EP0591981A1 - Procédé d'extraction de graisses et d'huiles - Google Patents
Procédé d'extraction de graisses et d'huiles Download PDFInfo
- Publication number
- EP0591981A1 EP0591981A1 EP93116266A EP93116266A EP0591981A1 EP 0591981 A1 EP0591981 A1 EP 0591981A1 EP 93116266 A EP93116266 A EP 93116266A EP 93116266 A EP93116266 A EP 93116266A EP 0591981 A1 EP0591981 A1 EP 0591981A1
- Authority
- EP
- European Patent Office
- Prior art keywords
- extraction
- oils
- oil
- fats
- pressure
- 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
-
- C—CHEMISTRY; METALLURGY
- C11—ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
- C11B—PRODUCING, e.g. BY PRESSING RAW MATERIALS OR BY EXTRACTION FROM WASTE MATERIALS, REFINING OR PRESERVING FATS, FATTY SUBSTANCES, e.g. LANOLIN, FATTY OILS OR WAXES; ESSENTIAL OILS; PERFUMES
- C11B1/00—Production of fats or fatty oils from raw materials
- C11B1/10—Production of fats or fatty oils from raw materials by extracting
- C11B1/104—Production of fats or fatty oils from raw materials by extracting using super critical gases or vapours
Definitions
- the present invention relates to a process for the extraction of fats and oils from natural substances, such as e.g. Vegetable, animal or microbial raw materials, with the help of liquid propane as a solvent, this process for the production of fats and oils as well as for the production of degreased or oiled products, which are becoming increasingly important as low-fat and thus low-calorie products in the food sector. is applicable.
- natural substances such as e.g. Vegetable, animal or microbial raw materials
- a disadvantage of conventional solvent extraction is the fact that most solvents are not toxicologically safe and that the extracted fats and oils and the extraction residues must be largely solvent-free before they can be used for food or feed purposes. This requires comparatively high temperatures, which can negatively affect the sensory properties of the products.
- the separation has the largest technical Importance.
- the difference in density of meat and fat components is usually used after thermal or mechanical digestion of the starting material in order to carry out a separation in separators or decanters.
- this method cannot be used to produce fatty meat products with a fat content below 10%, otherwise the loss of meat is too high.
- extractive processes which, in the case of the use of organic solvents, have the disadvantages already mentioned.
- the present invention was therefore based on the object of developing a process for the extraction of fats and oils from natural substances with the aid of propane as a solvent, which does not have the disadvantages of the prior art mentioned and which, without great technical outlay, has both sufficient gas loading with fats and oils as well as a good sensory quality of the products.
- all fat-containing or oil-containing natural substances based on plants, animals or microbes can be used for the process according to the invention.
- vegetable fats or oils are olive oil, palm oil, bamboo fat, coconut fat, cocoa butter, coffee oils, peanut butter, rapeseed oil (rapeseed oil), flax oil (linseed oil), sunflower oil, wheat germ oil, rice germ oil, cottonseed oil, corn germ oil, soybean oil, palm kernel oil and pumpkin seed oil.
- beef or veal and marine oils such as e.g. Fish oils in question.
- the method according to the invention can also be used for fermentation residues, for example from yeasts, fungi or bacteria.
- the extraction material in comminuted, pelletized form.
- the (in particular solid) starting material have a have a high water content, such as meat or fermentation residues, it has proven to be particularly advantageous to reduce the moisture to below 50% by suitable drying methods before the extraction.
- the extraction with liquid propane is carried out in a very narrow and defined pressure and temperature range which is 10 to 30 bar or 10 to 55 ° C.
- the process is preferably carried out at an extraction pressure of 15 to 25 bar and an extraction temperature of 20 to 45 ° C.
- the extraction pressure and temperature must be coordinated so that the propane is in a liquid state.
- the amount of propane gas used can be varied within wide limits and depends essentially on the amount of oil or fat to be extracted. Depending on the type of raw material, 2.5 to 500 g of liquid propane are normally required per g of fat or oil to be extracted. The maximum gas loading with lipid substances under these extraction conditions is 5 to 25% by weight, depending on the type of fat or oil extracted.
- the purity of the propane gas used is relatively uncritical in most cases, i.e. noticeable amounts of impurities from homologous hydrocarbons (due to the refining process) can also be present without any noticeable loss in quality.
- Propane is preferably used in technical purity of approx. 90% and in deodorized form.
- the extraction with liquid propane can in some cases also be carried out in two or more stages in order to obtain the fats or oils completely.
- the propane gas is preferably circulated in order to be able to load the desired lipid substances several times, but it is also possible to contact the extraction material only once with the extraction medium.
- several extraction autoclaves can be connected in series and the extraction medium can be flowed through in succession.
- the maximum achievable gas load of the liquid propane can always be optimally used by suitably switching the sequence of these autoclaves (e.g. flow through according to the advanced degree of extraction).
- fats and oils dissolved in the liquid propane are separated by reducing the pressure and / or increasing the temperature, a reduction in pressure and an increase in temperature to ⁇ 80 ° C. having proven particularly advantageous. In this way it is ensured that no undesired reactions such as isomerization of the double bonds of polyunsaturated fatty acids take place during the deposition.
- the deposition is carried out by isobaric evaporation of the solvent, as a result of which the economy of the process can be increased significantly.
Landscapes
- Chemical & Material Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Wood Science & Technology (AREA)
- Organic Chemistry (AREA)
- Fats And Perfumes (AREA)
Applications Claiming Priority (4)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE4233911 | 1992-10-08 | ||
DE4233911 | 1992-10-08 | ||
DE4326399A DE4326399C2 (de) | 1992-10-08 | 1993-08-06 | Verfahren zur Extraktion von Fetten und Ölen |
DE4326399 | 1993-08-06 |
Publications (2)
Publication Number | Publication Date |
---|---|
EP0591981A1 true EP0591981A1 (fr) | 1994-04-13 |
EP0591981B1 EP0591981B1 (fr) | 1996-12-11 |
Family
ID=25919292
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP93116266A Expired - Lifetime EP0591981B1 (fr) | 1992-10-08 | 1993-10-07 | Procédé d'extraction de graisses et d'huiles |
Country Status (8)
Country | Link |
---|---|
US (1) | US5405633A (fr) |
EP (1) | EP0591981B1 (fr) |
JP (1) | JPH06207193A (fr) |
AT (1) | ATE146216T1 (fr) |
CA (1) | CA2107864A1 (fr) |
DK (1) | DK0591981T3 (fr) |
ES (1) | ES2097415T3 (fr) |
RU (1) | RU2062295C1 (fr) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0739975A1 (fr) * | 1995-02-08 | 1996-10-30 | SKW Trostberg Aktiengesellschaft | Procédé pour la purification des dérivés carbohydrés avec une activité surfactante |
EP0812903A1 (fr) * | 1994-04-05 | 1997-12-17 | Agritech International, L.L.C. | Extraction d'huile à partir de parties de plantes oléagineuses |
Families Citing this family (39)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE4222153C2 (de) * | 1992-07-06 | 1998-12-03 | Peter Siegfried | Verfahren zur Entölung von Rohlecithin |
GB9406423D0 (en) * | 1994-03-31 | 1994-05-25 | Ici Plc | Solvent extraction process |
DE4447116A1 (de) * | 1994-12-29 | 1996-07-04 | Sueddeutsche Kalkstickstoff | Verfahren zur Fraktionierung bzw. Raffination von lipiden Naturstoffen |
US6015913A (en) * | 1996-09-06 | 2000-01-18 | Mars, Incorporated | Method for producing fat and/or solids from cocoa beans |
US6905715B1 (en) | 1996-09-06 | 2005-06-14 | Mars, Incorporated | Cocoa solids having a high cocoa procyanidin content |
US6737088B1 (en) | 1996-09-06 | 2004-05-18 | Mars, Incorporated | Cocoa extracts prepared from cocoa solids having high cocoa polyphenol contents |
US6312753B1 (en) | 1996-09-06 | 2001-11-06 | Mars, Incorporated | Cocoa components, edible products having enriched polyphenol content, methods of making same and medical uses |
US5707673A (en) * | 1996-10-04 | 1998-01-13 | Prewell Industries, L.L.C. | Process for extracting lipids and organics from animal and plant matter or organics-containing waste streams |
MY127634A (en) * | 1996-10-31 | 2006-12-29 | Global Palm Products Sdn Bhd | Refining of edible oil rich in natural carotenes and vitamin e |
US6177114B1 (en) | 1996-10-31 | 2001-01-23 | Carotina Sdn. Bhd. | Refining of edible oil rich in natural carotenes and Vitamin E |
US6066350A (en) * | 1997-02-07 | 2000-05-23 | Cargill Incorporated | Method and arrangement for processing cocoa mass |
US6090432A (en) * | 1997-08-26 | 2000-07-18 | Mckeown; Michael J. | Health enhancing salad dressing |
US5980964A (en) * | 1998-06-18 | 1999-11-09 | Gilroy Foods, D/B/A/Conagra Corporation | Extraction of oil from oil bearing products with a chilled liquefied normally gaseous solvent |
TR199903215A2 (xx) * | 1998-12-23 | 2001-05-21 | Unilever N.V. | Oleanolik asit ile takviye edilmi� g�da �r�nlerinin haz�rlanmas� i�in i�lem |
US6111119A (en) * | 1999-01-14 | 2000-08-29 | Cocotech, Inc. | Process for removing oil from food products |
GB0027047D0 (en) * | 2000-11-06 | 2000-12-20 | Ici Plc | Process for reducing the concentration of undesired compounds in a composition |
DE10101326A1 (de) * | 2001-01-13 | 2002-07-25 | Fraunhofer Ges Forschung | Verfahren zur Herstellung von emulgierfähigen Proteinprodukten aus einer Ölsaat |
US6551642B2 (en) * | 2001-03-08 | 2003-04-22 | Cocotech, Inc. | Process for removing oil from foodstuffs using a membrane filter |
US6569480B2 (en) | 2001-04-30 | 2003-05-27 | Donald R. Hall | Liquefied gas extraction process |
US20040071847A1 (en) * | 2002-10-15 | 2004-04-15 | Cargill, Inc. | Producing cocoa powders with different cocoa butter contents by liquefied gas extraction on substantially the same production line |
US7201934B2 (en) | 2002-10-15 | 2007-04-10 | Cargill, Incorporated | Dispersible cocoa products |
US20040071848A1 (en) * | 2002-10-15 | 2004-04-15 | Cargill Inc. | Process for producing cocoa butter and cocoa powder by liquefied gas extraction |
NZ523920A (en) | 2003-01-31 | 2005-11-25 | Fonterra Co Operative Group | Methods for extracting lipids from diary products using a near critical phase fluid |
US7384557B2 (en) | 2003-07-14 | 2008-06-10 | Applied Ambient Extraction Process Consultants, Llc | Method and apparatus for removing solute from a solid solute-bearing product |
FR2865642A1 (fr) * | 2004-01-29 | 2005-08-05 | Oreal | Procede de preparation d'une composition de traitement cosmetique a partir de fluide sous pression, de ceramides, de cires et/ou de silicones |
US20050175717A1 (en) * | 2004-01-29 | 2005-08-11 | L'oreal | (Cosmetic) composition, process of making, uses thereof |
US20050170023A1 (en) * | 2004-01-29 | 2005-08-04 | L'oreal | Composition, process for making using pressurized fluid, and uses thereof |
US20050169876A1 (en) * | 2004-01-29 | 2005-08-04 | L'oreal | Composition for treating keratin material, process of making, uses thereof |
FR2865643B1 (fr) * | 2004-01-29 | 2007-10-19 | Oreal | Procede de preparation d'une composition pour le traitement cosmetique des matieres keratiniques a partir de fluide sous pression et de subtances vegetales |
US20050170063A1 (en) * | 2004-01-29 | 2005-08-04 | Lalit Chordia | Production of powder and viscous material |
FR2865637B1 (fr) * | 2004-01-29 | 2007-10-05 | Oreal | Procede de preparation d'une composition pour le traitement cosmetique des matieres keratiniques a partir de fluide sous pression et de composes cosmetiquement actifs pieges par des particules |
DE102005037209A1 (de) * | 2005-08-06 | 2007-02-08 | Degussa Ag | Verfahren zur Gewinnung von natürlichen Ölen aus pflanzlichen Bestandteilen |
FR2905862A1 (fr) * | 2006-09-20 | 2008-03-21 | Oreal | Procede de preparation d'une composition ayant des proprietes antibacteriennes |
US8859793B2 (en) * | 2011-10-27 | 2014-10-14 | Jerry Hamler | Process for extracting oil from plants and animal matter |
US9169455B2 (en) * | 2011-10-27 | 2015-10-27 | Jerry Hamler | Process for extracting oil from plants and animal matter |
RU2550076C2 (ru) * | 2013-04-16 | 2015-05-10 | Федеральное государственное бюджетное образовательное учреждение высшего профессионального образования "Астраханский государственный университет" | Способ получения и состав масла из семян тыквы |
US9296979B1 (en) | 2014-12-12 | 2016-03-29 | Metal Industries Research & Development Centre | Flower essential oil extraction method |
US10758579B2 (en) | 2016-12-07 | 2020-09-01 | Metagreen Ventures | Systems and methods for extraction of natural products |
US20190308116A1 (en) * | 2018-04-10 | 2019-10-10 | Craig Alan Brodersen | Solvent based cannabinoid extraction process with improved efficiency, safety, quality, which yields a homogenous and pasteurized product |
Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US1802533A (en) * | 1928-09-13 | 1931-04-28 | Columbia Engineering & Man Cor | Extraction of oils |
DE1069629B (de) * | 1959-11-26 | Mölndal Herbert Peter August Groll (Schweden) | Verfahren zum Fraktionieren von ölartligen Gemischen hoh'ermolekularer organischer Verbindungen durch selektive Extraktion | |
US3939281A (en) * | 1972-11-14 | 1976-02-17 | Pfeifer & Langen | Extraction of fat from starch-containing vegetable matter |
DE3228927A1 (de) * | 1982-08-03 | 1984-02-09 | Extraktionstechnik Gesellschaft für Anlagenbau mbH, 2000 Hamburg | Verfahren zur kontinuierlichen extraktion von schuettfaehigen feststoffen |
JPS6456793A (en) * | 1987-08-27 | 1989-03-03 | Mori Seiyu Kk | Method for extracting and separating vegetable fat and oil |
US5041245A (en) * | 1989-03-10 | 1991-08-20 | Bioseparations, Inc. | Continuous extraction of oil-containing vegetable matter with pressurized normally gaseous solvent |
Family Cites Families (10)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB1444551A (en) * | 1972-10-18 | 1976-08-04 | Unilever Ltd | Solvent extraction of glyceride oils |
IL79838A0 (en) * | 1976-08-26 | 1986-11-30 | Vitamins Inc | Mass transfer extraction of liquids from solids |
DE3322968A1 (de) * | 1983-06-25 | 1985-01-10 | Fried. Krupp Gmbh, 4300 Essen | Verfahren und vorrichtung zur gewinnung von fetten und oelen |
US5210240A (en) * | 1984-08-09 | 1993-05-11 | Siegfried Peter | Process for the extraction of oil containing vegetable materials |
US5169968A (en) * | 1985-09-10 | 1992-12-08 | Vitamins, Inc. | Mass separation of liquid or soluble components from solid materials utilizing supercritical fluids |
US5290959A (en) * | 1985-09-10 | 1994-03-01 | Vitamins, Inc. | Mass separation of materials |
US4749522A (en) * | 1985-10-31 | 1988-06-07 | Angio-Medical Corporation | Supercritical fluid extraction of animal derived materials |
US4981579A (en) * | 1986-09-12 | 1991-01-01 | The Standard Oil Company | Process for separating extractable organic material from compositions comprising said extractable organic material intermixed with solids and water |
US5170727A (en) * | 1991-03-29 | 1992-12-15 | Union Carbide Chemicals & Plastics Technology Corporation | Supercritical fluids as diluents in combustion of liquid fuels and waste materials |
US5281732A (en) * | 1991-12-31 | 1994-01-25 | University Research & Marketing | Solvent extraction of oil from oil-bearing materials |
-
1993
- 1993-10-04 US US08/131,296 patent/US5405633A/en not_active Expired - Lifetime
- 1993-10-06 CA CA002107864A patent/CA2107864A1/fr not_active Abandoned
- 1993-10-07 ES ES93116266T patent/ES2097415T3/es not_active Expired - Lifetime
- 1993-10-07 JP JP5251744A patent/JPH06207193A/ja active Pending
- 1993-10-07 DK DK93116266.3T patent/DK0591981T3/da active
- 1993-10-07 EP EP93116266A patent/EP0591981B1/fr not_active Expired - Lifetime
- 1993-10-07 AT AT93116266T patent/ATE146216T1/de not_active IP Right Cessation
- 1993-10-07 RU RU9393056645A patent/RU2062295C1/ru active
Patent Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE1069629B (de) * | 1959-11-26 | Mölndal Herbert Peter August Groll (Schweden) | Verfahren zum Fraktionieren von ölartligen Gemischen hoh'ermolekularer organischer Verbindungen durch selektive Extraktion | |
US1802533A (en) * | 1928-09-13 | 1931-04-28 | Columbia Engineering & Man Cor | Extraction of oils |
US3939281A (en) * | 1972-11-14 | 1976-02-17 | Pfeifer & Langen | Extraction of fat from starch-containing vegetable matter |
DE3228927A1 (de) * | 1982-08-03 | 1984-02-09 | Extraktionstechnik Gesellschaft für Anlagenbau mbH, 2000 Hamburg | Verfahren zur kontinuierlichen extraktion von schuettfaehigen feststoffen |
JPS6456793A (en) * | 1987-08-27 | 1989-03-03 | Mori Seiyu Kk | Method for extracting and separating vegetable fat and oil |
US5041245A (en) * | 1989-03-10 | 1991-08-20 | Bioseparations, Inc. | Continuous extraction of oil-containing vegetable matter with pressurized normally gaseous solvent |
Non-Patent Citations (2)
Title |
---|
M. MATTIKOW: "Refining fatty oils with liquid propane", JOURNAL OF THE AMERICAN OIL CHEMISTS' SOCIETY., vol. 27, no. 1, 1950, CHAMPAIGN US, pages 11 - 14 * |
PATENT ABSTRACTS OF JAPAN vol. 13, no. 255 (C - 606)<3603> 12 June 1989 (1989-06-12) * |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0812903A1 (fr) * | 1994-04-05 | 1997-12-17 | Agritech International, L.L.C. | Extraction d'huile à partir de parties de plantes oléagineuses |
EP0739975A1 (fr) * | 1995-02-08 | 1996-10-30 | SKW Trostberg Aktiengesellschaft | Procédé pour la purification des dérivés carbohydrés avec une activité surfactante |
US5703228A (en) * | 1995-02-08 | 1997-12-30 | Skw Trostberg Aktiengesellschaft | Process for the purification of carbohydrate derivatives with surface-active properties |
Also Published As
Publication number | Publication date |
---|---|
EP0591981B1 (fr) | 1996-12-11 |
JPH06207193A (ja) | 1994-07-26 |
ATE146216T1 (de) | 1996-12-15 |
DK0591981T3 (da) | 1997-06-09 |
ES2097415T3 (es) | 1997-04-01 |
CA2107864A1 (fr) | 1994-04-09 |
US5405633A (en) | 1995-04-11 |
RU2062295C1 (ru) | 1996-06-20 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
EP0591981B1 (fr) | Procédé d'extraction de graisses et d'huiles | |
DE4429506B4 (de) | Verfahren zur Extraktion natürlicher Carotinoid-Farbstoffe | |
DE4219360C2 (de) | Verfahren zur Gewinnung von Lipiden mit einem hohen Anteil von langkettig-hochungesättigten Fettsäuren | |
DE60027692T2 (de) | Verfahren für die behandlung von pflanzenöl-miscella | |
DE69406776T2 (de) | Entfernung von phospholipiden aus glyceridoelen | |
DE2147970A1 (de) | Verfahren zum Herstellen eines Proteinkonzentrats aus Pflanzensamen | |
EP0761765B1 (fr) | Procédé pour l'extraction de colorants de carotène à partir de produits naturels | |
DE2363418A1 (de) | Verfahren zur gewinnung von fetten und oelen aus pflanzlichen und tierischen produkten | |
DE4407917C2 (de) | Verfahren zur Gewinnung von Lipidfraktionen aus pulverförmigen Eiprodukten | |
CH618326A5 (fr) | ||
DE2448233A1 (de) | Fettzusammensetzung | |
EP0615694B1 (fr) | Procédé de préparation de poudres à base d'oeuf à teneur réduite en matière grasse et cholestérol | |
DE4326399C2 (de) | Verfahren zur Extraktion von Fetten und Ölen | |
DE69105988T2 (de) | Extrahiere von cholesterin aus eigelb. | |
EP1648987B1 (fr) | Procede pour produire des matieres premieres pour la production de bougies ainsi que matiere accumulatrice de chaleur | |
DE2147327A1 (de) | Verfahren zur Trennung von Phos phatiden aus Phosphaüdmischungen | |
DE1467498A1 (de) | Verfahren zum Extrahieren von OEl aus pflanzlichem Gut | |
DE2602998C3 (de) | Verfahren zum Auftrennen eines Öls oder Fettes in eine flüssige und eine feste Fraktion | |
LU102019B1 (de) | Verfahren zur Herstellung von Öl aus einem Mikroalgenerzeugnis | |
DE2355892A1 (de) | Verfahren zur herstellung von pflanzenproteinhaltigem material | |
DE102016115911A1 (de) | Wertprodukt und Verfahren zur Gewinnung einer Wertstoffphase | |
DE2937327A1 (de) | Verfahren zur herstellung eines oxydationsstabilisators und dessen verwendung zum stabilisieren von oelen oder fetten | |
DE551102C (de) | Verfahren zur Extraktion von pflanzlichen Rohstoffen | |
AT316291B (de) | Verfahren zur Herstellung einer speisewürzenden Zwiebelcreme | |
DE410170C (de) | Verfahren zur Entfernung der freien, nicht fluechtigen Fettsaeuren aus pflanzlichen und tierischen OElen und Fetten oder zur Destillation nicht fluechtiger Fettsaeuren |
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 DE DK ES FR GB GR IT LU NL PT |
|
17P | Request for examination filed |
Effective date: 19940531 |
|
17Q | First examination report despatched |
Effective date: 19950728 |
|
GRAG | Despatch of communication of intention to grant |
Free format text: ORIGINAL CODE: EPIDOS AGRA |
|
GRAH | Despatch of communication of intention to grant a patent |
Free format text: ORIGINAL CODE: EPIDOS IGRA |
|
GRAH | Despatch of communication of intention to grant a patent |
Free format text: ORIGINAL CODE: EPIDOS IGRA |
|
GRAA | (expected) grant |
Free format text: ORIGINAL CODE: 0009210 |
|
AK | Designated contracting states |
Kind code of ref document: B1 Designated state(s): AT BE DE DK ES FR GB GR IT LU NL PT |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
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: 19961211 |
|
REF | Corresponds to: |
Ref document number: 146216 Country of ref document: AT Date of ref document: 19961215 Kind code of ref document: T |
|
ITF | It: translation for a ep patent filed |
Owner name: JACOBACCI & PERANI S.P.A. |
|
GBT | Gb: translation of ep patent filed (gb section 77(6)(a)/1977) |
Effective date: 19961211 |
|
REF | Corresponds to: |
Ref document number: 59304742 Country of ref document: DE Date of ref document: 19970123 |
|
ET | Fr: translation filed | ||
REG | Reference to a national code |
Ref country code: PT Ref legal event code: SC4A Free format text: AVAILABILITY OF NATIONAL TRANSLATION Effective date: 19961212 |
|
REG | Reference to a national code |
Ref country code: ES Ref legal event code: FG2A Ref document number: 2097415 Country of ref document: ES Kind code of ref document: T3 |
|
REG | Reference to a national code |
Ref country code: DK Ref legal event code: T3 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: GB Payment date: 19970915 Year of fee payment: 5 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: NL Payment date: 19970919 Year of fee payment: 5 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: DK Payment date: 19970924 Year of fee payment: 5 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: AT Payment date: 19970925 Year of fee payment: 5 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: LU Payment date: 19971003 Year of fee payment: 5 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: PT Payment date: 19971008 Year of fee payment: 5 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: BE Payment date: 19971010 Year of fee payment: 5 |
|
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 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: ES Payment date: 19971021 Year of fee payment: 5 |
|
26N | No opposition filed | ||
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: 19981007 Ref country code: GB Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 19981007 Ref country code: DK Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 19981007 Ref country code: AT Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 19981007 |
|
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 EXPIRATION OF PROTECTION Effective date: 19981008 |
|
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: 19981031 |
|
BERE | Be: lapsed |
Owner name: SKW TROSTBERG A.G. Effective date: 19981031 |
|
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: 19990430 |
|
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 NON-PAYMENT OF DUE FEES Effective date: 19990501 |
|
GBPC | Gb: european patent ceased through non-payment of renewal fee |
Effective date: 19981007 |
|
NLV4 | Nl: lapsed or anulled due to non-payment of the annual fee |
Effective date: 19990501 |
|
REG | Reference to a national code |
Ref country code: PT Ref legal event code: MM4A Free format text: LAPSE DUE TO NON-PAYMENT OF FEES Effective date: 19990430 |
|
REG | Reference to a national code |
Ref country code: ES Ref legal event code: FD2A Effective date: 20010201 |
|
REG | Reference to a national code |
Ref country code: DK Ref legal event code: EBP |
|
REG | Reference to a national code |
Ref country code: FR Ref legal event code: TP |
|
REG | Reference to a national code |
Ref country code: FR Ref legal event code: RM |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: IT Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES;WARNING: LAPSES OF ITALIAN PATENTS WITH EFFECTIVE DATE BEFORE 2007 MAY HAVE OCCURRED AT ANY TIME BEFORE 2007. THE CORRECT EFFECTIVE DATE MAY BE DIFFERENT FROM THE ONE RECORDED. Effective date: 20051007 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: DE Payment date: 20121023 Year of fee payment: 20 Ref country code: FR Payment date: 20121031 Year of fee payment: 20 |
|
REG | Reference to a national code |
Ref country code: DE Ref legal event code: R071 Ref document number: 59304742 Country of ref document: DE |
|
REG | Reference to a national code |
Ref country code: DE Ref legal event code: R071 Ref document number: 59304742 Country of ref document: DE |
|
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 EXPIRATION OF PROTECTION Effective date: 20131008 |