US20010037540A1 - Filtration device and process for its manufacture - Google Patents
Filtration device and process for its manufacture Download PDFInfo
- Publication number
- US20010037540A1 US20010037540A1 US09/202,147 US20214798A US2001037540A1 US 20010037540 A1 US20010037540 A1 US 20010037540A1 US 20214798 A US20214798 A US 20214798A US 2001037540 A1 US2001037540 A1 US 2001037540A1
- Authority
- US
- United States
- Prior art keywords
- fibres
- web
- process according
- group
- filtration device
- 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
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B60—VEHICLES IN GENERAL
- B60H—ARRANGEMENTS OF HEATING, COOLING, VENTILATING OR OTHER AIR-TREATING DEVICES SPECIALLY ADAPTED FOR PASSENGER OR GOODS SPACES OF VEHICLES
- B60H3/00—Other air-treating devices
- B60H3/06—Filtering
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D39/00—Filtering material for liquid or gaseous fluids
- B01D39/14—Other self-supporting filtering material ; Other filtering material
- B01D39/16—Other self-supporting filtering material ; Other filtering material of organic material, e.g. synthetic fibres
- B01D39/1607—Other self-supporting filtering material ; Other filtering material of organic material, e.g. synthetic fibres the material being fibrous
- B01D39/1623—Other self-supporting filtering material ; Other filtering material of organic material, e.g. synthetic fibres the material being fibrous of synthetic origin
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D39/00—Filtering material for liquid or gaseous fluids
- B01D39/14—Other self-supporting filtering material ; Other filtering material
- B01D39/20—Other self-supporting filtering material ; Other filtering material of inorganic material, e.g. asbestos paper, metallic filtering material of non-woven wires
- B01D39/2003—Glass or glassy material
- B01D39/2017—Glass or glassy material the material being filamentary or fibrous
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D39/00—Filtering material for liquid or gaseous fluids
- B01D39/14—Other self-supporting filtering material ; Other filtering material
- B01D39/20—Other self-supporting filtering material ; Other filtering material of inorganic material, e.g. asbestos paper, metallic filtering material of non-woven wires
- B01D39/2027—Metallic material
- B01D39/2041—Metallic material the material being filamentary or fibrous
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D46/00—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
- B01D46/10—Particle separators, e.g. dust precipitators, using filter plates, sheets or pads having plane surfaces
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24F—AIR-CONDITIONING; AIR-HUMIDIFICATION; VENTILATION; USE OF AIR CURRENTS FOR SCREENING
- F24F8/00—Treatment, e.g. purification, of air supplied to human living or working spaces otherwise than by heating, cooling, humidifying or drying
- F24F8/10—Treatment, e.g. purification, of air supplied to human living or working spaces otherwise than by heating, cooling, humidifying or drying by separation, e.g. by filtering
- F24F8/108—Treatment, e.g. purification, of air supplied to human living or working spaces otherwise than by heating, cooling, humidifying or drying by separation, e.g. by filtering using dry filter elements
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24F—AIR-CONDITIONING; AIR-HUMIDIFICATION; VENTILATION; USE OF AIR CURRENTS FOR SCREENING
- F24F8/00—Treatment, e.g. purification, of air supplied to human living or working spaces otherwise than by heating, cooling, humidifying or drying
- F24F8/10—Treatment, e.g. purification, of air supplied to human living or working spaces otherwise than by heating, cooling, humidifying or drying by separation, e.g. by filtering
-
- 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
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10S55/00—Gas separation
- Y10S55/05—Methods of making filter
Definitions
- the present invention concerns a process for manufacturing a filtration device more particularly intended for filtering gases such as air for ventilating and/or heating and/or air conditioning rooms or motor vehicles.
- the invention also concerns a filtration device manufactured by the above process.
- Prior art filtration devices are made by spinning a thermoplastics polymer through nozzles to produce an intermingling of the filaments issuing from the nozzles forming, after cooling, a lap that can constitute a particle filter.
- the filters obtained in this way have a high specific gravity and a high unit cost.
- the process for manufacturing a filtration device of the aforementioned type in accordance with the invention is characterised in that it comprises an operation of carding fibres having a length in the range 38 mm to 120 mm and a diameter greater than 10 ⁇ m to form an isotropic web and in that said web is subjected to a mechanical consolidation operation by means of hydraulic binding consisting in passing very fine water jets at a high pressure through the web disposed on a rotating drum followed by a drying operation.
- the carding operation is carried out using a wool type card
- said card incorporates “Dispelmel” type randomising units
- the pressure of the water jets used for the hydraulic binding is in the range 40 bars to 200 bars;
- the parameters of the card are chosen to obtain a web having a mass per unit surface area in the range approximately 20 g/m 2 to approximately 150 g/m 2 .
- the filtration device of the above type is characterised in that it comprises an isotropic web.
- said web is in a single layer
- the length of said fibres is at least equal to 38 mm;
- the length of said fibres is at most equal to 120 mm;
- the average diameter of said fibres is at least equal to 10 ⁇ m
- said fibres are fibres of the same kind or a mixture of different fibres.
- said fibres are selected from the group of thermoplastics fibres such as fibres of polypropylene, polyethylene, polyester, polycarbonate, polyamide, the group of acrylic fibres, pre-oxidised acrylic fibres, the group of aramide fibres, the group of phenolic fibres, the group of fluorocarbon fibres, the group of mineral fibres such as glass fibres and the group of metal fibres.
- thermoplastics fibres such as fibres of polypropylene, polyethylene, polyester, polycarbonate, polyamide, the group of acrylic fibres, pre-oxidised acrylic fibres, the group of aramide fibres, the group of phenolic fibres, the group of fluorocarbon fibres, the group of mineral fibres such as glass fibres and the group of metal fibres.
- the invention provides a filtration device that is efficient and of lower unit cost and of lower specific gravity than the prior art filtration devices.
- 1.7 Tex (14 ⁇ m diameter) polypropylene fibres are cut to a length of 40 mm and then introduced into a mixer.
- the fibre mixture obtained is then carded by means of a two-doffer wool type card equipped with a “Dispelmel” type randomising unit to obtain an isotropic web.
- the web leaving the card is introduced into a condenser to form a single layer lap.
- the parameters of the card and/or of the condenser are selected to produce a web or a lap having a mass per unit surface area in the range approximately 20 g/m 2 to approximately 150 g/m 2 .
- the web or lap is deposited onto a belt and then consolidated by a hydraulic binding operation.
- the hydraulic binding operation consists in passing very fine water jets at a high pressure (in the range 40 bars to 200 bars) through the web or lap disposed on a rotating drum.
- the web or lap is mounted on a support to form the filtration device.
- the particles corresponded to a “fine SAE powder” defined in US Standard SAE J 726/ISO 5011.
- the particle concentration was 100 mg/m 3 .
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Life Sciences & Earth Sciences (AREA)
- Geology (AREA)
- Combustion & Propulsion (AREA)
- General Engineering & Computer Science (AREA)
- Filtering Materials (AREA)
- Nonwoven Fabrics (AREA)
Abstract
Description
- The present invention concerns a process for manufacturing a filtration device more particularly intended for filtering gases such as air for ventilating and/or heating and/or air conditioning rooms or motor vehicles.
- The invention also concerns a filtration device manufactured by the above process.
- Prior art filtration devices are made by spinning a thermoplastics polymer through nozzles to produce an intermingling of the filaments issuing from the nozzles forming, after cooling, a lap that can constitute a particle filter.
- The prior art processes have the drawback of necessitating the superposition and binding together of a plurality of layers in order to obtain filters that are sufficiently efficient.
- The filters obtained in this way have a high specific gravity and a high unit cost.
- An aim of the invention is to manufacture a filtration device that is efficient and less dense and more economic than the prior art devices.
- The process for manufacturing a filtration device of the aforementioned type in accordance with the invention is characterised in that it comprises an operation of carding fibres having a length in the range 38 mm to 120 mm and a diameter greater than 10 μm to form an isotropic web and in that said web is subjected to a mechanical consolidation operation by means of hydraulic binding consisting in passing very fine water jets at a high pressure through the web disposed on a rotating drum followed by a drying operation.
- In accordance with other features of the process in accordance with the invention, separately or in all technically possible combinations:
- the carding operation is carried out using a wool type card;
- said card incorporates “Dispelmel” type randomising units;
- the pressure of the water jets used for the hydraulic binding is in the range 40 bars to 200 bars;
- the parameters of the card are chosen to obtain a web having a mass per unit surface area in the range approximately 20 g/m2 to approximately 150 g/m2.
- In accordance with the invention the filtration device of the above type is characterised in that it comprises an isotropic web.
- In accordance with other features of the filtration device in accordance with the invention, separately or in all technically possible combinations:
- said web is in a single layer;
- the length of said fibres is at least equal to 38 mm;
- the length of said fibres is at most equal to 120 mm;
- the average diameter of said fibres is at least equal to 10 μm;
- said fibres are fibres of the same kind or a mixture of different fibres.
- said fibres are selected from the group of thermoplastics fibres such as fibres of polypropylene, polyethylene, polyester, polycarbonate, polyamide, the group of acrylic fibres, pre-oxidised acrylic fibres, the group of aramide fibres, the group of phenolic fibres, the group of fluorocarbon fibres, the group of mineral fibres such as glass fibres and the group of metal fibres.
- It has been found that the invention provides a filtration device that is efficient and of lower unit cost and of lower specific gravity than the prior art filtration devices.
- Another important advantage compared to the prior art is that the head loss when a gas passes through the filtration device is much lower.
- Other aspects and advantages of the invention will become apparent in the following description of one embodiment of a filtration device designed to be installed in equipment for heating/air conditioning a motor vehicle.
- 1.7 Tex (14 μm diameter) polypropylene fibres are cut to a length of 40 mm and then introduced into a mixer.
- The fibre mixture obtained is then carded by means of a two-doffer wool type card equipped with a “Dispelmel” type randomising unit to obtain an isotropic web.
- In one variant of the process the web leaving the card is introduced into a condenser to form a single layer lap.
- The parameters of the card and/or of the condenser are selected to produce a web or a lap having a mass per unit surface area in the range approximately 20 g/m2 to approximately 150 g/m2.
- The web or lap is deposited onto a belt and then consolidated by a hydraulic binding operation.
- The hydraulic binding operation consists in passing very fine water jets at a high pressure (in the range 40 bars to 200 bars) through the web or lap disposed on a rotating drum.
- When they bounce off the drum the water jets cause knotting of the fibres imparting a high mechanical strength to the web or lap without significantly increasing its specific gravity.
- After drying, the web or lap is mounted on a support to form the filtration device.
- Using a 0.84 mm thick web or lap the process has produced a filter having a mass per unit surface area of 66 g/m2 and a specific gravity of 0.07.
- To test the efficiency of a filter obtained in the above manner, it was disposed across a 100 cm2 20 cm/s flow of air laden with particles.
- The particles corresponded to a “fine SAE powder” defined in US Standard SAE J 726/ISO 5011.
- The particle concentration was 100 mg/m3.
- The head loss across the filter under the above conditions was only 14 Pa and the efficiency was 80%.
- Compared to filtration devices currently on the market, an efficiency comparable to the best of them was obtained with a product having a much lower specific gravity (0.07 compared to 0.12 to 0.30) generating a much lower head loss.
- Endurance tests have shown that the efficiency of the filtration device in accordance with the invention is more stable with time.
- What is more, the process described hereinabove is carried out continuously and produces the filtration device in a single operation.
Claims (12)
Applications Claiming Priority (4)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
FR9704524A FR2761901B1 (en) | 1997-04-10 | 1997-04-10 | METHOD FOR PRODUCING A FILTERING DEVICE AND FILTERING DEVICE IN PARTICULAR FOR AERATION AND / OR AIR CONDITIONING OF PREMISES OR VEHICLES |
FR9704524 | 1997-04-10 | ||
FR97/04524 | 1997-04-10 | ||
PCT/FR1998/000633 WO1998045023A1 (en) | 1997-04-10 | 1998-03-27 | Filtration device and process for its manufacture |
Publications (2)
Publication Number | Publication Date |
---|---|
US20010037540A1 true US20010037540A1 (en) | 2001-11-08 |
US6440192B2 US6440192B2 (en) | 2002-08-27 |
Family
ID=9505839
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US09/202,147 Expired - Fee Related US6440192B2 (en) | 1997-04-10 | 1998-03-27 | Filtration device and process for its manufacture |
Country Status (6)
Country | Link |
---|---|
US (1) | US6440192B2 (en) |
EP (1) | EP0925101B1 (en) |
JP (1) | JP2000512900A (en) |
DE (1) | DE19880664T1 (en) |
FR (1) | FR2761901B1 (en) |
WO (1) | WO1998045023A1 (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20050233666A1 (en) * | 2000-12-13 | 2005-10-20 | N.V. Bekaert S.A. | Short metal fibers |
US20060277731A1 (en) * | 2003-04-08 | 2006-12-14 | Jochen Schreiber | Method for stitch-bonding or finishing a material web by means of hidrodynamic needling, and product produced according to this method |
Families Citing this family (26)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR2800993B1 (en) * | 1999-11-17 | 2003-08-15 | Valeo | METHOD FOR PRODUCING A FILTRATION DEVICE AND FILTRATION DEVICE FOR GAS FILTRATION SUCH AS AIR FOR AERATION AND / OR HEATING AND / OR AIR CONDITIONING OF PREMISES OR MOTOR VEHICLES. |
FR2806320B1 (en) * | 2000-03-15 | 2003-02-07 | Valeo | FILTRATION DEVICE FOR FITTING A VENTILATION AND / OR HEATING AND / OR AIR CONDITIONING APPARATUS, PARTICULARLY FOR A MOTOR VEHICLE |
FR2806319B1 (en) * | 2000-03-15 | 2002-10-25 | Valeo | FILTRATION DEVICE FOR FITTING A VENTILATION AND / OR HEATING AND / OR AIR CONDITIONING APPARATUS, PARTICULARLY FOR A MOTOR VEHICLE |
FR2806318B1 (en) * | 2000-03-15 | 2002-10-25 | Valeo | FILTRATION DEVICE FOR FITTING A VENTILATION AND / OR HEATING AND / OR AIR CONDITIONING APPARATUS, IN PARTICULAR FOR A MOTOR VEHICLE |
DE10053233A1 (en) * | 2000-10-26 | 2002-05-16 | Tesa Ag | Use of a roughened textile fabric as pollen protection for windows and doors |
US7582270B2 (en) | 2002-10-28 | 2009-09-01 | Geo2 Technologies, Inc. | Multi-functional substantially fibrous mullite filtration substrates and devices |
US7572311B2 (en) | 2002-10-28 | 2009-08-11 | Geo2 Technologies, Inc. | Highly porous mullite particulate filter substrate |
US6946013B2 (en) * | 2002-10-28 | 2005-09-20 | Geo2 Technologies, Inc. | Ceramic exhaust filter |
US7574796B2 (en) | 2002-10-28 | 2009-08-18 | Geo2 Technologies, Inc. | Nonwoven composites and related products and methods |
FR2875714B1 (en) * | 2004-09-29 | 2006-11-24 | Valeo Materiaux De Friction Sa | FILTERING MEDIA FOR GAS FILTRATION, FILTRATION DEVICE AND METHOD FOR MANUFACTURING THE FILTER MEDIA |
US12172111B2 (en) | 2004-11-05 | 2024-12-24 | Donaldson Company, Inc. | Filter medium and breather filter structure |
US8057567B2 (en) | 2004-11-05 | 2011-11-15 | Donaldson Company, Inc. | Filter medium and breather filter structure |
US8021457B2 (en) | 2004-11-05 | 2011-09-20 | Donaldson Company, Inc. | Filter media and structure |
ES2541469T3 (en) | 2004-11-05 | 2015-07-20 | Donaldson Company, Inc. | Spray separator |
BRPI0606842A2 (en) | 2005-02-04 | 2009-07-21 | Donaldson Co Inc | aerosol separator |
CN101163534A (en) | 2005-02-22 | 2008-04-16 | 唐纳森公司 | Aerosol separator |
US7211232B1 (en) | 2005-11-07 | 2007-05-01 | Geo2 Technologies, Inc. | Refractory exhaust filtering method and apparatus |
US7682577B2 (en) | 2005-11-07 | 2010-03-23 | Geo2 Technologies, Inc. | Catalytic exhaust device for simplified installation or replacement |
US7682578B2 (en) | 2005-11-07 | 2010-03-23 | Geo2 Technologies, Inc. | Device for catalytically reducing exhaust |
US7722828B2 (en) | 2005-12-30 | 2010-05-25 | Geo2 Technologies, Inc. | Catalytic fibrous exhaust system and method for catalyzing an exhaust gas |
US7444805B2 (en) | 2005-12-30 | 2008-11-04 | Geo2 Technologies, Inc. | Substantially fibrous refractory device for cleaning a fluid |
US7563415B2 (en) | 2006-03-03 | 2009-07-21 | Geo2 Technologies, Inc | Catalytic exhaust filter device |
CN101652168A (en) | 2007-02-22 | 2010-02-17 | 唐纳森公司 | Filter element and method thereof |
EP2125149A2 (en) | 2007-02-23 | 2009-12-02 | Donaldson Company, Inc. | Formed filter element |
US9885154B2 (en) | 2009-01-28 | 2018-02-06 | Donaldson Company, Inc. | Fibrous media |
JP2022098027A (en) | 2020-12-21 | 2022-07-01 | キヤノン電子管デバイス株式会社 | X-ray tube |
Family Cites Families (20)
Publication number | Priority date | Publication date | Assignee | Title |
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US2862251A (en) * | 1955-04-12 | 1958-12-02 | Chicopee Mfg Corp | Method of and apparatus for producing nonwoven product |
CH509450A (en) * | 1965-07-29 | 1971-06-30 | Snia Viscosa | Non-woven fabric prodn |
US3563241A (en) * | 1968-11-14 | 1971-02-16 | Du Pont | Water-dispersible nonwoven fabric |
USRE28680E (en) * | 1971-01-05 | 1976-01-13 | Johnson & Johnson | Apertured nonwoven fabrics and methods of making the same |
US4375718A (en) * | 1981-03-12 | 1983-03-08 | Surgikos, Inc. | Method of making fibrous electrets |
US4361619A (en) * | 1981-05-20 | 1982-11-30 | E. I. Du Pont De Nemours And Company | Filter of poly(tetrafluoroethylene) and glass fibers |
US4548628A (en) * | 1982-04-26 | 1985-10-22 | Asahi Kasei Kogyo Kabushiki Kaisha | Filter medium and process for preparing same |
DE3346335A1 (en) * | 1983-12-22 | 1985-07-18 | Hergeth Hollingsworth GmbH, 4408 Dülmen | METHOD AND DEVICE FOR PRODUCING A UNIFORM FIBER MATING IN THE FABRICATION ZONE BETWEEN TAMBOUR AND FIBER TAKEOVER ORGAN |
DE3346327A1 (en) * | 1983-12-22 | 1985-07-18 | Hergeth Hollingsworth GmbH, 4408 Dülmen | METHOD AND DEVICE FOR THE PRODUCTION OF A FLUSHED FIBER MESH FROM MESH |
US4612237A (en) * | 1985-12-13 | 1986-09-16 | E. I. Du Pont De Nemours And Company | Hydraulically entangled PTFE/glass filter felt |
US4874399A (en) * | 1988-01-25 | 1989-10-17 | Minnesota Mining And Manufacturing Company | Electret filter made of fibers containing polypropylene and poly(4-methyl-1-pentene) |
JP2975396B2 (en) * | 1990-05-22 | 1999-11-10 | ダイニック株式会社 | Air filter material |
FR2667622B1 (en) * | 1990-10-08 | 1994-10-07 | Kaysersberg Sa | HYDRAULICALLY LINKED MONTISSE AND MANUFACTURING METHOD THEREOF. |
CA2145650A1 (en) * | 1992-11-23 | 1994-06-09 | Ray Wnenchak | Triboelectric filtration material |
EP0678128B1 (en) * | 1993-01-07 | 1996-09-25 | Minnesota Mining And Manufacturing Company | Flexible nonwoven mat |
FR2717820B1 (en) * | 1994-03-25 | 1996-05-15 | Valeo | Friction material intended to equip a device implementing friction in a liquid medium, as well as the process for producing such a friction material and the device which is equipped with it. |
FR2717802B1 (en) | 1994-03-25 | 1996-06-21 | Sanofi Sa | New aromatic compounds, process for their preparation and pharmaceutical compositions containing them. |
US5422159A (en) * | 1994-12-08 | 1995-06-06 | Ausimont U.S.A., Inc. | Fluorpolymer sheets formed from hydroentangled fibers |
US5770532A (en) * | 1996-01-11 | 1998-06-23 | Hitachi, Ltd. | Method for manufacturing a solidified fiber fleece, the resulting solidified fiber fleece, and use of this fleece |
US5970583A (en) * | 1997-06-17 | 1999-10-26 | Firma Carl Freudenberg | Nonwoven lap formed of very fine continuous filaments |
-
1997
- 1997-04-10 FR FR9704524A patent/FR2761901B1/en not_active Expired - Fee Related
-
1998
- 1998-03-27 DE DE19880664T patent/DE19880664T1/en not_active Withdrawn
- 1998-03-27 WO PCT/FR1998/000633 patent/WO1998045023A1/en active IP Right Grant
- 1998-03-27 US US09/202,147 patent/US6440192B2/en not_active Expired - Fee Related
- 1998-03-27 JP JP10542439A patent/JP2000512900A/en not_active Ceased
- 1998-03-27 EP EP98917261A patent/EP0925101B1/en not_active Expired - Lifetime
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20050233666A1 (en) * | 2000-12-13 | 2005-10-20 | N.V. Bekaert S.A. | Short metal fibers |
US20060277731A1 (en) * | 2003-04-08 | 2006-12-14 | Jochen Schreiber | Method for stitch-bonding or finishing a material web by means of hidrodynamic needling, and product produced according to this method |
Also Published As
Publication number | Publication date |
---|---|
JP2000512900A (en) | 2000-10-03 |
DE19880664T1 (en) | 1999-05-12 |
FR2761901A1 (en) | 1998-10-16 |
EP0925101B1 (en) | 2004-04-21 |
EP0925101A1 (en) | 1999-06-30 |
US6440192B2 (en) | 2002-08-27 |
WO1998045023A1 (en) | 1998-10-15 |
FR2761901B1 (en) | 1999-05-14 |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
AS | Assignment |
Owner name: VALEO, FRANCE Free format text: ASSIGNMENT OF ASSIGNORS INTEREST;ASSIGNORS:GUERIN, RICHARD;LEGRAND, CLAUDE;REEL/FRAME:010064/0838 Effective date: 19981109 |
|
AS | Assignment |
Owner name: VALCO, FRANCE Free format text: CORRECTIVE ASSIGNMENT TO CORRECT THE ADDRESS OF THE ASSIGNEE. FILED ON 12/09/1998, RECORDED ON REEL 010064 FRAME 0838;ASSIGNORS:GUERIN, RICHARD;LEGRAND, CLAUDE;REEL/FRAME:012859/0891 Effective date: 19981109 |
|
FPAY | Fee payment |
Year of fee payment: 4 |
|
REMI | Maintenance fee reminder mailed | ||
LAPS | Lapse for failure to pay maintenance fees | ||
STCH | Information on status: patent discontinuation |
Free format text: PATENT EXPIRED DUE TO NONPAYMENT OF MAINTENANCE FEES UNDER 37 CFR 1.362 |
|
FP | Lapsed due to failure to pay maintenance fee |
Effective date: 20100827 |