are regulated in a known manner depending on the temperature.
  • the performance of the first direct suction 9 and a further direct suction 10 is also known Constantly controlled via a temperature in the direction of the firing material mass flow after the direct suction units 9, 10.
  • the output of the supply air fan 11 is constantly regulated via the pressure at any point in the cooling zone, which can be, for example, between the rapid cooling 8 and the first direct extraction 9.
  • maximum-minimum temperature limit values detected by thermocouples are provided as a further controlled variable at a point between rapid cooling 8 and first direct suction 9. If the upper temperature limit is exceeded, this triggers an incremental increase in the pressure setpoint of the supply air fan 11 by an adjustable size. If the temperature falls below the lower limit, this gradually lowers the pressure setpoint of the supply air fan by an adjustable amount. Maximum and minimum pressure are limited.
  • the pressure drop in the furnace is increased or decreased and thus adapted to the mass flow in the critical area of the cooling zone so that the cooling curve in this area does not exceed a certain temperature gradient. or falls below.
  • the pressure control in the heating zone A will attempt to compensate for the higher pressure drop by increasing the speed of the flue gas fan 6, so that, as desired, the air mass flow is increased until the upper temperature limit in the heating zone is reached, which thus limits the entire adaptation process upwards; the same - vice versa - is the case when the pressure level in the cooling zone is reduced.

Landscapes

  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Furnace Details (AREA)
  • Waste-Gas Treatment And Other Accessory Devices For Furnaces (AREA)
  • Tunnel Furnaces (AREA)
  • Control Of Temperature (AREA)
EP89105526A 1988-06-29 1989-03-29 Système de régulation pour un four tunnel fonctionnant à contre-courant Expired - Lifetime EP0348603B1 (fr)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
DE3821858 1988-06-29
DE3821858A DE3821858C1 (fr) 1988-06-29 1988-06-29

Publications (3)

Publication Number Publication Date
EP0348603A2 true EP0348603A2 (fr) 1990-01-03
EP0348603A3 EP0348603A3 (fr) 1992-01-02
EP0348603B1 EP0348603B1 (fr) 1994-06-01

Family

ID=6357475

Family Applications (1)

Application Number Title Priority Date Filing Date
EP89105526A Expired - Lifetime EP0348603B1 (fr) 1988-06-29 1989-03-29 Système de régulation pour un four tunnel fonctionnant à contre-courant

Country Status (3)

Country Link
EP (1) EP0348603B1 (fr)
AT (1) ATE106538T1 (fr)
DE (2) DE3821858C1 (fr)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0690280A1 (fr) * 1994-07-01 1996-01-03 Hans Lingl Anlagenbau und Verfahrenstechnik GmbH & Co. KG Transfert thermique dans un four tunnel
FR2725266A1 (fr) * 1994-09-29 1996-04-05 Riedhammer Gmbh Co Kg Dispositif de regulation de la pression d'un gaz dans des zones voisines d'un four a passage continu
WO2007085317A1 (fr) * 2006-01-26 2007-08-02 Sacmi Forni S.P.A. Processus et appareil pour une gestion optimisée d'un four pour carreaux en céramique
CN105202912A (zh) * 2015-10-23 2015-12-30 青岛铸英特陶科技有限公司 燃气辊道窑炉

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
NL1000909C1 (nl) * 1995-08-01 1995-11-10 Flynn Controls B V Temperatuurregelaar voor een tunneloven.

Family Cites Families (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3142884A (en) * 1961-10-19 1964-08-04 Pullman Inc Method and apparatus for controlling the cooling zone of a tunnel kiln
DE1303473C2 (de) * 1966-04-06 1974-01-17 Keller Ofenbau Gmbh, 4533 Laggenbeck Verfahren zum kontinuierlichen brennen von keramischem einsatzgut in tunneloefen und tunnelofen zur durchfuehrung des verfahrens
DE2357057B2 (de) * 1973-11-15 1976-12-30 Leisenberg, Manfred, 6312 Laubach Verfahren und vorrichtung zur luftmengenregelung in einem tunnelofen

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0690280A1 (fr) * 1994-07-01 1996-01-03 Hans Lingl Anlagenbau und Verfahrenstechnik GmbH & Co. KG Transfert thermique dans un four tunnel
US5613847A (en) * 1994-07-01 1997-03-25 Hans Lingl Anlagenbau Und Verfahrenstechnik Gmbh & Co. Heat transfer in a tunnel kiln
FR2725266A1 (fr) * 1994-09-29 1996-04-05 Riedhammer Gmbh Co Kg Dispositif de regulation de la pression d'un gaz dans des zones voisines d'un four a passage continu
WO2007085317A1 (fr) * 2006-01-26 2007-08-02 Sacmi Forni S.P.A. Processus et appareil pour une gestion optimisée d'un four pour carreaux en céramique
CN105202912A (zh) * 2015-10-23 2015-12-30 青岛铸英特陶科技有限公司 燃气辊道窑炉

Also Published As

Publication number Publication date
EP0348603B1 (fr) 1994-06-01
EP0348603A3 (fr) 1992-01-02
ATE106538T1 (de) 1994-06-15
DE3821858C1 (fr) 1989-11-23
DE58907741D1 (de) 1994-07-07

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