EP2354740A2 - Dispositif et procédé de traitement thermique de bandes de produits en forme de bandes - Google Patents

Dispositif et procédé de traitement thermique de bandes de produits en forme de bandes Download PDF

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Publication number
EP2354740A2
EP2354740A2 EP11151441A EP11151441A EP2354740A2 EP 2354740 A2 EP2354740 A2 EP 2354740A2 EP 11151441 A EP11151441 A EP 11151441A EP 11151441 A EP11151441 A EP 11151441A EP 2354740 A2 EP2354740 A2 EP 2354740A2
Authority
EP
European Patent Office
Prior art keywords
treatment
air
fields
supply air
heating system
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
EP11151441A
Other languages
German (de)
English (en)
Other versions
EP2354740B1 (fr
EP2354740A3 (fr
Inventor
Michael Christ
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.)
Brueckner Trockentechnik GmbH and Co KG
Original Assignee
Brueckner Trockentechnik 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.)
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Publication date
Application filed by Brueckner Trockentechnik GmbH and Co KG filed Critical Brueckner Trockentechnik GmbH and Co KG
Publication of EP2354740A2 publication Critical patent/EP2354740A2/fr
Publication of EP2354740A3 publication Critical patent/EP2354740A3/fr
Application granted granted Critical
Publication of EP2354740B1 publication Critical patent/EP2354740B1/fr
Not-in-force legal-status Critical Current
Anticipated expiration legal-status Critical

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Classifications

    • DTEXTILES; PAPER
    • D06TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
    • D06BTREATING TEXTILE MATERIALS USING LIQUIDS, GASES OR VAPOURS
    • D06B15/00Removing liquids, gases or vapours from textile materials in association with treatment of the materials by liquids, gases or vapours
    • D06B15/09Removing liquids, gases or vapours from textile materials in association with treatment of the materials by liquids, gases or vapours by jets of gases
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F26DRYING
    • F26BDRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
    • F26B13/00Machines and apparatus for drying fabrics, fibres, yarns, or other materials in long lengths, with progressive movement
    • F26B13/10Arrangements for feeding, heating or supporting materials; Controlling movement, tension or position of materials
    • DTEXTILES; PAPER
    • D06TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
    • D06CFINISHING, DRESSING, TENTERING OR STRETCHING TEXTILE FABRICS
    • D06C7/00Heating or cooling textile fabrics
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F26DRYING
    • F26BDRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
    • F26B21/00Arrangements or duct systems, e.g. in combination with pallet boxes, for supplying and controlling air or gases for drying solid materials or objects
    • F26B21/02Circulating air or gases in closed cycles, e.g. wholly within the drying enclosure
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F26DRYING
    • F26BDRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
    • F26B21/00Arrangements or duct systems, e.g. in combination with pallet boxes, for supplying and controlling air or gases for drying solid materials or objects
    • F26B21/06Controlling, e.g. regulating, parameters of gas supply
    • F26B21/10Temperature; Pressure
    • 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

Definitions

  • the invention relates to a device and a method for heat treatment of web-shaped, in particular textile webs with a plurality of successive treatment fields.
  • the DE 100 10 842 B4 consists of the device for the treatment of webs, in particular for drying textile webs, essentially of a housing, at least one treatment field for acting on the web with a treatment gas, means for supplying fresh air into the housing and means for discharging moisture-laden exhaust air the housing.
  • a mixing device is further provided, which provides one or more inflow openings for the circulating circulating air, one or more inflow openings for the fresh air and a discharge opening for the treatment gas and further comprises adjusting means by which the present in the treatment gas ratio of fresh air circulating circulating air is adjustable.
  • a burner device is provided in the region of the mixing device, which has a flame guide tube and wherein inflow openings for the circulating circulating air and the fresh air are provided, which are arranged concentrically around the flame guide tube.
  • a device for heat treatment of textile webs which consists essentially of a plurality of successive treatment zones, which are designed as impact jet ventilation zones and means for deriving the exhaust air of the impact jet ventilation zones. Furthermore, an upstream in the transport direction of the web treatment zone is provided, which is designed as a ventilation zone, wherein the means for discharging the exhaust air of the impact jet ventilation zones are connected to the ventilation zone such that the exhaust air is passed through the web.
  • the treatment gas is blown onto the web in order to dry it, for example, whereby the treatment gas absorbs the moisture.
  • the exhaust air By the exhaust air is passed through the web in the upstream aeration zone, the exhaust air can continue to cool down to the cooling limit temperature, wherein energy is supplied to the web. This causes an increase in the efficiency of the drying performance and an energy saving.
  • the invention is based on the object to take further measures to save energy.
  • the treatment gas is through Burner devices, which are arranged in each treatment field, brought to the required temperature. It had to be accepted that the burner devices in different treatment fields have to be partly operated with different power.
  • the required heat output in particular by the properties of the web and / or a changing ratio of supply air and circulating circulating air, vary, so that the burner devices can not always be operated at the optimum operating point and thereby often can not exploit their full efficiency.
  • the heat required to adjust the temperature of the treatment gas can be generated centrally.
  • Each treatment device only removes the required amount of heat, with the amount of heat that has not been removed being returned via the loop.
  • the central Auflieiz coupled, in particular a central combustion chamber, always be driven in the optimal control range, whereby a more complete burnout and better energy utilization is ensured.
  • the replacement of the plurality of burners (in the individual treatment fields) by a central heating system results in a significant cost savings.
  • the central heating system is designed to heat the supply air and the means for supplying the supply air are formed by the loop, which in turn communicates with the mixing means of the plurality of treatment fields.
  • the supply air is heated centrally and fed via the loop to the individual treatment fields, while excess supply air is returned to the central heating system.
  • the treatment fields each comprise a heat exchanger for heating the treatment gas, the heat exchangers of the treatment fields being connected on their hot side via the loop to the central heating system.
  • the central heating system has a connection for supplying fresh air.
  • the treatment fields can be followed by a fresh air-operated cooling field, which has a connection for supplying fresh air and a connection connected to the central heating system for discharging preheated fresh air.
  • the central heating system can be controlled as a function of at least one parameter of the exhaust air produced in the treatment fields, in particular as a function of the carbon content and / or the humidity and / or the temperature of the supply air.
  • a first embodiment of the invention is shown schematically.
  • This is, for example, a device for heat treatment of textile webs.
  • the webs may also be, for example, nonwovens, coatings of textile supports such as carpet backings, artificial leather and the like.
  • other, non-textile, web-shaped webs come into consideration.
  • a textile material web 4 is transported through the treatment fields by means of transport means 4a, which are indicated schematically only by arrows, in the expanded state.
  • transport means 4a which are indicated schematically only by arrows, in the expanded state.
  • jet ventilation zones with lower and upper nozzle systems 5, 6 are formed, which extend over the entire width of the web, so that the web is acted upon both from above and from below with a treatment gas 7.
  • the treatment gas 7 is composed of a certain ratio of supply air 8 and circulating circulating air 9, wherein the supply air 8 in a central heating system 10 (FIG. Figure 1C ) is heated and fed via a ring line 11 the individual treatment fields 1 to 3.
  • a temperature-controlled controller 12 Via a temperature-controlled controller 12, an actuator 13a arranged in front of a mixing device 13b is actuated in order to maintain the temperature of the treatment gas 7 at a predetermined level of, for example, 200 ° C. by admixing hot supply air 8.
  • different temperatures can also be set in the individual treatment fields.
  • the treatment gas 7 is applied to the web 4 by means of one or more fans 14 via the lower and upper nozzle systems 5, 6.
  • the amount of supply air 8 supplied to the treatment gas is discharged in a corresponding amount in the form of exhaust air 15 via a central device 16.
  • All other half-fields 1b to 3a are constructed in an analogous manner, wherein the supply of the treatment gas to the nozzle systems 5, 6 in successive half fields always takes place alternately from the one or the other side.
  • the central heating system 10 is accommodated for heating the supply air, which communicates via the ring line 11 with the mixing devices 13b of the treatment fields 1 to 3. It consists in the illustrated embodiment essentially of a central combustion chamber 10a and a central heat exchanger 10b, the two ends of the loop 11 are connected to the combustion chamber 10a, so that unused supply air to the central heating system 10 is returned and can be used again.
  • the central heating system also has a connection 17 for supplying fresh air 18 provided on the heat exchanger 10b.
  • the heat exchanger is further connected to the means 16 for removing the exhaust air 15, so that the supplied via the port 17 fresh air 8 is preheated with the exhaust gases 15 from the treatment fields before the fresh air is fed in the combustion chamber 10 a.
  • the treatment field 3 is still a downstream of the fresh air 18 cooled box 20 downstream, which has a connection 20a for supplying the fresh air 18 and a connection with the central heating system 10 in connection 20b for discharging preheated fresh air.
  • the cooling field 20 may optionally be designed as a baffle ventilation zone 20c or as a ventilation zone 20d, wherein the fresh air is either inflated from above and below onto the material web 4 (impact jet ventilation zone 20c) or the fresh air is forced through the material web 4 and / or drawn in (aeration zone 20d).
  • the control of the central heating system via an only schematically indicated control device (see Fig. 1b ).
  • the pressure in the loop 11 is measured after the last, connected half-field via a pressure sensor 22 and used to control the amount of fresh air.
  • the combustion chamber 10a is controlled as a function of at least one parameter of the exhaust air, in particular as a function of the carbon content and / or the humidity and / or the temperature of the supply air 8, wherein both combustion air 10c, fuel 10d and fresh air quantity can be controlled.
  • the device is driven in the predetermined nominal ranges or with predetermined nominal values.
  • the entire device is housed within a housing 24, wherein in particular the ring line 11 and the central means 16 for discharging the exhaust air and the central heating system are disposed within the housing.
  • the central heating system is preferably arranged below the nozzle systems 5, 6 of the last treatment field 3 in the transport direction (arrow 4a). As in particular from the Fig. 3 and 4 As can be seen, the combustion chamber 10a and the heat exchanger below the lower nozzle system 5 can be installed. There is still sufficient space for the mixing device 13b of the last treatment field. This creates a very compact device.
  • a heat exchanger 25 for indirect heating of the treatment gas 7 is arranged in each treatment field or half-field.
  • a central heating system 26 is provided, which in turn comprises a central combustion chamber 26a and a central heat exchanger 26b.
  • the hot sides of the heat exchangers 25 in the individual treatment fields are connected to the central combustion chamber 26 a of the central heating system 26 via a ring line, which is formed here with flow and return lines 11 a 11 b.
  • the hot loop air generated in the combustion chamber 26a is the individual heat exchangers via actuators 27 as needed for indirect heating of the treatment gas available.
  • fresh air 18 is heated by means of the hot exhaust air 15 of the treatment fields and fed as supply air via lines 28 to the treatment fields.
  • the exhaust air used in the heat exchanger 26b is discharged, optionally after filtering, as exhaust air 19.
  • the treatment gas is adjusted by mixing the preheated supply air 8 with the circulating circulating air 9, before it is indirectly heated in the heat exchanger to the required temperature of, for example, 200 ° C.
  • the unused ring air is returned to the central combustion chamber 26a.
  • flow and return lines 11a, 11b could Of course, only a single loop can be provided. When using two lines, the individual treatment fields are arranged according to a parallel connection, when using a line, this corresponds to a series connection of the treatment fields. It would also be conceivable that the flow and return lines 11a, 11b are merged after the last treatment field to form a line.
  • the last treatment field can again be followed by a cooling field in order to preheat the fresh air upstream of the heat exchanger 26b.
  • the device for heat treatment of the web further comprises the above-described control device.
  • the central heating system may be in communication with all of the treatment fields of the web-like web heat-treating device, or may cover only a part of the device, such as the front or back half. However, it is also conceivable that a first, central heating system for the front half and a second, central heating system for the rear half is provided.
  • a suction zone for the web is provided, this is particularly suitable for preheating the fresh air.

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  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Textile Engineering (AREA)
  • Treatment Of Fiber Materials (AREA)
EP11151441.0A 2010-02-02 2011-01-19 Dispositif et procédé de traitement thermique de bandes de produits en forme de bandes Not-in-force EP2354740B1 (fr)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
DE102010006577A DE102010006577A1 (de) 2010-02-02 2010-02-02 Vorrichtung und Verfahren zur Wärmebehandlung von bahnförmigen Warenbahnen

Publications (3)

Publication Number Publication Date
EP2354740A2 true EP2354740A2 (fr) 2011-08-10
EP2354740A3 EP2354740A3 (fr) 2013-12-11
EP2354740B1 EP2354740B1 (fr) 2017-03-08

Family

ID=43587154

Family Applications (1)

Application Number Title Priority Date Filing Date
EP11151441.0A Not-in-force EP2354740B1 (fr) 2010-02-02 2011-01-19 Dispositif et procédé de traitement thermique de bandes de produits en forme de bandes

Country Status (6)

Country Link
US (1) US20110185589A1 (fr)
EP (1) EP2354740B1 (fr)
KR (1) KR20110090817A (fr)
DE (1) DE102010006577A1 (fr)
ES (1) ES2620461T3 (fr)
TW (1) TW201144727A (fr)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP2639535A2 (fr) 2012-03-13 2013-09-18 Brückner Trockentechnik GmbH & Co. KG Dispositif et procédé de traitement thermique de bandes de produits en forme de bandes
WO2017101894A1 (fr) * 2015-12-17 2017-06-22 Olbrich Gmbh Procédé pour traiter un adhésif et dispositif correspondant

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP1830146A2 (fr) 2006-03-13 2007-09-05 Brückner Trockentechnik GmbH & Co. KG Dispositif destiné à guider des bandes de matériau textile
DE10010842B4 (de) 2000-03-06 2009-10-01 Brückner Trockentechnik GmbH & Co. KG Vorrichtung zur Behandlung von Warenbahnen

Family Cites Families (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2441357A (en) * 1938-07-30 1948-05-11 Joseph Hibbert & Company Ltd Apparatus for drying and cooling fabrics
US2952078A (en) * 1953-11-30 1960-09-13 Cyril A Litzler Apparatus for controlled heating and cooling of continuous textile material
US3793741A (en) * 1972-01-07 1974-02-26 Smitherm Industries Drying apparatus with moisture profile control
US4017254A (en) * 1975-12-15 1977-04-12 S. J. Agnew Recirculating furnace-dryer combination
JPS59225277A (ja) * 1983-06-02 1984-12-18 和歌山鉄工株式会社 布帛処理用熱風浄化循環装置
DE3822703C1 (en) * 1988-07-05 1989-11-16 Jean-Louis Hermann Hauset Be Nieberding Air-duct system
DE19918669A1 (de) * 1999-04-23 2000-10-26 Heidelberger Druckmasch Ag Trockner mit integrierter Kühleinheit
DE10233754B4 (de) * 2002-07-25 2005-11-24 A. Monforts Textilmaschinen Gmbh & Co.Kg Textilmaschine mit Umluftheizung durch gasbeheizte Wärmetauscher

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE10010842B4 (de) 2000-03-06 2009-10-01 Brückner Trockentechnik GmbH & Co. KG Vorrichtung zur Behandlung von Warenbahnen
EP1830146A2 (fr) 2006-03-13 2007-09-05 Brückner Trockentechnik GmbH & Co. KG Dispositif destiné à guider des bandes de matériau textile

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP2639535A2 (fr) 2012-03-13 2013-09-18 Brückner Trockentechnik GmbH & Co. KG Dispositif et procédé de traitement thermique de bandes de produits en forme de bandes
DE102012102096A1 (de) * 2012-03-13 2013-09-19 Brückner Trockentechnik GmbH & Co. KG Vorrichtung und Verfahren zur Wärmebehandlung von bahnförmigen Warenbahnen
EP2639535A3 (fr) * 2012-03-13 2015-09-09 Brückner Trockentechnik GmbH & Co. KG Dispositif et procédé de traitement thermique de bandes de produits en forme de bandes
WO2017101894A1 (fr) * 2015-12-17 2017-06-22 Olbrich Gmbh Procédé pour traiter un adhésif et dispositif correspondant
CN107922635A (zh) * 2015-12-17 2018-04-17 奥布里希有限责任公司 用于处理粘合剂的工艺及其装置
US10780446B2 (en) 2015-12-17 2020-09-22 Olbrich Gmbh Process for processing an adhesive and a device therefor
CN107922635B (zh) * 2015-12-17 2021-04-06 奥布里希有限责任公司 用于处理粘合剂的工艺及其装置

Also Published As

Publication number Publication date
CN102192642A (zh) 2011-09-21
EP2354740B1 (fr) 2017-03-08
US20110185589A1 (en) 2011-08-04
DE102010006577A1 (de) 2011-08-04
TW201144727A (en) 2011-12-16
ES2620461T3 (es) 2017-06-28
EP2354740A3 (fr) 2013-12-11
KR20110090817A (ko) 2011-08-10

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