EP2924380B1 - Brûleur supplémentaire - Google Patents

Brûleur supplémentaire Download PDF

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Publication number
EP2924380B1
EP2924380B1 EP14162383.5A EP14162383A EP2924380B1 EP 2924380 B1 EP2924380 B1 EP 2924380B1 EP 14162383 A EP14162383 A EP 14162383A EP 2924380 B1 EP2924380 B1 EP 2924380B1
Authority
EP
European Patent Office
Prior art keywords
air
clean gas
heat source
line
return line
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.)
Active
Application number
EP14162383.5A
Other languages
German (de)
English (en)
Other versions
EP2924380A1 (fr
Inventor
Sabine Schindler
Norbert Heckmann
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.)
Individual
Original Assignee
Individual
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 Individual filed Critical Individual
Priority to PL14162383T priority Critical patent/PL2924380T3/pl
Priority to EP14162383.5A priority patent/EP2924380B1/fr
Priority to ES14162383.5T priority patent/ES2618455T3/es
Priority to CN201510138588.1A priority patent/CN104949499B/zh
Priority to US14/671,119 priority patent/US10254044B2/en
Publication of EP2924380A1 publication Critical patent/EP2924380A1/fr
Application granted granted Critical
Publication of EP2924380B1 publication Critical patent/EP2924380B1/fr
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Classifications

    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F26—DRYING
    • F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
    • F26B23/00—Heating arrangements
    • F26B23/001—Heating arrangements using waste heat
    • F26B23/002—Heating arrangements using waste heat recovered from dryer exhaust gases
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F26—DRYING
    • F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
    • F26B21/00—Arrangements or duct systems, e.g. in combination with pallet boxes, for supplying and controlling air or gases for drying solid materials or objects
    • F26B21/02—Circulating air or gases in closed cycles, e.g. wholly within the drying enclosure
    • F26B21/04—Circulating air or gases in closed cycles, e.g. wholly within the drying enclosure partly outside the drying enclosure
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F26—DRYING
    • F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
    • F26B23/00—Heating arrangements
    • F26B23/02—Heating arrangements using combustion heating
    • F26B23/022—Heating 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
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F26—DRYING
    • F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
    • F26B2210/00—Drying processes and machines for solid objects characterised by the specific requirements of the drying good
    • F26B2210/12—Vehicle bodies, e.g. after being painted

Definitions

  • the invention relates to a device for the efficient use of hot air streams in a dryer system for dry goods, especially for a vehicle painting plant, the exhaust air is heated in a thermal afterburner and can be supplied as clean gas Um Kunststoffrekuperatoren and at least one Frischluftrekuperator.
  • the freshly painted drying goods such as karts
  • the Karrossen After heating in the heating zone of the dryer, for example, the Karrossen enter the holding zone of the dryer at about 140 ° C - 180 ° C. Then the karrossen leave the dryer.
  • exhaust air raw gas
  • TSV thermal afterburner
  • the exhaust air is preheated regularly in an exhaust air recuperator.
  • the clean gas from the post-combustion system initially cools down in the exhaust air recuperator and is then used to heat the dryer. This is done in such a way that the clean gas is passed through recirculation recuperators, which heat the recirculated air removed from the dryer again, whereupon the recirculated air is returned to the dryer becomes.
  • the clean gas can still be passed through a fresh air recuperator to heat the fresh air to be supplied to the dryer.
  • the aim is to operate the thermal afterburner not at full load, but at partial load.
  • the invention has for its object to provide a device for energy saving in drying systems.
  • the device has at least one additional heat source for the clean gas and a recirculation system with at least one parallel to the clean gas line recirculation line, which is connected to the clean gas line in the last Umluftrekuperators and in the additional heat source.
  • the clean gas can be additionally heated.
  • the design variable is the adequate oxidative conversion of the substances under full load operation.
  • Regulating the temperature is easier than regulating volumetric flows.
  • the additional heat source can be controlled out of the process so that it only adds as much additional heat energy as needed for the process.
  • a recirculation system has at least one return line parallel to the clean gas line, wherein the return line and the clean gas line are linked via connections in the region of the additional heat source and before the last circulating air recuperator. Clean gas can be diverted from the clean gas line before the last circulating air recuperator and fed via the return line into the area of the additional heat source.
  • a fan is preferably included in the return line, in particular for conversion and maintenance purposes, the return line can also be closed by a closure element.
  • clean gas is taken from an area in front of the last recirculating air recuperator and returned to the area of the additional heat source.
  • the clean gas guided through the clean gas line is completely discharged via a chimney after passing through the recuperators.
  • a fixed volume flow over the chimney as well as a fixed volume flow as circulating air are constantly driven.
  • the lower exhaust air volume flow is supplemented by the proportion of recirculated air, equal to an increase in the clean gas volume flow in the area of recirculating air recuperators.
  • the additional heat source provides only as much heat energy as needed.
  • the operation of the additional heat source is controlled by means of the temperature conditions in the last Um Kunststoffrekuperator.
  • the last recirculating air recuperator is last supplied with clean gas. If it is determined that the temperature in this last recirculating air recuperator falls below a set value, the additional heat source will be started because it is controlled by the temperature conditions in this recirculating air recirculation circuit.
  • the additional heat source is preferably an auxiliary burner that can be operated with the same fuel as the thermal afterburning.
  • the auxiliary burner is assigned to the clean gas line so that it can act on the clean gas before it reaches the first recirculating air recuperator.
  • the dryer 1 has an inlet lock 2, a heating zone 3, a holding zone 4 and an outlet lock 5.
  • the arrow 6 symbolizes the introduction of the dry goods, for example bodies, which are located on SKIDs.
  • the arrow 7 symbolizes the entry of the solvents, which are introduced with the color coatings of the dried goods in the dryer.
  • the arrow 8 symbolizes the dry goods leaving the dryer and SKIDs.
  • the thermal afterburner TNV is designated 9.
  • 10 to 13 are circulating air recuperators. 13a is an exhaust recuperator and 15 is a fresh air recuperator. With 21 an exhaust chimney is called.
  • the arrows 22 indicate the supply of fresh air from the environment.
  • the exhaust ducts are at 18 and the circulating air lines are designated 17.
  • the the dryer 1 via the exhaust ducts 18 extracted exhaust (raw gas) is a fan unit 19 and the Ab povertyrekuperator 13 of the TNV. 9 supplied and subjected there to the oxidation process.
  • the cleaned by the conversion exhaust air leaves the TNV 9 as clean gas in the clean gas line 20.
  • the clean gas is first passed through the Abluftrekuperator 13a, then through the Um Kunststoffrekuperatoren 10 to 13 and finally flows through the Frischluftrekuperator 15, whereupon it via the exhaust chimney 21 into the atmosphere exit.
  • flaps 26 are used. They correspond with flaps 25 in diversions 27 of the clean gas line 20.
  • the last Umluftrekuperator 13 is a bypass line 16 associated with a corresponding flap 26.
  • the flaps 25 and 26 establish a regulated flow of the clean gas and circulating air through the Umbuchrekuperatoren 10 to 13 ago. A regulation of the circulating air and the clean gas is then not carried out, but the temperature of the clean gas and circulating air is regulated.
  • the clean gas line 20 is connected to a return line 25 prior to entry into the last recirculating air recuperator 13.
  • the return line 25 leads back into the region of the auxiliary burner 14, where it is linked to the line piece 22.
  • a fan 27 and a closure flap 28 is inserted in the return line 25 in the return line 25, a fan 27 and a closure flap 28 is inserted.

Landscapes

  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Sustainable Development (AREA)
  • Chemical & Material Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Drying Of Solid Materials (AREA)
  • Coating Apparatus (AREA)
  • Air Supply (AREA)

Claims (5)

  1. Dispositif pour l'utilisation efficace des flux d'air chaud dans un système de séchage pour des matériaux de séchage, en particulier pour une installation de peinture de véhicules, comprenant un séchoir (1) dont l'air d'échappement est chauffé dans une installation de postcombustion thermique (9) et peut être amené en tant que gaz purifié à des récupérateurs d'air ambiant (10-13) ou à au moins un récupérateur d'air frais (15), dans lequel il présente au moins une source de chaleur supplémentaire (14) pour le gaz purifié,
    caractérisé en ce qu'il présente un système de circulation d'air avec au moins une conduite de retour (25) menée parallèlement à la conduite de gaz purifié (20), laquelle est raccordée à la conduite de gaz purifié (20) dans la zone du dernier récupérateur d'air ambiant (13) et dans la zone de la source de chaleur supplémentaire.
  2. Dispositif selon la revendication 1, caractérisé en ce que la source de chaleur supplémentaire est un brûleur supplémentaire (14).
  3. Dispositif selon la revendication 1 ou 2, caractérisé en ce que la source de chaleur supplémentaire de la conduite de gaz purifié (20) est associée au premier récupérateur d'air ambiant (10).
  4. Dispositif selon l'une des revendications 1 à 3, caractérisé en ce qu'au moins un ventilateur (27) est disposé dans la conduite de retour (25).
  5. Dispositif selon la revendication 4, caractérisé en ce qu'au moins un élément de fermeture (28) pour les milieux circulant à travers la conduite de retour (25) est disposé dans la conduite de retour (25).
EP14162383.5A 2014-03-28 2014-03-28 Brûleur supplémentaire Active EP2924380B1 (fr)

Priority Applications (5)

Application Number Priority Date Filing Date Title
PL14162383T PL2924380T3 (pl) 2014-03-28 2014-03-28 Palnik dodatkowy
EP14162383.5A EP2924380B1 (fr) 2014-03-28 2014-03-28 Brûleur supplémentaire
ES14162383.5T ES2618455T3 (es) 2014-03-28 2014-03-28 Quemador adicional
CN201510138588.1A CN104949499B (zh) 2014-03-28 2015-03-27 辅助燃烧器
US14/671,119 US10254044B2 (en) 2014-03-28 2015-03-27 Method and device for extracting, heating, and recirculating waste air from a dryer system

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
EP14162383.5A EP2924380B1 (fr) 2014-03-28 2014-03-28 Brûleur supplémentaire

Publications (2)

Publication Number Publication Date
EP2924380A1 EP2924380A1 (fr) 2015-09-30
EP2924380B1 true EP2924380B1 (fr) 2016-12-07

Family

ID=50424037

Family Applications (1)

Application Number Title Priority Date Filing Date
EP14162383.5A Active EP2924380B1 (fr) 2014-03-28 2014-03-28 Brûleur supplémentaire

Country Status (5)

Country Link
US (1) US10254044B2 (fr)
EP (1) EP2924380B1 (fr)
CN (1) CN104949499B (fr)
ES (1) ES2618455T3 (fr)
PL (1) PL2924380T3 (fr)

Families Citing this family (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE102015214706A1 (de) 2015-07-31 2017-02-02 Dürr Systems Ag Behandlungsanlage und Verfahren zum Behandeln von Werkstücken
DE102015214711A1 (de) * 2015-07-31 2017-02-02 Dürr Systems Ag Behandlungsanlage und Verfahren zum Behandeln von Werkstücken
DE102015012848A1 (de) * 2015-10-06 2017-04-06 Eisenmann Se Vorrichtung zur Temperierung von Gegenständen sowie Verfahren zur Steuerung einer Vorrichtung zur Temperierung von Gegenständen
DE102015224916A1 (de) * 2015-12-10 2017-06-14 Dürr Systems Ag Behandlungsanlage und Verfahren zum Behandeln von Werkstücken
US11058550B2 (en) 2019-10-04 2021-07-13 Pain TEQ, LLC Allograft implant for fusing a sacroiliac joint
DE102022131532A1 (de) 2022-11-29 2024-05-29 Bayerische Motoren Werke Aktiengesellschaft Behandlungsanlage zum Behandeln von Werkstücken und Verfahren zum Behandeln von Werkstücken

Family Cites Families (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE19735322A1 (de) * 1997-08-14 1999-02-18 Bayerische Motoren Werke Ag Durchlauflufttrocknungsanlage
DE10125771C1 (de) * 2001-05-26 2002-11-21 Eisenmann Kg Maschbau Trockner
DE102008012792B4 (de) 2008-03-05 2013-01-03 Eisenmann Ag Trockner für Lackieranlage
EP2295909B1 (fr) * 2009-09-10 2016-02-24 Crone, Fokko Procédé d'utilisation efficace des flux d'air chaud dans un système de séchage, notamment pour un atelier de peinture de véhicules
DE102010001234A1 (de) * 2010-01-26 2011-07-28 Dürr Systems GmbH, 74321 Anlage zum Trocknen von Karossen mit Gasturbine
CN203061402U (zh) 2012-12-03 2013-07-17 兰州吉利汽车工业有限公司 一种汽车涂装热能回收系统

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
None *

Also Published As

Publication number Publication date
ES2618455T3 (es) 2017-06-21
PL2924380T3 (pl) 2017-06-30
CN104949499A (zh) 2015-09-30
EP2924380A1 (fr) 2015-09-30
US10254044B2 (en) 2019-04-09
CN104949499B (zh) 2019-07-09
US20150276315A1 (en) 2015-10-01

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