EP1398587A2 - Sécheur d'objets, notamment de carrosseries de véhicules, ainsi que procédé de fonctionnement d'un tel sécheur - Google Patents

Sécheur d'objets, notamment de carrosseries de véhicules, ainsi que procédé de fonctionnement d'un tel sécheur Download PDF

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Publication number
EP1398587A2
EP1398587A2 EP03018518A EP03018518A EP1398587A2 EP 1398587 A2 EP1398587 A2 EP 1398587A2 EP 03018518 A EP03018518 A EP 03018518A EP 03018518 A EP03018518 A EP 03018518A EP 1398587 A2 EP1398587 A2 EP 1398587A2
Authority
EP
European Patent Office
Prior art keywords
air
catalytic
dryer
connection
objects
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
EP03018518A
Other languages
German (de)
English (en)
Other versions
EP1398587B1 (fr
EP1398587A3 (fr
Inventor
Heiko Schneider
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.)
Eisenmann Anlagenbau GmbH and Co KG
Original Assignee
Eisenmann Anlagenbau 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 Eisenmann Anlagenbau GmbH and Co KG filed Critical Eisenmann Anlagenbau GmbH and Co KG
Publication of EP1398587A2 publication Critical patent/EP1398587A2/fr
Publication of EP1398587A3 publication Critical patent/EP1398587A3/fr
Application granted granted Critical
Publication of EP1398587B1 publication Critical patent/EP1398587B1/fr
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F26DRYING
    • F26BDRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
    • F26B23/00Heating arrangements
    • F26B23/02Heating arrangements using combustion heating
    • F26B23/022Heating arrangements using combustion heating incinerating volatiles in the dryer exhaust gases, the produced hot gases being wholly, partly or not recycled into the drying enclosure
    • F26B23/024Heating arrangements using combustion heating incinerating volatiles in the dryer exhaust gases, the produced hot gases being wholly, partly or not recycled into the drying enclosure by means of catalytic oxidation
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F26DRYING
    • F26BDRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
    • F26B3/00Drying solid materials or objects by processes involving the application of heat
    • F26B3/28Drying solid materials or objects by processes involving the application of heat by radiation, e.g. from the sun
    • F26B3/30Drying solid materials or objects by processes involving the application of heat by radiation, e.g. from the sun from infrared-emitting elements
    • F26B3/305Drying solid materials or objects by processes involving the application of heat by radiation, e.g. from the sun from infrared-emitting elements the infrared radiation being generated by combustion or combustion gases
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F26DRYING
    • F26BDRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
    • F26B2210/00Drying processes and machines for solid objects characterised by the specific requirements of the drying good
    • F26B2210/12Vehicle bodies, e.g. after being painted

Definitions

  • Dryers that use catalytic lamps as a heat source are enjoying increasing popularity.
  • This for good Reason On the one hand is the primary energy used, namely the combustion gas (natural gas, propane, butane or liquid gas), very inexpensive compared to electrical energy.
  • To the another can be one with such catalytic emitters Infrared radiation especially in that long-wave Create an area that is used for drying or firing coatings, especially paint finishes particularly, effectively is. Energy savings are also achieved by that essentially only the one to be dried Coating, but not other objects heated become.
  • the long-wave radiation from a catalytic emitter the property by a compared with short or medium-wave rays moderate energy density the subject Warm and dry gently.
  • Impurities contained in this supply air thus remained unoxidized, so that the removed from the dryer Exhaust air from a separate exhaust air cleaning device, for example a thermal, a regenerative or a catalytic afterburning device had to be fed.
  • a separate exhaust air cleaning device for example a thermal, a regenerative or a catalytic afterburning device had to be fed.
  • These devices then served often as collective disposal for everyone with organic Substances, especially exhaust air volume flows loaded with solvents, those in the entire facility, so not only in the dryer.
  • the object of the present invention is a dryer of the type mentioned in such a way that on a separate exhaust gas cleaning device is dispensed with can be or at least the amount of exhaust air can be reduced so that the separate exhaust gas purification device kept smaller and therefore cheaper can be.
  • the idea of the invention is as follows: if catalytic emitters are used that do not require air cooling, can put the entire in the drying room of the dryer Supply air via the connection of the catalytic lamp for forced air to be directed, so that all supply air that enters the drying room at least once on the catalytically active layer flowed past or through the catalytically active layer is. In this way it becomes possible to use the catalytic oxidative conversion of organic impurities to be carried out in the supply air as a controlled reaction, including quantitative predictions of reaction sales possible are.
  • the supply air supplied to the dryer can partially from the dryer itself, but also from other parts of the system originate, so that the dryer as a "collective disposal facility" So far for the entire system provided separate exhaust air cleaning devices can replace in whole or in part.
  • the catalytic emitter can have a connection via which is only supplied with air.
  • This Supply air is placed in one place within the catalytic heater directed from which it is a surface of the catalytic flow to the active layer. This will Conditions created under which a controlled Implementation of the organic contained in the supply air Contamination takes place.
  • a fan For convective heating of the objects to be dried a fan can be provided with which the air in the Drying room can be circulated.
  • an embodiment of the invention can be achieved in which the dryer is multi-stage is formed, with each stage in the in one of the Claims 1 to 4 described manner is formed and the connection for exhaust air from the upstream Stage with the connection for the supply air each downstream stage is connected.
  • the dryer is multi-stage is formed, with each stage in the in one of the Claims 1 to 4 described manner is formed and the connection for exhaust air from the upstream Stage with the connection for the supply air each downstream stage is connected.
  • the object of the present invention is also a Method for operating a dryer at the beginning Specify the type in which the in the dryer contained catalytic emitters in a targeted and controllable manner used to clean the supply air supplied to the dryer can be.
  • the total dryer provided with the reference number 1 comprises a dryer Housing 2 with an outer wall 2a and an inner wall 2 B.
  • the inner wall 2b of the housing 2 encloses one Drying room 3 by a device 4, z. Legs Partition, in two air-technical separated Sub-rooms 3a and 3b is divided.
  • Freshly painted Vehicle bodies are not shown in the drawing shown locks, coming from the left, into the sub-area 3a by means of a likewise not shown Conveyor system introduced by this through a the device 4 provided lock in the subspace 3b transferred and leave the housing 2 of the dryer 1 by another not shown in the drawing Lock.
  • each catalytic emitter 5 includes 5 an outer housing 6 and an inner housing 7, between which a flow gap serving as air guidance 8 remains.
  • the outer case 6 and the inner case 7 are on the lower in Figure 2, the drying room in operation 3 facing side open.
  • the inner housing 7 of the catalytic emitter 5 contains from top down a gas distribution device 9, in which a gas supply line 10 opens, an insulation layer 11, an electrical preheater 12 and one catalytically active layer 13, which on the in Figure 2 downward-facing side is exposed.
  • the entire catalytic emitter 5 is by the choice of materials used designed to withstand high temperatures, therefore also required at operating temperatures of for example 250 to 300 ° C no cooling air.
  • Air supply connector 14 of the catalytic radiator 5 connected are supplied with supply air.
  • This supply air can z.
  • the contained in the sub-room 3a of the drying room 3 Air can be drawn through a line 16 in which a blower 17 lies, circulate. Branches from line 16 a further line 18 leading to the air supply nozzle 14 in the second sub-room 3b of the drying room 3 arranged catalytic radiator 5 leads. That too Sub-space 3b is assigned a circulation line 19, in which is another blower 20. From the circulation line 19 leads an exhaust duct 21 to the outside atmosphere.
  • the dryer 1 described above works as follows:
  • the catalytically active layers 13 of the different catalytic rays 5 with the help the electrical preheaters 12 to a temperature preheated from approx. 150 to 200 ° C, for catalytic Oxidation of the combustion gas is required.
  • the catalytic emitters 5 in both sub-rooms 3a, 3b of the drying room 3 via the respective gas supply lines 10 combustion gas supplied. This is in the corresponding catalytic emitter 5 by the gas distribution device 9 over the entire flow cross-section evened out, penetrates the insulating layer 11, which also because of their flow resistance a contribution to the equalization of the gas flow performs, and then reaches the preheated catalytic active layer 13.
  • FIG Dryer 1 The airways are shown in detail in FIG Dryer 1 as follows:
  • the air in sub-room 3a is blown with the help of the blower 17 circulated and an air stream drawn off via line 18, the - converted to the same temperature - that Air volume corresponds to that through the line 15 is supplied.
  • the air circulated by the fan also overflows the object to be dried and heats it convectively.
  • the amount of circulated air also determines whose temperature is the amount of energy transferred.
  • the catalytic emitters 5 transfer to the one to be dried Subject energy in the form of infrared radiation. This Amount of energy is by the amount of combustion gas that is supplied through the lines 10, and through the Distance between the object to be dried and the Catalytic radiators 5 determined.
  • a second type is shown as the Catalytic radiator 5 can be supplied with supply air.
  • the catalytic emitter 5 of FIG. 3 coincides with that of Figure 2 are identical.
  • Via the gas supply line 10, however, does not become a pure combustion gas, but a mixture of polluted supply air and combustion gas inside the catalytic emitter 5 initiated.
  • This mixture is in a premixer 23 produced, the combustion gas via a first line 24 and via a second line 25 containing pollutants Exhaust air is supplied.
  • the lines are installed in the dryer 1 of FIG. 1 25 the premixer 23 the catalytic emitter 5, the assigned to the left subspace 3a of the drying room 3 are parallel to the branch lines 15a, 15b to the Line 15 connected, through which the contaminated supply air comes from the evaporation zone while the ducts 25, which is the right in FIG. 1 subspace 3b of the drying room 3 are assigned, parallel to the lines 18a, 18b leading to the already pre-cleaned air Line 18 are connected.
  • the ratio in which the combustion gas 24 in the premixers 23 is mixed with air set that according to the pollution of the Air catalytic oxidation as complete as possible the pollutants take place. In a corresponding way the proportion of the polluted air via line 25 to the premixer and what proportion over the air supply nozzle 14 is supplied to the catalytic emitter 5.

Landscapes

  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Sustainable Development (AREA)
  • Microbiology (AREA)
  • Drying Of Solid Materials (AREA)
  • Exhaust Gas Treatment By Means Of Catalyst (AREA)
EP03018518A 2002-09-16 2003-08-16 Sécheur d'objets, notamment de carrosseries de véhicules, ainsi que procédé de fonctionnement d'un tel sécheur Expired - Lifetime EP1398587B1 (fr)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
DE10242944A DE10242944B4 (de) 2002-09-16 2002-09-16 Trockner für Gegenstände, insbesondere für Fahrzeugkarosserien, sowie Verfahren zum Betreiben eines solchen Trockners
DE10242944 2002-09-16

Publications (3)

Publication Number Publication Date
EP1398587A2 true EP1398587A2 (fr) 2004-03-17
EP1398587A3 EP1398587A3 (fr) 2006-05-10
EP1398587B1 EP1398587B1 (fr) 2008-07-30

Family

ID=31724806

Family Applications (1)

Application Number Title Priority Date Filing Date
EP03018518A Expired - Lifetime EP1398587B1 (fr) 2002-09-16 2003-08-16 Sécheur d'objets, notamment de carrosseries de véhicules, ainsi que procédé de fonctionnement d'un tel sécheur

Country Status (3)

Country Link
US (1) US6889446B2 (fr)
EP (1) EP1398587B1 (fr)
DE (2) DE10242944B4 (fr)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP2177852A1 (fr) * 2008-10-15 2010-04-21 Symach S.r.l. Appareil pour le séchage d'un produit de peinture et son procédé de fonctionnement
WO2013117637A3 (fr) * 2012-02-11 2013-10-24 Technische Universität Bergakademie Freiberg Procédé de séchage d'un produit traité au moyen d'une substance contenant un solvant

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP2177276A1 (fr) * 2008-10-15 2010-04-21 Symach S.r.l. Procédé pour la peinture de carrosséries de véhicules
US8524330B2 (en) * 2009-03-06 2013-09-03 GM Global Technology Operations LLC Method and apparatus for paint curing
US11229925B2 (en) * 2020-03-12 2022-01-25 Ayotte Techno-Gaz Inc. System and process for curing a wet coating applied to a substrate

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3865076A (en) * 1973-08-27 1975-02-11 Burdett Manufacturing Co Finishing line heat recovery
EP0389652A1 (fr) * 1989-03-28 1990-10-03 Siemens Aktiengesellschaft Panneau radiateur catalytique
DE19544417A1 (de) * 1995-11-29 1997-06-05 Bernhard Dipl Ing Dahm Katalytischer Brenner
WO2000058678A1 (fr) * 1999-03-25 2000-10-05 Sunkiss Equipement de chauffage par emission surfacique d'un rayonnement infrarouge, du type tunnel

Family Cites Families (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
SU1575032A1 (ru) * 1988-01-26 1990-06-30 Прибалтийский Сектор Центрального Проектно-Конструкторского Бюро "Ремстройпроект" Радиационно-конвективна сушильна установка
US5594999A (en) * 1991-05-15 1997-01-21 Haden Schweitzer Corporation Radiant wall oven and process for generating infrared radiation having a nonuniform emission distribution
DE4312892A1 (de) * 1993-04-21 1994-10-27 Burkamp En Und Anlagentechnik Lacktrocknungsanlage
JP3251157B2 (ja) * 1995-10-03 2002-01-28 株式会社大氣社 塗装乾燥炉

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3865076A (en) * 1973-08-27 1975-02-11 Burdett Manufacturing Co Finishing line heat recovery
EP0389652A1 (fr) * 1989-03-28 1990-10-03 Siemens Aktiengesellschaft Panneau radiateur catalytique
DE19544417A1 (de) * 1995-11-29 1997-06-05 Bernhard Dipl Ing Dahm Katalytischer Brenner
WO2000058678A1 (fr) * 1999-03-25 2000-10-05 Sunkiss Equipement de chauffage par emission surfacique d'un rayonnement infrarouge, du type tunnel

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
DATABASE WPI Section PQ, Week 199109 Derwent Publications Ltd., London, GB; Class Q76, AN 1991-064224 XP002372065 & SU 1 575 032 A (BALTIC REMSTROIPROE) 30. Juni 1990 (1990-06-30) *

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP2177852A1 (fr) * 2008-10-15 2010-04-21 Symach S.r.l. Appareil pour le séchage d'un produit de peinture et son procédé de fonctionnement
US8291610B2 (en) 2008-10-15 2012-10-23 Symach S.R.L. Apparatus for drying a painting product and operating method thereof
WO2013117637A3 (fr) * 2012-02-11 2013-10-24 Technische Universität Bergakademie Freiberg Procédé de séchage d'un produit traité au moyen d'une substance contenant un solvant

Also Published As

Publication number Publication date
EP1398587B1 (fr) 2008-07-30
US6889446B2 (en) 2005-05-10
DE10242944B4 (de) 2005-07-07
EP1398587A3 (fr) 2006-05-10
DE50310231D1 (de) 2008-09-11
DE10242944A1 (de) 2004-03-25
US20040123491A1 (en) 2004-07-01

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