EP1682719A2 - Device for the production and/or treatment of strip or sheet material - Google Patents
Device for the production and/or treatment of strip or sheet materialInfo
- Publication number
- EP1682719A2 EP1682719A2 EP04791256A EP04791256A EP1682719A2 EP 1682719 A2 EP1682719 A2 EP 1682719A2 EP 04791256 A EP04791256 A EP 04791256A EP 04791256 A EP04791256 A EP 04791256A EP 1682719 A2 EP1682719 A2 EP 1682719A2
- Authority
- EP
- European Patent Office
- Prior art keywords
- fuel cell
- drying
- cell unit
- machine
- gas
- 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.)
- Withdrawn
Links
- 239000000463 material Substances 0.000 title claims abstract description 48
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 10
- 239000000446 fuel Substances 0.000 claims abstract description 76
- 238000010438 heat treatment Methods 0.000 claims abstract description 26
- 239000011111 cardboard Substances 0.000 claims abstract description 3
- 239000011087 paperboard Substances 0.000 claims abstract description 3
- 238000001035 drying Methods 0.000 claims description 104
- 238000000034 method Methods 0.000 claims description 6
- 239000012530 fluid Substances 0.000 claims description 2
- 239000007789 gas Substances 0.000 description 43
- 239000000123 paper Substances 0.000 description 8
- 239000011248 coating agent Substances 0.000 description 5
- 238000000576 coating method Methods 0.000 description 5
- 230000005855 radiation Effects 0.000 description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 3
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 2
- 230000005611 electricity Effects 0.000 description 2
- 239000002737 fuel gas Substances 0.000 description 2
- 238000009499 grossing Methods 0.000 description 2
- 239000001257 hydrogen Substances 0.000 description 2
- 229910052739 hydrogen Inorganic materials 0.000 description 2
- 238000007603 infrared drying Methods 0.000 description 2
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 2
- 239000001301 oxygen Substances 0.000 description 2
- 229910052760 oxygen Inorganic materials 0.000 description 2
- 238000004381 surface treatment Methods 0.000 description 2
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 1
- 230000005540 biological transmission Effects 0.000 description 1
- 238000002485 combustion reaction Methods 0.000 description 1
- 239000003344 environmental pollutant Substances 0.000 description 1
- 239000000284 extract Substances 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 238000007602 hot air drying Methods 0.000 description 1
- 150000002431 hydrogen Chemical class 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 239000003345 natural gas Substances 0.000 description 1
- 230000002093 peripheral effect Effects 0.000 description 1
- 231100000719 pollutant Toxicity 0.000 description 1
- 230000001105 regulatory effect Effects 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 238000005496 tempering Methods 0.000 description 1
Classifications
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21F—PAPER-MAKING MACHINES; METHODS OF PRODUCING PAPER THEREON
- D21F5/00—Dryer section of machines for making continuous webs of paper
- D21F5/02—Drying on cylinders
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21F—PAPER-MAKING MACHINES; METHODS OF PRODUCING PAPER THEREON
- D21F5/00—Dryer section of machines for making continuous webs of paper
- D21F5/001—Drying webs by radiant heating
- D21F5/002—Drying webs by radiant heating from infrared-emitting elements
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21F—PAPER-MAKING MACHINES; METHODS OF PRODUCING PAPER THEREON
- D21F5/00—Dryer section of machines for making continuous webs of paper
- D21F5/02—Drying on cylinders
- D21F5/04—Drying on cylinders on two or more drying cylinders
- D21F5/042—Drying on cylinders on two or more drying cylinders in combination with suction or blowing devices
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21F—PAPER-MAKING MACHINES; METHODS OF PRODUCING PAPER THEREON
- D21F5/00—Dryer section of machines for making continuous webs of paper
- D21F5/18—Drying webs by hot air
- D21F5/185—Supporting webs in hot air dryers
- D21F5/187—Supporting webs in hot air dryers by air jets
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M2250/00—Fuel cells for particular applications; Specific features of fuel cell system
- H01M2250/10—Fuel cells in stationary systems, e.g. emergency power source in plant
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02B—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO BUILDINGS, e.g. HOUSING, HOUSE APPLIANCES OR RELATED END-USER APPLICATIONS
- Y02B90/00—Enabling technologies or technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02B90/10—Applications of fuel cells in buildings
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/30—Hydrogen technology
- Y02E60/50—Fuel cells
Definitions
- the present invention relates to a machine for the production and / or treatment of web or sheet material, in particular paper or cardboard.
- Such machines include, for example, paper machines which are known from the paper industry.
- paper machines essentially comprise a headbox in which the paper stock is fed and distributed evenly, a wire section in which the sheet is formed by a filtration process, a press section in which pulp water contained in the material web is expelled by means of pressure, and a drying section Drying the material web, a surface tempering section, for example a coating device, for smoothing, coating, etc. the material web, as well as a reel for the finished material web.
- further drying devices can be provided in this part of the system.
- sub-processes in the manufacture or / and processing of web or sheet material are often carried out in separate plants.
- an offline coating device can be used for the surface coating of a paper web or a calender for smoothing.
- drying cylinders in which a material web to be dried passes through an arrangement of drying cylinders, is particularly common for drying devices, such as the drying section or the surface treatment section.
- a drying felt which absorbs the moisture of the material web and is dried on a felt dryer in a return area of the arrangement.
- the material web to be dried is threaded between the drying felt and the heated drying cylinders and thus brought into close contact with the respective drying cylinder on the one hand and the drying felt on the other (contact drying).
- steam which is taken as process steam from another section of the paper machine or is made available with the aid of electrical energy, for example using cogeneration.
- gas-powered steam generators is also known.
- Hot air dryers are also used to dry a running material web, which heat an air stream to a temperature of several hundred degrees Celsius and thus act on the material web to be dried.
- Such hot air dryers are operated with gas and have various known advantages over drying cylinder arrangements, such as the possibility of contactless web guidance, a high power density and a higher operating speed. On the other hand, however, they are associated with higher operating and acquisition costs.
- Has heating section the operation of these heating sections, especially in
- Another object of the invention is to provide drying devices for a machine of the type mentioned above, which can be operated in an effective and energy-saving manner.
- the present invention provides that the machine is connected to at least one assigned fuel cell unit, such that thermal energy generated by the fuel cell unit can be supplied to the machine as operating energy.
- a fuel cell is used in a manner known per se to convert chemical energy into electrical energy.
- the classic fuel cell comprises an anode and a cathode, to which hydrogen or oxygen are supplied as energy sources. Inside the cell, the hydrogen oxidizes, releasing water and free charges, which are made available via the electrodes as electrical energy in the form of a direct current. Fuel cells used to generate electricity can now achieve an efficiency of more than 50 percent.
- One type of fuel cell that is preferably used to generate electricity operates at an operating temperature of approximately 600 ° C.-1,000 ° C. If the associated thermal energy according to the invention is now supplied to the machine for the production and / or treatment of web or sheet material, this energy can flow into the energy balance of the machine. In addition, when operating fuel cell systems as exhaust gases, essentially only hot air and water vapor are generated, so that pollution of the environment of the machine and the environment is avoided.
- Part of the energy generated by the fuel cell as for the machine usable energy is provided, such a combination of a fuel cell unit and a machine for the production and / or treatment of web or sheet material can provide an overall system with particularly high efficiency.
- At least one heating section of the machine which is designed to do so, during an operating state of the machine to heat or to be heated, thermal energy generated by the fuel cell unit can be supplied as operating energy.
- the exhaust air emitted by the fuel cell unit can be supplied to the at least one heating section.
- the exhaust air from a fuel cell has a temperature of about 300 ° C to 600 ° C and thus represents a simple transmission medium for the transport of thermal energy from the fuel cell to the machine.
- the at least one heating section or at least one of the heating sections comprises a drying device, through which the web or sheet material can be passed or / and along which the sheet or sheet material can be guided
- the drying device at least one heatable Drying roller comprises, along which the web or sheet material can be guided directly or adjacent to a drying felt running on the drying roller, thermal energy generated by the fuel cell unit being able to be supplied to the drying roller.
- the thermal energy required by a drying device with heatable drying rollers for heating the drying rollers can thus be supplied effectively by a fuel cell unit.
- exhaust air emitted by the fuel cell unit flows through the at least one drying roller and / or that a fluid flows through the drying roller, which contains thermal energy generated by the fuel cell unit, in particular from the Exhaust air emitted from the fuel cell unit can be supplied. This ensures uniform and continuous heating of the drying rollers.
- a machine designed according to the invention comprises a hot gas drying device, through which the web or sheet material can be passed or / and along which the web or sheet material can be guided, the hot gas drying device being based on drying gas works with which the web or sheet material can be acted upon, the drying gas being able to be provided on the basis of thermal energy emitted by the fuel cell unit.
- the drying gas can be heated to an operating temperature in an economical manner and without significant pollutant emission, using the thermal energy of the fuel cell unit.
- exhaust air emitted by the fuel cell unit can be combined with gas provided by a gas supply, as a result of which the heat transfer from the fuel cell unit to the gas is achieved in a particularly simple manner using the exhaust air.
- exhaust air emitted by the fuel cell unit can be fed to a heat exchanger which is designed to heat gas provided by a gas supply and thus to provide it as a drying gas.
- the paths of the exhaust air and the drying gas can be separated from one another.
- exhaust air emitted by the fuel cell unit can be supplied as drying gas to the hot gas drying device. This variant is structurally particularly simple and therefore inexpensive, since the provision of a separate drying gas and a heat exchanger is not necessary.
- the fuel cell unit in the vicinity, preferably at a distance of less than approximately 100 meters, of at least one heating section of the machine. Losses of thermal energy, in particular in guide channels for heat transfer media which transmit the thermal energy from the fuel cell to the heating section of the machine, can thus be reduced.
- the invention also provides a combination of a machine according to the type described above with the associated fuel cell unit.
- the invention provides a method for producing or / and treating, in particular for heating or / and drying, sheet or sheet material using a machine, in particular a machine according to one of claims 1 to 11, in which the machine consists of a fuel cell unit generated thermal (and possibly also electrical) energy is supplied.
- the machine consists of a fuel cell unit generated thermal (and possibly also electrical) energy is supplied.
- FIG. 1 shows a drying device of a machine combined with a fuel cell unit according to the first embodiment of the present invention.
- FIG. 2 shows a drying device of a machine according to the second embodiment of the present invention.
- 3 and 4 each show further exemplary embodiments for drying devices of a machine according to the invention.
- the drying device 10 comprises an arrangement of drying rollers 12 in two mutually parallel rows.
- a drying felt 16 is guided around the drying rollers 12 of a row with the aid of felt guide rollers 14 in such a way that it rotates about two thirds of each drying roller 12 and is then guided around a felt dryer 18.
- a material web section 20 to be dried enters the drying device 10 on the left in FIG. 1 by running between the drying felt 16 of the first row and the first drying roller 12 of the first row.
- the material web section 20 then runs around a first drying roller 12 of the second row, again enclosed between the drying roller 12 on the one hand and a second drying felt 16 of the second row on the other.
- each drying roller 12 is connected to a feed channel 22, via which a heating medium can be fed to the respective drying cylinder 12.
- a supply channel 22 is provided for each row of drying rollers 12, both supply channels 22 being connected to a main supply line 24, which in turn is connected to a fuel cell unit 26.
- the main feed line 24 is fed with the exhaust air from the fuel cell unit 24, which then flows into the feed channels 22 at a temperature of several hundred degrees Celsius and is fed directly from there into the individual drying rollers 12.
- the exhaust air supplied there gives off part of its thermal energy to the drying rollers 12, for example on the walls thereof, as a result of which the drying rollers 12 are heated to a certain temperature or are kept at a certain temperature.
- the exhaust air After the exhaust air has released at least part of its thermal energy to the drying rollers 12, it flows out of the drying rollers 12 through openings (not shown) and can then be derived or reused.
- a heat exchanger whose primary side is heated by the hot exhaust air and whose secondary side is connected to the drying rollers 12 in via a heat transfer medium is in thermal contact to transfer the thermal energy of the exhaust air to the drying rollers 12. It is then also conceivable for the fuel cell unit 26 to also provide any electrical energy required to drive pumps, motors or the like for moving the exhaust air or the heat transfer medium.
- a fuel cell unit with a high-temperature fuel cell whose operating temperature is in the range from approximately 600 ° C. to approximately 1,000 ° C.
- An example of such a fuel cell unit 26, shown schematically in FIG. 1, comprises a gas processing unit 28, a central unit 30 with fuel cell stacks 32 arranged therein and an electrical unit 34 with an energy processing unit 36 and a control / regulating unit 38.
- the gas processing unit is supplied with fresh air via a fresh air inlet 40 and via a gas inlet 42 is supplied with natural gas, town gas, or other suitable fuel gas.
- the gas supplied via the gas inlet 42 is processed in the gas processing unit, in particular desulphurized and preheated, and then supplied to the central unit 30 as process gas via a gas line 44.
- the fresh air supplied to the gas processing unit 28 via the fresh air inlet 40 is fed to the central unit 30 via a fresh air line 46.
- process gas and atmospheric oxygen react at the electrodes of the fuel cell stack 32 to form electrical charges and thermal energy.
- the thermal energy generated is removed from the central unit 30 in the form of hot exhaust air and returns via an exhaust air line 48 to the gas processing unit 28, from which it exits through an exhaust air outlet 50.
- the exhaust air leaves the fuel cell unit 26 at a temperature of approximately 400 ° C. or at a temperature of approximately 600 ° C.
- the one in the combustion process on the electrodes of the fuel cell Charges generated are discharged via a power line 43 and made available to the energy processing unit 36 of the electrical unit 34.
- the energy processing unit 36 can convert the direct current supplied by the fuel cell into an alternating current, which can ultimately be used by a consumer.
- the operation of the fuel cell unit 26 is controlled and monitored by a control unit 38, which is connected to the central unit 30 and the gas treatment unit 28 via lines 45 and 39, respectively.
- FIG. 2 shows a hot gas drying device 100 of a machine according to the second embodiment of the present invention.
- the hot gas drying device 100 comprises two blower units 152, to which hot exhaust air from a fuel cell unit 126, which is only indicated schematically, can be supplied via heating gas connections 154 and air via fresh air connections 156.
- the air is brought into thermal contact with the hot exhaust gas via a heat exchanger and heated to an operating temperature.
- the heated air then flows as drying gas from nozzles 158 in the blower units 152 and acts on a web of material 120 passed between the blower units 152.
- the drying of the web of material 120 thus takes place in a stream of hot drying gas without contact, using the thermal energy provided by the fuel cell unit 126.
- cooled exhaust air leaves the blower unit 152 via outlets 160.
- blower units 152 can also be designed in such a way that the fresh air supplied is mixed with the supplied exhaust air of the fuel cell unit in the blower units 152 and the resulting gas mixture leaves the blower units 152 through the nozzles 158 as drying gas, around the material web 120 to act upon.
- a fresh air supply line entirely dispense and let the exhaust air of the fuel cell unit 126 exit directly from the nozzles 158 of the blower units 152 in order to dry the material web 120 directly in the flow of the hot exhaust air.
- FIG. 3 illustrates an exemplary embodiment of the present invention, in which an infrared drying device 200 of a machine, for example a paper machine, is connected to the exhaust air outlet 250 of a fuel cell unit 226, which is only indicated in FIG. 3.
- the infrared drying device 200 comprises two infrared radiators 252 with radiation surfaces 258, which face a material web 220 to be dried and carried out between the infrared radiators 252.
- Hot exhaust air from the fuel cell unit 226 is fed to the infrared radiators 252 via heating gas connections 254, which then releases part of its thermal energy to the infrared radiators 252 and then leaves the infrared radiators 252 via outlets 260.
- the exhaust air from the fuel cell unit 226 is thus brought into thermal contact with the infrared radiators 252 in order to heat the radiation surfaces 258 of the infrared radiators 252 to an operating temperature.
- the radiation surfaces 258 then radiate heat radiation in the direction of the material web 220 to be dried, as a result of which this is heated and dried.
- FIG. 4 shows another example of a drying device of a machine according to the present invention.
- hot exhaust air is fed to a blower unit 352 via a heating gas connection 354 to a fuel cell unit 326, which heats fresh air there, analogously to the drying device 100 from FIG was fed to the blower unit 352 via a fresh air connection 356.
- the fresh air thus heated to an operating temperature then flows out of the blower unit 352 through nozzles 358 and acts on a material web 320 which is guided past the blower unit 352. Cooled exhaust air leaves the blower unit 352 via an outlet 360.
- the surface 362 facing the material web 320, in which the nozzles 358 are also arranged has a convex curvature, so that the path of the material web 320 has a curvature in this area.
- the material web 320 runs on an air bed which is formed by the hot drying gas emerging from the nozzles 358.
- This principle for deflecting a running material web is known as a so-called air turn.
- a blower unit 352 which is designed in accordance with the principle of an air turn and is now supplied with hot exhaust air from a fuel cell unit 326, the hot air drying device according to the invention can also be used for material web deflection.
Landscapes
- Drying Of Solid Materials (AREA)
- Paper (AREA)
- Fuel Cell (AREA)
Abstract
Description
Claims
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE10351623A DE10351623A1 (en) | 2003-11-05 | 2003-11-05 | Arrangement for producing or / and treating web or sheet material |
PCT/EP2004/052580 WO2005045130A2 (en) | 2003-11-05 | 2004-10-20 | Device for the production and/or treatment of strip or sheet material |
Publications (1)
Publication Number | Publication Date |
---|---|
EP1682719A2 true EP1682719A2 (en) | 2006-07-26 |
Family
ID=34559344
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP04791256A Withdrawn EP1682719A2 (en) | 2003-11-05 | 2004-10-20 | Device for the production and/or treatment of strip or sheet material |
Country Status (6)
Country | Link |
---|---|
US (1) | US20080023166A1 (en) |
EP (1) | EP1682719A2 (en) |
JP (1) | JP2007514118A (en) |
CN (1) | CN1875149A (en) |
DE (1) | DE10351623A1 (en) |
WO (1) | WO2005045130A2 (en) |
Families Citing this family (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE102005037856A1 (en) * | 2005-08-10 | 2007-02-15 | Voith Patent Gmbh | Method for generating process heat and / or electrical energy |
WO2011010609A1 (en) * | 2009-07-24 | 2011-01-27 | 王子製紙株式会社 | Method for manufacturing a fiber sheet |
Family Cites Families (12)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CA937045A (en) * | 1969-08-18 | 1973-11-20 | Dominion Engineering Works | Integrated drying processes and apparatus |
FI58953B (en) * | 1977-12-22 | 1981-01-30 | Valmet Oy | EXTENSION OF MEASUREMENT OF THERMAL MECHANICAL MASS OF BODY MACHINERY |
CA1206197A (en) * | 1982-08-19 | 1986-06-17 | Hansraj C. Maru | Use of low temperature blowers for recirculation of hot gas |
JPS62257496A (en) * | 1986-04-25 | 1987-11-10 | 三菱重工業株式会社 | Heat recovery of papermaking dryer |
JPS6361721A (en) * | 1986-09-02 | 1988-03-17 | Takuma Co Ltd | Waste heat utilizing dryer system |
JPH074837A (en) * | 1993-06-14 | 1995-01-10 | Kawasaki Steel Corp | Method of heating steel-strip and apparatus therefor |
FR2732044B1 (en) * | 1995-03-20 | 1997-04-30 | Kaysersberg Sa | METHOD FOR WRINGING A SHEET OF CELLULOSIC MATERIAL BY HOT AIR PASSING THROUGH UNDER A HIGH VACUUM |
JPH1064566A (en) * | 1996-08-14 | 1998-03-06 | Shikoku Sogo Kenkyusho:Kk | Fuel cell power generator and waste heat recovery method therefor |
JP2000117042A (en) * | 1998-10-15 | 2000-04-25 | Matsushita Seiko Co Ltd | Dry type dehumidifier |
JP2001068126A (en) * | 1999-08-25 | 2001-03-16 | Daikin Ind Ltd | Fuel cell power generating system |
JP2002153844A (en) * | 2000-11-16 | 2002-05-28 | Mitsubishi Heavy Ind Ltd | Method for treating organic waste and system therefor |
JP2003282082A (en) * | 2002-03-25 | 2003-10-03 | Mitsubishi Materials Corp | Power generating and hot-water supplying system for kitchen |
-
2003
- 2003-11-05 DE DE10351623A patent/DE10351623A1/en not_active Withdrawn
-
2004
- 2004-10-20 JP JP2006537278A patent/JP2007514118A/en active Pending
- 2004-10-20 CN CNA2004800316418A patent/CN1875149A/en active Pending
- 2004-10-20 WO PCT/EP2004/052580 patent/WO2005045130A2/en active Application Filing
- 2004-10-20 US US10/578,422 patent/US20080023166A1/en not_active Abandoned
- 2004-10-20 EP EP04791256A patent/EP1682719A2/en not_active Withdrawn
Non-Patent Citations (1)
Title |
---|
See references of WO2005045130A2 * |
Also Published As
Publication number | Publication date |
---|---|
WO2005045130A2 (en) | 2005-05-19 |
JP2007514118A (en) | 2007-05-31 |
CN1875149A (en) | 2006-12-06 |
WO2005045130A3 (en) | 2005-07-07 |
DE10351623A1 (en) | 2005-06-16 |
US20080023166A1 (en) | 2008-01-31 |
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Legal Events
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PUAI | Public reference made under article 153(3) epc to a published international application that has entered the european phase |
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Owner name: VOITH PATENT GMBH |
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DAX | Request for extension of the european patent (deleted) | ||
17Q | First examination report despatched |
Effective date: 20080513 |
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RIC1 | Information provided on ipc code assigned before grant |
Ipc: D21F 5/18 20060101ALI20130605BHEP Ipc: D21F 5/02 20060101AFI20130605BHEP Ipc: D21F 5/04 20060101ALI20130605BHEP |
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Free format text: STATUS: THE APPLICATION IS DEEMED TO BE WITHDRAWN |
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18D | Application deemed to be withdrawn |
Effective date: 20140501 |