EP2295909A1 - Procédé d'utilisation efficace des flux d'air chaud dans un système de séchage, notamment pour un atelier de peinture de véhicules - Google Patents
Procédé d'utilisation efficace des flux d'air chaud dans un système de séchage, notamment pour un atelier de peinture de véhicules Download PDFInfo
- Publication number
- EP2295909A1 EP2295909A1 EP20090011579 EP09011579A EP2295909A1 EP 2295909 A1 EP2295909 A1 EP 2295909A1 EP 20090011579 EP20090011579 EP 20090011579 EP 09011579 A EP09011579 A EP 09011579A EP 2295909 A1 EP2295909 A1 EP 2295909A1
- Authority
- EP
- European Patent Office
- Prior art keywords
- dryer
- air
- fresh air
- clean gas
- heated
- 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
Links
- 238000000034 method Methods 0.000 title claims abstract description 11
- 238000001035 drying Methods 0.000 title claims description 6
- 238000010422 painting Methods 0.000 title claims description 3
- 239000000203 mixture Substances 0.000 claims abstract description 7
- 238000002485 combustion reaction Methods 0.000 claims description 5
- 230000007812 deficiency Effects 0.000 claims 1
- 230000002265 prevention Effects 0.000 claims 1
- 238000010438 heat treatment Methods 0.000 abstract description 8
- 239000007789 gas Substances 0.000 description 32
- 230000003134 recirculating effect Effects 0.000 description 6
- 239000003973 paint Substances 0.000 description 4
- 238000013459 approach Methods 0.000 description 2
- 239000003054 catalyst Substances 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 2
- 230000001105 regulatory effect Effects 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 229910002092 carbon dioxide Inorganic materials 0.000 description 1
- CURLTUGMZLYLDI-UHFFFAOYSA-N carbon dioxide Natural products O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- 238000009500 colour coating Methods 0.000 description 1
- -1 compounds carbon dioxide Chemical class 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 239000003344 environmental pollutant Substances 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 231100000252 nontoxic Toxicity 0.000 description 1
- 230000003000 nontoxic effect Effects 0.000 description 1
- 239000003960 organic solvent Substances 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 230000001590 oxidative effect Effects 0.000 description 1
- 231100000719 pollutant Toxicity 0.000 description 1
- 230000000630 rising effect Effects 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
- 239000002918 waste heat Substances 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Images
Classifications
-
- 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 method for the efficient use of the hot air streams in a dryer system for dry goods, in particular for a vehicle painting, in which the exhaust air from the dryer is heated in a thermal afterburner and led as clean gas by Um Kunststoffrekuperatoren and at least one Frischluftrekuperator is heated in which the recirculated air removed from the dryer and is returned to the dryer and the fresh air is heated and fed into the dryer.
- the freshly painted dry goods such as karts
- a support frame in the dryer, wherein the organic solvents are in the fresh paint of the dry goods
- 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 - 180 ° C. Then the karrossen leave the dryer.
- gaseous organic substances are removed by suction and fed as exhaust air (raw gas) a thermal afterburner (TNV) for the oxidative conversion of organic substances in the non-toxic compounds carbon dioxide and water vapor.
- TSV thermal afterburner
- the exhaust air Before entering the thermal post-combustion plant, the exhaust air is preheated 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 Umgasrekuperatoren, which heat the recirculated air removed from the dryer, whereupon the circulating air is returned to the dryer. Finally, the clean gas is passed through a fresh air recuperator, in which the fresh air to be supplied to the dryer is heated.
- the invention has for its object to provide a more efficient method for energy saving in drying systems.
- 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 and 12 are circulating air recuperators. 13 is an exhaust air recuperator, 14 is a catalyst stage, 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 gas (crude gas) is fed via a fan unit 19 and the Ab povertyrekuperator 13 of the TNV 9 and there subjected to the oxidation process.
- the cleaned by the conversion exhaust air leaves the TNV as clean gas in the clean gas line 20.
- the clean gas is first passed through the Ab povertyrekuperator 13, then optionally through a catalyst stage 14, the Umluftrekuperator 10 and the Umbuchrekuperator 12 and finally flows through the Frischluftrekuperator 15, whereupon it over the exhaust chimney 21 exits into the atmosphere.
- the heating zone 3 and the holding zone 4 of the dryer 1 is removed via recirculating air ducts 17a circulating air in the Um Kunststoffrekuperatoren 10 and 12 is heated and recycled via recirculating air lines 17b in the heating zone and in the holding zone.
- the inlet sluice 2 operated with negative pressure and the outlet sluice 5 operated with negative pressure are supplied with fresh air from the immediate vicinity (arrows 22).
- Fresh air taken from the atmosphere and / or the installation space is supplied to the fresh air recuperator 15 via a fresh air line 23.
- the heated fresh air is introduced via a fan unit 24 and fresh air partial lines 23a in the recirculating air ducts 17a.
- a fresh air-fresh air mixture is passed through the Umbuchrekuperatoren 10 and 12, which is thus heated and returned via the circulating air lines 17b in the heating zone 3 and in the holding zone 4.
- the temperature of the dryer 1 is regulated via a two flap valve system associated with each recirculating air recuperator 10 and 12 in the clean gas line 20 and in a bypass 27 bypassing the circulating air recuperator. Is requested by the dryer 1 warmer circulating air, so opens a first flap 25 in the clean gas line 20 the path of the clean gas Um Kunststoffrekuperator 10 and at the same time closes a second flap 26 the bypass 27, so that the clean gas flows through the Um Kunststoffrekuperator to there heat energy to the Circulating air. If the dryer 1 requires less heat, the system works in reverse order. The flap 25 in the clean gas line closes and the flap 26 in the bypass 27 opens, so that the clean gas is led around the Umbuchrekuperator 10 via the bypass 27. In the same way, the Umluftrekuperator 12 is moved.
- the combustion chamber temperature of the TNV 9 is set to a constant temperature value, so that the clean gas temperature in the exit from the TNV and after flowing through the Abluftrekuperators 13 also has a constant temperature.
- the required energy requirement of the dryer 1 is automatically regulated via the exit temperature of the clean gas behind the fresh air recuperator 15 at the temperature tap 29 in conjunction with the clean gas volume flow.
- the clean gas temperature at the tap 29 is constantly set to, for example, 80 ° C.
- a control unit 30 measures the clean gas temperature at the tap 29 and gives a manipulated variable to the frequency converter of the fresh air fan unit 24 and the exhaust fan unit 19.
- the TNV 9 then also works with maximum power due to the maximum amount of air. If the individual zones of the dryer finally approach the setpoint temperature of the dryer, the flaps 25 close in the clean gas line and open the flaps 26 in the bypasses 27 at the recirculating air recuperators and the clean gas temperature drops to the maximum setpoint temperature of the clean gas. The controller 30 then lowers the speed of the fresh air and exhaust fan units. The heat output of the TNV 9 drops as the exhaust air volume flow decreases.
- the control unit 30 monitors the clean gas temperature at each Umluftrekuperator 10, 12 behind the flaps 26 at points 34 (T1) in the bypasses 27 and in each subsequent strand of the clean gas line 20 at points 35 (T2 ). If the temperature level behind the flaps 26 (T1) approaches that in the respectively adjacent strand of the clean gas line 20 (T2) to a value to be determined (T1 must always be greater than T2), the reduction of the amounts of exhaust air is stopped. The best possible waste heat utilization is then achieved.
- the self-regulating paint drying system recognizes each of these required conditions and automatically adjusts automatically to each of these dryer operating states.
- the volume flow balance (exhaust air / fresh air) via a determined characteristic of the frequency converter of the fan units 19, 24 as a function of different volume flows or via the volume flow measuring points 31 and 32 in the exhaust duct 18 before the exhaust recuperator 13 and in the fresh air line 23.
- the relative humidity of the clean gas behind the fresh air recuperator 15 measured at the measuring point 33 and displayed. If condensation forms in the exhaust chimney 21, the chimney temperature must be raised by the operator.
- the required air volume balance in the dryer is set once fixed and locked via fixed throttle valves 28 on the exhaust air lines 18 and the individual fresh air supply lines 23a before entering the Um Kunststoffrekuperatoren during commissioning.
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Combustion & Propulsion (AREA)
- Life Sciences & Earth Sciences (AREA)
- Sustainable Development (AREA)
- Drying Of Solid Materials (AREA)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
EP09011579.1A EP2295909B1 (fr) | 2009-09-10 | 2009-09-10 | Procédé d'utilisation efficace des flux d'air chaud dans un système de séchage, notamment pour un atelier de peinture de véhicules |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
EP09011579.1A EP2295909B1 (fr) | 2009-09-10 | 2009-09-10 | Procédé d'utilisation efficace des flux d'air chaud dans un système de séchage, notamment pour un atelier de peinture de véhicules |
Publications (2)
Publication Number | Publication Date |
---|---|
EP2295909A1 true EP2295909A1 (fr) | 2011-03-16 |
EP2295909B1 EP2295909B1 (fr) | 2016-02-24 |
Family
ID=41694592
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP09011579.1A Not-in-force EP2295909B1 (fr) | 2009-09-10 | 2009-09-10 | Procédé d'utilisation efficace des flux d'air chaud dans un système de séchage, notamment pour un atelier de peinture de véhicules |
Country Status (1)
Country | Link |
---|---|
EP (1) | EP2295909B1 (fr) |
Cited By (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2013075793A1 (fr) * | 2011-11-25 | 2013-05-30 | Eisenmann Ag | Dispositif de mise en température d'objets |
EP2633922A1 (fr) * | 2012-03-01 | 2013-09-04 | Eisenmann AG | Dispositif d'utilisation thermique d'un fluide primaire et installation de traitement d'objets avec celui-ci |
EP2924381A1 (fr) * | 2014-03-28 | 2015-09-30 | Sabine Schindler | Alimentation en air frais |
EP2924380A1 (fr) * | 2014-03-28 | 2015-09-30 | Sabine Schindler | Brûleur supplémentaire |
EP2844937B1 (fr) | 2012-05-02 | 2018-03-21 | Dürr Systems AG | Dispositif pourvu d'une chambre de traitement pour pièces d'oeuvre |
DE102017105094A1 (de) | 2017-03-10 | 2018-09-13 | Eisenmann Se | Temperiervorrichtung für oberflächenbehandelte Gegenstände wie Fahrzeugteile |
WO2020015846A1 (fr) | 2018-07-16 | 2020-01-23 | Wenker Gmbh & Co. Kg | Procédé à régulation thermodynamique et installation de séchage à régulation thermodynamique pour le séchage de produits à sécher |
US10928134B2 (en) | 2016-02-17 | 2021-02-23 | Eisenmann Se | Burner unit and device for the temperature control of objects |
Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3218727A (en) * | 1962-07-17 | 1965-11-23 | Dorothy C Lind | Apparatus for freeze-drying and method |
US4662840A (en) * | 1985-09-09 | 1987-05-05 | Hunter Engineering (Canada) Ltd. | Indirect fired oven system for curing coated metal products |
EP0851194A2 (fr) * | 1996-12-23 | 1998-07-01 | Martin Dipl.-Ing. Knabe | Sécheur avec purification de gaz d'échappement par post-combustion thermique |
DE19735322A1 (de) | 1997-08-14 | 1999-02-18 | Bayerische Motoren Werke Ag | Durchlauflufttrocknungsanlage |
EP1076218A1 (fr) * | 1999-08-11 | 2001-02-14 | EISENMANN MASCHINENBAU KG (Komplementär: EISENMANN-Stiftung) | Séchoir pour une installation de peinture |
-
2009
- 2009-09-10 EP EP09011579.1A patent/EP2295909B1/fr not_active Not-in-force
Patent Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3218727A (en) * | 1962-07-17 | 1965-11-23 | Dorothy C Lind | Apparatus for freeze-drying and method |
US4662840A (en) * | 1985-09-09 | 1987-05-05 | Hunter Engineering (Canada) Ltd. | Indirect fired oven system for curing coated metal products |
EP0851194A2 (fr) * | 1996-12-23 | 1998-07-01 | Martin Dipl.-Ing. Knabe | Sécheur avec purification de gaz d'échappement par post-combustion thermique |
DE19735322A1 (de) | 1997-08-14 | 1999-02-18 | Bayerische Motoren Werke Ag | Durchlauflufttrocknungsanlage |
EP1076218A1 (fr) * | 1999-08-11 | 2001-02-14 | EISENMANN MASCHINENBAU KG (Komplementär: EISENMANN-Stiftung) | Séchoir pour une installation de peinture |
Cited By (14)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN103946655A (zh) * | 2011-11-25 | 2014-07-23 | 艾森曼股份公司 | 用于对物体调温的装置 |
WO2013075793A1 (fr) * | 2011-11-25 | 2013-05-30 | Eisenmann Ag | Dispositif de mise en température d'objets |
CN103946655B (zh) * | 2011-11-25 | 2016-06-01 | 艾森曼股份公司 | 用于对物体调温的装置 |
US9410741B2 (en) | 2011-11-25 | 2016-08-09 | Eisenmann Ag | Device for controlling the temperature of objects |
EP2633922A1 (fr) * | 2012-03-01 | 2013-09-04 | Eisenmann AG | Dispositif d'utilisation thermique d'un fluide primaire et installation de traitement d'objets avec celui-ci |
EP2844937B1 (fr) | 2012-05-02 | 2018-03-21 | Dürr Systems AG | Dispositif pourvu d'une chambre de traitement pour pièces d'oeuvre |
EP2844937B2 (fr) † | 2012-05-02 | 2023-05-03 | Dürr Systems AG | Dispositif pourvu d'une chambre de traitement pour pièces d'oeuvre |
EP2924381A1 (fr) * | 2014-03-28 | 2015-09-30 | Sabine Schindler | Alimentation en air frais |
US10254044B2 (en) | 2014-03-28 | 2019-04-09 | Sabine SCHINDLER | Method and device for extracting, heating, and recirculating waste air from a dryer system |
EP2924380A1 (fr) * | 2014-03-28 | 2015-09-30 | Sabine Schindler | Brûleur supplémentaire |
US10928134B2 (en) | 2016-02-17 | 2021-02-23 | Eisenmann Se | Burner unit and device for the temperature control of objects |
DE102017105094A1 (de) | 2017-03-10 | 2018-09-13 | Eisenmann Se | Temperiervorrichtung für oberflächenbehandelte Gegenstände wie Fahrzeugteile |
US11137209B2 (en) | 2017-03-10 | 2021-10-05 | Eisenmann Se | Temperature control device for surface-treated objects such as vehicle parts |
WO2020015846A1 (fr) | 2018-07-16 | 2020-01-23 | Wenker Gmbh & Co. Kg | Procédé à régulation thermodynamique et installation de séchage à régulation thermodynamique pour le séchage de produits à sécher |
Also Published As
Publication number | Publication date |
---|---|
EP2295909B1 (fr) | 2016-02-24 |
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