EP0987089B1 - Verfahren zur Herstellung von Gegenständen aus rohem, pflanzlichem Material durch Pressen - Google Patents

Verfahren zur Herstellung von Gegenständen aus rohem, pflanzlichem Material durch Pressen Download PDF

Info

Publication number
EP0987089B1
EP0987089B1 EP99390017A EP99390017A EP0987089B1 EP 0987089 B1 EP0987089 B1 EP 0987089B1 EP 99390017 A EP99390017 A EP 99390017A EP 99390017 A EP99390017 A EP 99390017A EP 0987089 B1 EP0987089 B1 EP 0987089B1
Authority
EP
European Patent Office
Prior art keywords
cake
sunflower
oil
production
rapeseed
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.)
Expired - Lifetime
Application number
EP99390017A
Other languages
English (en)
French (fr)
Other versions
EP0987089A1 (de
Inventor
Juliette Apt. 101 Le Vieux Colombier Leyris
Françoise SILVESTRE
Luc Rigal
Antoine Gaset
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.)
TOULOUSAINE DE RECHERCHE ET DE DEVELOPPEMENT EN AB
Original Assignee
Toulousaine De Recherche Et De Developpement "trd" SA
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 Toulousaine De Recherche Et De Developpement "trd" SA filed Critical Toulousaine De Recherche Et De Developpement "trd" SA
Publication of EP0987089A1 publication Critical patent/EP0987089A1/de
Application granted granted Critical
Publication of EP0987089B1 publication Critical patent/EP0987089B1/de
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Images

Classifications

    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B27—WORKING OR PRESERVING WOOD OR SIMILAR MATERIAL; NAILING OR STAPLING MACHINES IN GENERAL
    • B27N—MANUFACTURE BY DRY PROCESSES OF ARTICLES, WITH OR WITHOUT ORGANIC BINDING AGENTS, MADE FROM PARTICLES OR FIBRES CONSISTING OF WOOD OR OTHER LIGNOCELLULOSIC OR LIKE ORGANIC MATERIAL
    • B27N3/00—Manufacture of substantially flat articles, e.g. boards, from particles or fibres
    • B27N3/08—Moulding or pressing
    • B27N3/28—Moulding or pressing characterised by using extrusion presses

Definitions

  • the invention relates to a method of manufacturing objects from vegetable raw material. It aims to make objects such as containers, packaging, panels or plates, in particular for the construction or furnishings, which, while benefiting from durability and stability compatible with their function, are biodegradable, compostable and recyclable.
  • biodegradable is meant that said object is likely to be degraded at least for the most part by microorganisms natural when put in the right conditions, without release of toxic products for the ecosystem, and at the scale of a few weeks to months.
  • compostable is meant an object which, divided, homogenized and mixed with organic matter and / or soil, provides a nutritious non-toxic substrate for plants.
  • recyclable is meant an object whose material can be reused to form an object of the same range.
  • the present invention proposes to overcome the disadvantages of known methods and to indicate a new method allowing to make a biodegradable, compostable and recyclable object in remarkable saving conditions.
  • Another object of the invention is to manufacture an object which has good flexural strength compatible with uses in construction, furniture, packaging, packaging ...
  • the manufacturing process according to the invention consists in (a) using a sunflower or rapeseed meal having a content weight by oil of less than 20% and a protein content by weight greater than 15%, hydrated so as to present a weight rate of hydration substantially between 5% and 55%, (b) press forming said cake in a shape adapted to that of the desired object and (c) to produce a heat treatment or drying treatment to ensure stiffening of the shaped object.
  • “Sunflower or rapeseed meal” means usual way the solid residue from oil extraction from sunflower seeds or whole or shelled rapeseed, whatever the means of extraction (pressing, solvent extraction ...), this oil extraction can be total or partial but lowering the oil content by weight of the product below a threshold generally around 20%; the meal may or may not have been the subject of a preliminary partial extraction of protein, its protein content by weight however, remaining above 15%. (All weight contents are expressed as a percentage relative to the weight of dry matter; the rate of hydration is expressed in relation to the total matter).
  • the method of the invention can be implemented by operating thermoforming of the cake, consisting of bringing it, during pressing, to a temperature substantially between 130 ° C and 200 ° C.
  • thermoforming is carried out at a pressure substantially between 15 and 25 megapascals. A such thermoforming process is faster than forming cold (discussed later) and leads to better mechanical resistance.
  • oil cake sunflower or rapeseed is preferably subjected to a treatment mechanics of division and homogenization to give it a distribution particle size such that the median diameter of the particles D50 is substantially between 0.1 mm and 1 mm.
  • median diameter D50 we means a diameter such that 50% of the particles by weight pass through a sieve vibrating with a mesh side equal to said diameter. (All measures particle size are carried out on the dry matter).
  • thermoforming sunflower meal or rapeseed meal panels usable in the construction, mainly consisting of plant fibers linked by proteins, having a flexural strength substantially between 10 and 25 megapascals.
  • the meal previously subjected to a mechanical division treatment and homogenization to give it a particle size distribution such as median particle diameter D50 is less than 1mm, is hydrated, by a addition of water, at a hydration rate substantially between 25% and 50% in order to obtain a plastic paste which is then cold formed by pressing before being dried until hardening.
  • the forming pressure can advantageously be adjusted between 1 and 5 megapascals.
  • the residual oil from the oil cake has an unfavorable effect on the forming and qualities of objects obtained, and an oil cake is advantageously used at least partially deoiled, with an oil content by weight of less than 10%.
  • an oil-depleted oil cake from the crushing of sunflower or rapeseed. (We generally mean by "exhausted cake in oil "a cake containing at most 2% oil). We limit or delete thus the hydrophobic repulsive forces which tend to oppose fiber / protein association.
  • the meal can in particular be divided and homogenized, and possibly at least partially de-oiled, by passing through a twin-screw device comprising, from upstream to downstream, shearing means, means crushing, means for withdrawing the liquid phase, at least one module not inverted to achieve axial compression of the solid materials, and a solids outlet, said twin-screw device being furthermore equipped with means water injection to adjust the hydration rate of the meal.
  • a twin-screw device comprising, from upstream to downstream, shearing means, means crushing, means for withdrawing the liquid phase, at least one module not inverted to achieve axial compression of the solid materials, and a solids outlet, said twin-screw device being furthermore equipped with means water injection to adjust the hydration rate of the meal.
  • Such treatment refines the texture of the meal and allows the association of fibers and proteins to be generated under optimal conditions during forming.
  • Sunflower or rapeseed meal may if necessary be enriched with vegetable fibers in order to further lower the cost price of objects obtained.
  • This method of implementation which makes it possible to value stocks existing low-value vegetable fibers (straw, sunflower shell) will be especially used when using a meal containing all its proteins original (without partial extraction) or when the object sought is not submitted to severe mechanical strength requirements.
  • the method of the invention makes it possible to manufacture objects of very diverse type: flat objects such as panels, plates, supports, spacers ..., hollow objects such as containers, packaging ...
  • the twin-screw device shown diagrammatically in Figures 1 and 2 is used to carry out the prior preparation of the cakes in Example 1; these measures is obtained from modules sold by the company "CLEXTRAL" (registered trademark) under the general reference "BC45".
  • Each module includes a double-walled tubular enclosure 1 and 2 which allows thermal regulation from the heart of the enclosure where the active organs are housed.
  • Some modules are type comprising two identical co-penetrating screws, others of the type comprising shear mixers composed of two-lobed discs.
  • the various modules are rotated in synchronism by an electric motor 3 allowing obtain a speed of rotation of its output shaft which can reach 700tr / min. In the examples, the speed of rotation chosen is 100 rpm.
  • the conventional type mold shown diagrammatically in FIG. 3 is intended to carry out a cold forming as described in Example 1.
  • This mold comprises, on the one hand, a hollow form 17, in the frustoconical example, fixed on a press plate 18 and having a removable bottom 19 to facilitate the demoulding, on the other hand, a conjugate counterform 20 fixed on the other plate 21 of the press. Correct positioning of the form and counter-form is ensured by a centering pin 22. Molding and demolding are carried out cold.
  • the conventional type mold shown diagrammatically in FIG. 4 is intended to carry out a thermoforming as described in Example 2, in order to obtain a hollow object of the same shape as in Example 1.
  • This mold is similar to that of Figure 3, except that the inner wall of the hollow form is equipped with a grid 23 for evacuating steam and the bottom of a frit 24 connected to a duct 25 steam outlet. These forms and counter-forms are arranged in a heating press (not shown).
  • a weak play about 1 mm is preserved above the hollow form to allow steam evacuation.
  • the conventional type mold shown diagrammatically in FIG. 5 is intended to carry out thermoforming of a panel as described in Example 3.
  • This mold comprises, first of all, a form 26 combined with that of the panels desired, the bottom of which consists of a removable base 27 fitted with a sinter 28 connected to a water vapor discharge duct 29.
  • the mold comprises also a counter-form 30 for closing off the form 26, this counter-form being equipped with a frit 31 connected to a steam evacuation duct 32.
  • sunflower meal spent in oil from the crushing of sunflower seeds, is used; the oil extraction was carried out by pressing and an extraction with hexane.
  • the composition of the meal is as follows: % Hydration rate % Minerals % Proteins % Fat % Cellulose % Lignin % Hemicellulose % Phenolic compounds 10.0 7.0 35.6 1.0 22.3 5.2 18.5 5.7
  • the median diameter D50 of the particles of the raw material is equal to 0.65 mm (dry measurement).
  • the screw rotation speed is equal to 100 revolutions per minute and the device temperature is regulated and maintained at 30 ° C.
  • the flow of cake injected at the head is close to 32 kg / h. About 32 l / h of water are inj ected.
  • the hydrated matter produced has a final weight rate hydration of 47% and a median diameter D50 of 0.4 mm (dry measurement). She is in the form of a homogeneous plastic paste and easily moldable.
  • the part was dried in an oven ventilated at 60 ° C overnight.
  • the part hardens and a shrinkage of approximately 1% can be seen.
  • the hollow part obtained can be filled with soil or gravel without deformation.
  • the cake is first homogenized by grinding (grinder hammer fitted with a 0.5 mm grid).
  • the D50 is reduced to 0.35 mm.
  • the cake is then mixed with water in proportions allowing a weight hydration rate equal to 38% to be obtained.
  • the mixing is carried out in a "Perrier" kneader for 10 min, at temperature room.
  • the mold is maintained at 160 ° C for about 1 min after the release of water vapor.
  • the part is then removed from the mold. She is dry and rigid. No measurable shrinkage is observed. The room does not require further conditioning. Crushed and buried, the part degrades then disappears in a few weeks.
  • the raw material is homogenized by grinding (hammer mill fitted with a 0.5mm grid).
  • the D50 is reduced to 0.35mm.
  • the initial hydration rate of the meal is retained (10%).
  • 30g of material are placed in the mold of Figure 5.
  • the sintered were previously coated with a release agent.
  • the temperature of the press lower plate is fixed at 150 ° C, that of the upper plate at 180 ° C.
  • a pressure of 20.4 megapascals is applied and maintained for one minute after rebalancing the temperature of the press platens.
  • the part can then be removed from the mold. It is dry, flat and rigid. Once cooled, it does not require any special conditioning. Its mechanical characteristics are presented in the table below. They were measured on an XTRAD texturometer according to standard NF EN 310. E (mm) Rf (Mpa) Em (Mpa) Density (g / cm 3 ) 3.67 18.2 2545 1.00 E: thickness of test piece Rf: resistance to breaking in bending Em: modulus of elasticity

Landscapes

  • Life Sciences & Earth Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Manufacturing & Machinery (AREA)
  • Wood Science & Technology (AREA)
  • Forests & Forestry (AREA)
  • Fodder In General (AREA)
  • Dry Formation Of Fiberboard And The Like (AREA)
  • Fats And Perfumes (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Fertilizers (AREA)
  • Casting Or Compression Moulding Of Plastics Or The Like (AREA)
  • Processing Of Solid Wastes (AREA)
  • Preparation Of Fruits And Vegetables (AREA)

Claims (12)

  1. Verfahren zur Herstellung eines biologisch abbaubaren, kompostierbaren und recycelbaren Gegenstands, dadurch gekennzeichnet, dass es die folgenden Schritte umfasst:
    (a) Verwenden eines Sonnenblumen- oder Rapskuchens mit einem Ölgehalt von weniger als 20 Gew.-% und einem Proteingehalt von mehr als 15 Gew.-% bezogen auf das Gewicht der Trockenmasse, so hydriert, dass ein Wasseranteil zwischen 5 und 55 Gew.-% bezogen auf die Gesamtmasse entsteht, (b) Durchführen eines Formvorgangs durch Pressen des genannten Kuchens in einer Form, die der des gewünschten Gegenstands entspricht, und (c) Durchführen einer Wärmebehandlung oder einer Trocknungsbehandlung, um den Gegenstand in seiner Form zum Erstarren zu bringen.
  2. Verfahren nach Anspruch 1, bei dem ein Kuchen mit einem Wasseranteil zwischen 10% und 25% bezogen auf die Gesamtmasse verwendet wird, und wobei eine Thermoformung des genannten Kuchens durchgeführt wird, indem dieser beim Pressen auf eine Temperatur zwischen 130°C und 200°C gebracht wird.
  3. Verfahren nach Anspruch 2, bei dem die Thermoformung bei einem Druck im Wesentlichen zwichen 15 und 25 Megapascal durchgeführt wird.
  4. Verfahren nach Anspruch 1, 2 oder 3, bei dem der Sonnenblumen- oder Rapskuchen zuvor einer mechanischen Zerteilungs- und Homogenisierungsbehandlung unterzogen wird, um ihm eine solche Korngrößenverteilung zu verleihen, dass der mit D50-Partikeln äquivalente mittlere Durchmesser zwischen 0,1 mm und 1 mm liegt.
  5. Verfahren nach einem der Ansprüche 1 bis 4, bei dem ein wenigstens teilweise entölter Sonnenblumen- oder Rapskuchen mit einem Ölgehalt von weniger als 10 Gew.-% verwendet wird.
  6. Verfahren nach Anspruch 5, bei dem ein ölfreier Sonnenblumenkuchen im Anschluss an eine Zerkleinerung der Sonnenblumen- oder Rapskörner verwendet wird.
  7. Verfahren nach Anspruch 5, bei dem ein zerteilter und homogenisierter Kuchen verwendet wird, der eventuell durch Passage durch eine Doppelschneckenvorrichtung entölt wird, die, stromabwärts gesehen, Schermittel (8), Quetschmittel (9), gegebenenfalls Mittel zum Entnehmen der Flüssigphase (11, 12), wenigstens ein Modul mit Umkehrgang (10) zum Erzielen einer axialen Kompression der festen Bestandteile, und einen Ausgang (14) für die genannten festen Bestandteile umfasst, wobei die genannte Doppelschneckenvorrichtung mit Wasserinjektionsmitteln (6, 7) ausgestattet ist, um den Wasseranteil des erhaltenen Kuchens einzustellen.
  8. Verfahren nach einem der Ansprüche 1 bis 7, bei dem ein an pflanzlichen Fasern reicher Sonnenblumen- oder Rapskuchen verwendet wird.
  9. Verfahren nach Anspruch 1, zur Kaltherstellung eines Gegenstandes, bei dem ein Sonnenblumen- oder Rapskuchen einer mechanischen Zerteilungs- und Homogenisierungsbehandlung unterzogen wird, um ihm eine solche Korngrößenverteilung zu verleihen, dass der mit D50-Partikeln äquivalente mittlere Durchmesser kleiner als 1 mm ist, der genannte Kuchen auf einen Wasseranteil zwischen 25 und 50% hydriert wird, so dass eine plastische Paste entsteht, Durchführen einer Kaltformung der genannten Paste und Erzielen einer Trocknung derselben bis zur Verfestigung.
  10. Verfahren nach Anspruch 9, bei dem die Formung auf einem Druck zwischen 1 und 5 Megapascal durchgeführt wird.
  11. Verfahren nach einem der Ansprüche 1 bis 10 zur Herstellung von flachen Gegenständen wie Schildern oder Platten.
  12. Verfahren nach einem der Ansprüche 1 bis 10 zur Herstellung von hohlen Gegenständen wie Behältern oder Verpackungen.
EP99390017A 1998-09-16 1999-09-14 Verfahren zur Herstellung von Gegenständen aus rohem, pflanzlichem Material durch Pressen Expired - Lifetime EP0987089B1 (de)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
FR9811552A FR2784047B1 (fr) 1998-09-16 1998-09-16 Procede de fabrication d'objets a partir de matiere premiere vegetale par formage ou thermoformage
FR9811552 1998-09-16

Publications (2)

Publication Number Publication Date
EP0987089A1 EP0987089A1 (de) 2000-03-22
EP0987089B1 true EP0987089B1 (de) 2004-01-02

Family

ID=9530492

Family Applications (1)

Application Number Title Priority Date Filing Date
EP99390017A Expired - Lifetime EP0987089B1 (de) 1998-09-16 1999-09-14 Verfahren zur Herstellung von Gegenständen aus rohem, pflanzlichem Material durch Pressen

Country Status (5)

Country Link
EP (1) EP0987089B1 (de)
AT (1) ATE257064T1 (de)
DE (1) DE69913901T2 (de)
ES (1) ES2214821T3 (de)
FR (1) FR2784047B1 (de)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN112109177A (zh) * 2020-09-23 2020-12-22 深圳康瑞博智能科技有限公司 一种刨花板制造加工系统

Families Citing this family (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB0101630D0 (en) * 2001-01-23 2001-03-07 Amylum Europ Nv Method for preparing composite materials containing natural binders
FR2849798A1 (fr) * 2003-01-13 2004-07-16 Bsm Dev Element structurel rigide d'assemblage ou de revetement, et procede de fabrication d'un tel element
FR2849799B1 (fr) * 2003-01-13 2005-06-24 Bsm Dev Element structurel rigide d'assemblage ou de revetement, et procede de fabrication d'un tel element
GB2441748A (en) * 2006-09-13 2008-03-19 Freeland Horticulture Ltd Apparatus and process for the treatment of plant waste to produce growing media
FR2967690B1 (fr) 2010-11-23 2013-10-11 Toulouse Inst Nat Polytech Procede de fabrication d'un materiau solide eco-compatible et materiau solide eco-compatible obtenu
ES2387975B1 (es) * 2011-03-07 2013-10-30 Consejo Superior De Investigaciones Cientificas Procedimiento de obtención de materiales multifuncionales y renovables a partir del rechazo de pipa procedente de la producción de aceite de girasol.
FR3124527B1 (fr) * 2021-06-24 2023-07-14 Luma/Arles Panneaux à base de moelle de tournesol

Family Cites Families (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5593625A (en) * 1992-08-11 1997-01-14 Phenix Biocomposites, Inc. Biocomposite material and method of making
BE1008821A7 (fr) * 1994-11-03 1996-08-06 Heusquin Guy Materiau biodegradable pour la fabrication d'articles divers.
US5663221A (en) * 1996-02-26 1997-09-02 Nidera Sociedad Anonima Method for the production of MDF boards based on sunflower seed husks
FR2747128B1 (fr) * 1996-04-05 1998-06-05 Toulousaine De Rech Et De Dev Procede et dispositif pour la fabrication d'esters d'acides gras a partir de graines oleagineuses
JPH09327684A (ja) * 1996-04-08 1997-12-22 Osaka City 食材加工廃棄物を主原料とする生物分解性成形体の製造方法

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN112109177A (zh) * 2020-09-23 2020-12-22 深圳康瑞博智能科技有限公司 一种刨花板制造加工系统
CN112109177B (zh) * 2020-09-23 2021-05-25 惠州大亚湾万圣振宇实业有限公司 一种刨花板制造加工系统

Also Published As

Publication number Publication date
FR2784047A1 (fr) 2000-04-07
EP0987089A1 (de) 2000-03-22
FR2784047B1 (fr) 2001-01-05
DE69913901D1 (de) 2004-02-05
DE69913901T2 (de) 2004-11-11
ES2214821T3 (es) 2004-09-16
ATE257064T1 (de) 2004-01-15

Similar Documents

Publication Publication Date Title
CN1964827B (zh) 形成高强度模制产品的方法
JP4081579B2 (ja) リグノセルロース系材料及びその利用
RU2526277C2 (ru) Способ получения полимерного материала, наполненного длинными волокнами
CN102470545B (zh) 木质纤维素和相关材料的处理
CN1756592A (zh) 混合粉碎装置、混合熔融方法及浸含粘合剂的纤维素类材料的成形方法
EP0987089B1 (de) Verfahren zur Herstellung von Gegenständen aus rohem, pflanzlichem Material durch Pressen
JP2018083876A (ja) 木質系複合樹脂材料の製造方法と木質系複合樹脂材料
EP1112319B1 (de) Biologisch abbaubarer werkstoff auf basis eines polymers und getreidemehl, verfahren zur herstellung und verwendungen
CN1213837C (zh) 由含天然聚合物和水的基料生产发泡模压体的方法
EP0180531B1 (de) Verfahren zur Gewinnung eines auf brennbaren Stoffen basierenden verformbaren oder extrudierbaren Materials durch Recycling von Haushaltsabfällen und das dadurch hergestellte Material
TW201809148A (zh) 麥粕纖維結合聚乳酸的組成物及其製造方法
JP3781727B2 (ja) 歯車の製造方法及び歯車
EP0988948B1 (de) Verfahren zur Herstellung von Gegenständen aus rohem, pflanzlichem Material durch Spritzgiessen
Evon et al. The thermo-mechano-chemical twin-screw reactor, a new perspective for the biorefinery of sunflower whole plant
FR2940297A1 (fr) Materiau plastique composite sous la forme de granulats issus de matieres proteiques vegetales et son procede de fabrication
FR2783740A1 (fr) Materiau a base de matiere vegetale issue de plantes cerealieres et procede d'obtention
FR2777901A1 (fr) Combustible a base de matieres residuaires organiques et procedes de preparation et d'utilisation de celui-ci
FR2618641A1 (fr) Granules cellulosiques pour litieres pour animaux domestiques
CH228877A (fr) Procédé de fabrication d'agglomérés combustibles formés, au moins pour leur plus grande partie, à partir de matières ligneuses, et produit obtenu d'après ce procédé.
CN1121181C (zh) 一次性植物纤维餐具及其生产方法
EP2643132A1 (de) Verfahren zur herstellung eines ökokmpatiblen feststoffes und auf diese weise gewonnener ökokompatibler feststoff
FR2809985A1 (fr) Materiau composite thermoplastique comportant une charge de particules de matiere vegetale, et procede et installation de fabrication de ce materiau
JP6474539B1 (ja) ペレット状バイオマス燃料、及びペレット状バイオマス燃料の製造方法
TW201811989A (zh) 生質燃料之製造方法
US773992A (en) Process of manufacturing peat fuel.

Legal Events

Date Code Title Description
PUAI Public reference made under article 153(3) epc to a published international application that has entered the european phase

Free format text: ORIGINAL CODE: 0009012

AK Designated contracting states

Kind code of ref document: A1

Designated state(s): AT BE CH CY DE DK ES FI FR GB GR IE IT LI LU MC NL PT SE

AX Request for extension of the european patent

Free format text: AL;LT;LV;MK;RO;SI

17P Request for examination filed

Effective date: 20000805

AKX Designation fees paid

Free format text: AT BE CH CY DE DK ES FI FR GB GR IE IT LI LU MC NL PT SE

17Q First examination report despatched

Effective date: 20030310

GRAP Despatch of communication of intention to grant a patent

Free format text: ORIGINAL CODE: EPIDOSNIGR1

GRAS Grant fee paid

Free format text: ORIGINAL CODE: EPIDOSNIGR3

GRAA (expected) grant

Free format text: ORIGINAL CODE: 0009210

AK Designated contracting states

Kind code of ref document: B1

Designated state(s): AT BE CH CY DE DK ES FI FR GB GR IE IT LI LU MC NL PT SE

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: NL

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20040102

Ref country code: FI

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20040102

Ref country code: CY

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20040102

Ref country code: AT

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20040102

REG Reference to a national code

Ref country code: GB

Ref legal event code: FG4D

Free format text: NOT ENGLISH

REG Reference to a national code

Ref country code: CH

Ref legal event code: EP

REG Reference to a national code

Ref country code: IE

Ref legal event code: FG4D

Free format text: FRENCH

REF Corresponds to:

Ref document number: 69913901

Country of ref document: DE

Date of ref document: 20040205

Kind code of ref document: P

RAP2 Party data changed (patent owner data changed or rights of a patent transferred)

Owner name: TOULOUSAINE DE RECHERCHE ET DE DEVELOPPEMENT EN AB

REG Reference to a national code

Ref country code: CH

Ref legal event code: NV

Representative=s name: BOVARD AG PATENTANWAELTE

NLT2 Nl: modifications (of names), taken from the european patent patent bulletin

Owner name: TOULOUSAINE DE RECHERCHE ET DE DEVELOPPEMENT EN AB

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: SE

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20040402

Ref country code: GR

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20040402

Ref country code: DK

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20040402

NLV1 Nl: lapsed or annulled due to failure to fulfill the requirements of art. 29p and 29m of the patents act
GBT Gb: translation of ep patent filed (gb section 77(6)(a)/1977)

Effective date: 20040602

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: LU

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20040914

REG Reference to a national code

Ref country code: ES

Ref legal event code: FG2A

Ref document number: 2214821

Country of ref document: ES

Kind code of ref document: T3

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: MC

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20040930

PLBE No opposition filed within time limit

Free format text: ORIGINAL CODE: 0009261

STAA Information on the status of an ep patent application or granted ep patent

Free format text: STATUS: NO OPPOSITION FILED WITHIN TIME LIMIT

26N No opposition filed

Effective date: 20041005

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: PT

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20040602

REG Reference to a national code

Ref country code: CH

Ref legal event code: PFA

Owner name: TOULOUSAINE DE RECHERCHE ET DE DEVELOPPEMENT EN A

Free format text: TOULOUSAINE DE RECHERCHE ET DE DEVELOPPEMENT EN ABREGE "T.R.D."#ZONE INDUSTRIELLE DE POMPIGNAL MIREMONT#31190 AUTERIVE (FR) -TRANSFER TO- TOULOUSAINE DE RECHERCHE ET DE DEVELOPPEMENT EN ABREGE "T.R.D."#ZONE INDUSTRIELLE DE POMPIGNAL MIREMONT#31190 AUTERIVE (FR)

REG Reference to a national code

Ref country code: FR

Ref legal event code: CD

Owner name: ARTERRIS INNOVATION, FR

Effective date: 20110927

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: DE

Payment date: 20130923

Year of fee payment: 15

Ref country code: CH

Payment date: 20130909

Year of fee payment: 15

Ref country code: IE

Payment date: 20130830

Year of fee payment: 15

Ref country code: ES

Payment date: 20130905

Year of fee payment: 15

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: GB

Payment date: 20130911

Year of fee payment: 15

Ref country code: FR

Payment date: 20130923

Year of fee payment: 15

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: IT

Payment date: 20130829

Year of fee payment: 15

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: BE

Payment date: 20130830

Year of fee payment: 15

REG Reference to a national code

Ref country code: DE

Ref legal event code: R119

Ref document number: 69913901

Country of ref document: DE

REG Reference to a national code

Ref country code: CH

Ref legal event code: PL

GBPC Gb: european patent ceased through non-payment of renewal fee

Effective date: 20140914

REG Reference to a national code

Ref country code: IE

Ref legal event code: MM4A

REG Reference to a national code

Ref country code: DE

Ref legal event code: R119

Ref document number: 69913901

Country of ref document: DE

Effective date: 20150401

REG Reference to a national code

Ref country code: FR

Ref legal event code: ST

Effective date: 20150529

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: BE

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20140930

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: DE

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20150401

Ref country code: LI

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20140930

Ref country code: GB

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20140914

Ref country code: CH

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20140930

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: FR

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20140930

Ref country code: IE

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20140914

Ref country code: IT

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20140914

REG Reference to a national code

Ref country code: ES

Ref legal event code: FD2A

Effective date: 20160128

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: ES

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20140915