Nothing Special   »   [go: up one dir, main page]

EP1074605A1 - Procédé et appareil de production d'huile de cuisson à partir de colza - Google Patents

Procédé et appareil de production d'huile de cuisson à partir de colza Download PDF

Info

Publication number
EP1074605A1
EP1074605A1 EP00112339A EP00112339A EP1074605A1 EP 1074605 A1 EP1074605 A1 EP 1074605A1 EP 00112339 A EP00112339 A EP 00112339A EP 00112339 A EP00112339 A EP 00112339A EP 1074605 A1 EP1074605 A1 EP 1074605A1
Authority
EP
European Patent Office
Prior art keywords
rapeseed
rape
press
particle size
nip
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
EP00112339A
Other languages
German (de)
English (en)
Other versions
EP1074605B1 (fr
Inventor
Felix Horst Prof. Dr.-Ing. Schneider
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.)
SCHNEIDER FELIX HORST PROF DR
Original Assignee
SCHNEIDER FELIX HORST PROF DR
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 SCHNEIDER FELIX HORST PROF DR filed Critical SCHNEIDER FELIX HORST PROF DR
Publication of EP1074605A1 publication Critical patent/EP1074605A1/fr
Application granted granted Critical
Publication of EP1074605B1 publication Critical patent/EP1074605B1/fr
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Images

Classifications

    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B02—CRUSHING, PULVERISING, OR DISINTEGRATING; PREPARATORY TREATMENT OF GRAIN FOR MILLING
    • B02C—CRUSHING, PULVERISING, OR DISINTEGRATING IN GENERAL; MILLING GRAIN
    • B02C9/00—Other milling methods or mills specially adapted for grain
    • B02C9/04—Systems or sequences of operations; Plant
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B02—CRUSHING, PULVERISING, OR DISINTEGRATING; PREPARATORY TREATMENT OF GRAIN FOR MILLING
    • B02B—PREPARING GRAIN FOR MILLING; REFINING GRANULAR FRUIT TO COMMERCIAL PRODUCTS BY WORKING THE SURFACE
    • B02B3/00—Hulling; Husking; Decorticating; Polishing; Removing the awns; Degerming
    • B02B3/04—Hulling; Husking; Decorticating; Polishing; Removing the awns; Degerming by means of rollers
    • B02B3/045—Hulling; Husking; Decorticating; Polishing; Removing the awns; Degerming by means of rollers cooperating rollers
    • 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
    • C11B1/02—Pretreatment
    • 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
    • C11B1/02—Pretreatment
    • C11B1/04—Pretreatment of vegetable raw material
    • 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
    • C11B1/06—Production of fats or fatty oils from raw materials by pressing
    • 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
    • C11B1/102—Production of fats or fatty oils from raw materials by extracting in counter-current; utilisation of an equipment wherein the material is conveyed by a screw

Definitions

  • the invention relates to a method for producing Edible oil from rapeseed or other oil seeds, the Rapeseed or the like after passing through a classifying deck is first dried, broken and sifted and finally after preparing a press is fed.
  • the invention further relates to a Establishment for the implementation of the procedure. For In the following, simplification is only related to rapeseed taken.
  • One of the cited references (DE-PS 21 35 173) relates to a process for peeling granular oil fruits, in which the grains are subjected to an impact become. This is done in a short time interval Grains heated to about 45 ° C using a stream of cold air against diagonally to the flow direction Impact plates thrown. The broken up Grains are then made mechanically by friction without oil extraction separated from the shell by the one with the Airflow blended grains of a helical shape Be subjected to movement between friction walls.
  • the second cited reference (DD-PS 131 530) relates to a process for the disclosure of oil and proteinaceous seeds, the casing by a Deformation of the seeds released from the core meat and then shell and core meat separated become. To remove the shell from the core meat, the Seeds of a defined deformation between two exposed to rigid surfaces, causing the shell to flake off. This then takes place in a subsequent viewing process Separation of the casing from the core meat.
  • the other cited reference (DE-OS 40 41 994) relates to a method and an arrangement for rape peeling, that with the extraction of core fractions Shell proportions ⁇ 5% as required for later use won oils for fuel purposes or also for other technical purposes are required. This is done through a combined pressure and impact treatment of the seeds. The won The core fraction can directly be used for fuel production following processes.
  • the known method sees u. a. before that cleaned Rapeseed hot - at a temperature of 95 ° C - dried and then by single-stage rolling is peeled, the nip 0.2 times to Corresponds to 0.4 times the average seed grain diameter.
  • Detaching the broken shells from the Core meat is made by impact impact loops at one pneumatic conveying, if necessary by a Air separation and a separation of the shells from the core meat through electrical separation.
  • the technological The rape peeling arrangement consists of a seed bunker, a scale, a roller peeler, a cyclone, one Air classifier and an electric separator. This well known The process has significant disadvantages in terms of technology. The hot drying of the seeds leads to the known quality disadvantages that of thermally stressed material extracted crude oils.
  • the one-time rolling for disassembly the seed with a wide grain spectrum in one Roller gap of 0.45 mm leads to crushing of the seeds and thus to oil leakage, whereby the disassembly of the Mixtures in the subsequent visual process is made more difficult.
  • the known method therefore requires an additional one pneumatic conveyance with loosening by impact impact and an additional, energetically unfavorable wind sifting for separating unpeeled seeds before the actual separation of the mixture on the electric classifier he follows.
  • Rapeseed peeling has gained no importance in practice. Rather, it is usually used in manufacturing of edible oil the rapeseed is squeezed first and then squeezed out. Here pass through the high shell content relatively many waxes and other ingredients into the cooking oil, which is only a small Quality. The known methods of manufacture of cooking oil from oilseeds therefore need Cleaning the oils a chemical and physical Refining.
  • Conventional rapeseed processing works to increase yield in plants with larger processing capacity with a hydro-thermal treatment of the Sowing before pressing.
  • the usual conditioning temperatures of up to 100 ° C increase the adverse influences of the high press temperatures.
  • the Contents of free fatty acids and phosphatides in the press oil are further increased compared to non-preheated seeds.
  • the oils pressed from not preheated seeds are used to improve sensor technology and durability often damping at temperatures above 100 ° C subjected.
  • the oils pressed from conditioned seeds must be refined at temperatures> 200 ° C become.
  • the high temperatures of damping and Refining lead to the formation of nutritionally negative trans fatty acids and to reduce the Contains volatile, valuable vitamins.
  • the invention has for its object a method and to create a facility to cold-press Make cooking oil while avoiding the oil thermally stressful and energetically complex Refining or damping immediately as high quality Cooking oil can be used.
  • the stocking consists of foreign seeds, plant parts and various contaminants, the cleaned Rapeseed from whole rapeseed and a small one Proportion of plant parts and the caraway grain from stunted or cracked rapeseed, parts of plants and Fine dust together.
  • Cooking oil only shows extremely low levels unwanted ingredients. It is therefore high-quality cooking oil. A subsequent one Post-treatment by refining or steaming is not required. With the cooking oil obtained, one fine nutty own taste to be evaluated positively the high levels of the get volatile vitamins. This is achieved by removing the majority of the rape shells and due to the low pressing temperatures. To the current state of knowledge can be assumed be that for press oils that come from the press with a limit temperature below 40 ° C, none quality-damaging processes are to be expected. At Pressing the reduced-seed seed without further pretreatment may be more intense due to warming Friction in the colander screw press the mentioned Limit temperature must not be fallen below.
  • the separation rapeseed is divided into three fractions in such a way that the particle size of the fill is more than 1.1 times, the particle size of the cleaned rapeseed between 0.7 times and 1.1 times and the Particle size of the kernel grain is less than 0.7 times of the average rapeseed grain diameter.
  • the drying temperature is expediently the cleaned and classified rapeseed maximum 35 ° C. This measure contributes significantly to a Damage to fatty acids, denaturation of proteins and prevent activation of the seed enzymes.
  • the breaking of the cleaned and dried rapeseed in two consecutive Rolling operations, and that takes place first Prebreak and then post-break, each in one Rolling mill with smooth rolls, the mean gap width of the nip is larger in the preliminary break than in the Postbreak is set.
  • the mean gap width of the roll gap during the preliminary break the mean gap width of the roll gap at the pre-break to 0.4 times to 0.5 times and at the refraction to 0.3 times to 0.4 times the medium rapeseed diameter set.
  • the rapeseed core only disintegrates into its natural five elements, like two outer and two inner Cotyledons as well as the seedling because the elements are only in in a closely localized area are. An essential oil leak from the rapeseed elements is avoided.
  • the pressing of the peeled rape with a low shell content on screw presses at low temperatures To enable the peeling rape to be conditioned by humidifying at a temperature below 40 ° C, with a water content of 5% to 7%, preferably is set from 5.5% to 6.5%.
  • a water content of 5% to 7% preferably is set from 5.5% to 6.5%.
  • the nip of the smooth rollers of the flaking mill adjusted so that the mean gap width of the nip 0.04 times to 0.05 times the average rapeseed grain diameter.
  • the by-products collected in the silo can be one be used for further use, for example as Feed.
  • the pressed reeds made from peeled rapeseed already have a significantly higher feed value because of a significantly reduced crude fiber content compared to reeds made from unpeeled seeds.
  • the low power consumption and the low wear of the screw press are to be mentioned, which significantly increases the service life.
  • the energetic use of the separated by-products, but especially the shell fraction provides a CO 2 -neutral full supply of the production process with both electrical and thermal energy.
  • the invention Procedure can be carried out without problems.
  • the facility can still be improved in that the rolling mill two pairs of rolls arranged one above the other has, which are provided with smooth rollers, the Roller gap of the upper pair of rollers is chosen larger, than the nip of the lower pair of rollers. Conveniently is the nip width of the nip of the upper pair of rollers 0.4 times to 0.5 times and the nip width of the nip of the lower pair of rollers 0.3 to 0.4 times the mean Rapeseed grain diameter set.
  • the press is a continuous one Colander screw press with a reed breaker.
  • the rapeseed AC which has been freed from metal parts, is then separated in a screening machine 2 into three fractions of different particle size, namely in fill AD, for example straw or foreign seeds, into cleaned rapeseed AE and Kümmer grain AF, which also includes cracked grain. Then the cleaned and classified rapeseed AE is dried in a dryer 3 and then broken. The trimmings AD and the Kümmer grain AF are fed to a silo 12 .
  • the drying of the rapeseed AG expediently takes place in a rolling mill 4 with two pairs of rolls arranged one above the other in two consecutive rolling processes without intermediate sighting. Both pairs of rollers have smooth rollers that run without slippage. There is first a preliminary breaking by means of the upper pair of rollers and then a subsequent breaking by means of the lower pair of rollers of the rolling mill 4 , the roller gap of the upper pair of rollers being chosen larger than the roller gap of the lower pair of rollers.
  • the broken rapeseed - the rapeseed rape AH - is separated in a further screening machine 5 into three fractions of different particle size, namely in the first rupture AJ , consisting of broken rapeseed or components of the rapeseed, in useful fraction AM , consisting of rapeseed husks and rapeseed elements separated from one another , and in Feinbruch AN, consisting of rapeseed husk particles and rapeseed meat particles.
  • the usable breakdown AM is broken down in a sifter 7 in peeled rape AO, consisting of rapeseed core elements with a small proportion of shell fragments, and in shells AP with a small proportion of core meat particles, while the opening AJ either via a distributor 6 - as described AK indicated - back into the rolling mill 4 or - as indicated by the designation AL - in the silo 12 .
  • the fine fraction AN and the shells AP are also fed into the silo 12 .
  • the classifier 7 can be designed as an air classifier or electrical classifier.
  • the peeling rape AO is designated PA in the area of the pressing process.
  • the water content of the peeling rape PA is increased in a conditioner 8 , namely by cold wetting with water.
  • the peel rape PA is then - without preheating - broken down in a flaking mill 9 by means of smooth rolling with a defined shear field.
  • the flaked peeled rape PC is then cold pressed in a press 10 , which is expediently designed as a colander screw press with a reed crusher, the press oil PD obtained in this way subsequently being cleaned of trub substances (solids) in a filter 11 and the press oil PD in cooking oil PF and is separated into filter cake PE .
  • the filter cake PE is returned to the press 10 .
  • the mixture PH accumulated in the silo 12 from the by-products trimming AD, Riemmerkorn AF, opening AL Feinbruch AN and trays AP can be used energetically as animal feed or as fuel.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Wood Science & Technology (AREA)
  • Organic Chemistry (AREA)
  • Food Science & Technology (AREA)
  • Fats And Perfumes (AREA)
  • Edible Oils And Fats (AREA)
EP00112339A 1999-08-06 2000-06-09 Procédé et appareil de production d'huile de cuisson à partir de colza Expired - Lifetime EP1074605B1 (fr)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
DE19937081A DE19937081C2 (de) 1999-08-06 1999-08-06 Verfahren und Einrichtung zur Herstellung von Speiseöl aus Rapssaat
DE19937081 1999-08-06

Publications (2)

Publication Number Publication Date
EP1074605A1 true EP1074605A1 (fr) 2001-02-07
EP1074605B1 EP1074605B1 (fr) 2003-08-27

Family

ID=7917397

Family Applications (1)

Application Number Title Priority Date Filing Date
EP00112339A Expired - Lifetime EP1074605B1 (fr) 1999-08-06 2000-06-09 Procédé et appareil de production d'huile de cuisson à partir de colza

Country Status (5)

Country Link
EP (1) EP1074605B1 (fr)
AT (1) ATE248213T1 (fr)
DE (2) DE19937081C2 (fr)
DK (1) DK1074605T3 (fr)
PL (1) PL201206B1 (fr)

Cited By (18)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2001084949A2 (fr) * 2000-05-09 2001-11-15 Her Majesty The Queen In Right Of Canada As Represented By The Minister Of Fisheries And Oceans Sources de proteines et de lipides utilisees dans l'alimentation de la faune aquatique et dans l'alimentation animale et procede de preparation
US6955831B2 (en) 2000-05-09 2005-10-18 Her Majesty The Queen In Right Of Canada As Represented By The Minister Of Fisheries And Oceans Protein and lipid sources for use in aquafeeds and animal feeds and a process for their preparation
FR2873129A1 (fr) * 2004-07-16 2006-01-20 Univ Compiegne Tech Procede d'extraction d'huile a partir de graines oleagineuses ou proteagineuses incluant un traitement par decharges electriques de haute tension
WO2009020409A2 (fr) 2007-08-09 2009-02-12 Instytut Agrofizyki Im. Bohdana Dobrzanskiego Polskiej Akademii Nauk Procédé de production d'huile alimentaire à partir de graines de colza
EP2475268A2 (fr) * 2009-09-11 2012-07-18 Teutoburger Ölmühle GmbH & Co. KG Utilisation de graines de colza décortiquées
CN103710139A (zh) * 2013-12-20 2014-04-09 南通家惠油脂发展有限公司 菜籽中温压榨生产油脂的方法
RU2525254C1 (ru) * 2013-02-22 2014-08-10 Федеральное государственное бюджетное образовательное учреждение высшего профессионального образования "Кубанский государственный технологический университет" (ФГБОУ ВПО "КубГТУ") Способ подготовки масличных семян к хранению и переработке
CN103981013A (zh) * 2014-05-30 2014-08-13 安徽渡民粮油有限公司 一种冷榨菜籽油生产工艺
CN104130854A (zh) * 2014-07-14 2014-11-05 新疆天鹰生物科技有限公司 一种冷榨油方法
CN108745450A (zh) * 2018-08-18 2018-11-06 芜湖市好亦快食品有限公司三山分公司 一种便于高效筛分且易清理的碾米装置
EP3550004A1 (fr) 2018-04-03 2019-10-09 Euro-Protein GmbH Procédé et dispositif de traitement de graines de colza industriel permettant d'obtenir l'huile de noyau de colza pressée à froid
CN111635816A (zh) * 2020-06-03 2020-09-08 怀宁县金田园油脂有限公司 一种菜籽榨油精炼工艺
WO2020207565A1 (fr) 2019-04-09 2020-10-15 Neumueller Waldemar Procédé et dispositif de collecte industrielle d'huile de colza et de concentré de protéines de colza à partir de graines de colza
US10982170B2 (en) * 2019-03-21 2021-04-20 Anhui Agricultural University Extraction methods of field muskmelon seed oil
CN113145223A (zh) * 2021-04-27 2021-07-23 郝飞龙 一种能够防止出油口堵塞的菜籽油生产加工设备
WO2022010776A1 (fr) * 2020-07-06 2022-01-13 Victory Foods, Pbc Produits à base de graines de chanvre et procédés et systèmes pour leur fabrication
US11576400B2 (en) * 2020-07-06 2023-02-14 Victory Foods, Pbc Methods for producing a hemp seed product
DE102020122456B4 (de) 2020-08-27 2024-07-25 Euro-Protein GmbH Verfahren zur industriellen Gewinnung von kaltgepresstem Kernöl aus geschälten ölhaltigen Saaten unter Einsatz einer Saat-eigenen Presshilfe

Families Citing this family (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE102012013756A1 (de) 2011-07-13 2013-01-17 Contec Maschinenbau Klocke Gmbh Verfahren und Einrichtung zur Gewinnung von Pflanzenölen aus ölhaltigen Pflanzenprodukten
EP3356501A4 (fr) * 2015-10-02 2019-04-03 Crown Iron Works Company Récupération de chaleur pour le fonctionnement de conditionneur et cuiseur de graines
DE102016014735B4 (de) 2016-12-12 2019-02-07 Christian Schein Bearbeitung von ölhaltigen Saaten
MX2019008704A (es) 2017-01-24 2020-01-14 Crown Iron Works Co Seccion de calentamiento de contenedor de semillas modular vertical.
DE102017005155A1 (de) 2017-05-31 2018-12-06 Christian Schein Bearbeitung von ölhaltigen Saaten, insbesondere Rapssamen
DE102017010083A1 (de) 2017-10-30 2019-05-02 Christian Schein Bearbeitung eines Preßkuchens und/oder Pulvers aus ölhaltigen Saaten
DE102019001591A1 (de) * 2019-05-02 2020-11-05 Teutoburger Ölmühle GmbH Bearbeitung von öhlhaltigen Saaten, insbesondere Rapssamen
DE102020002144A1 (de) 2020-04-03 2021-10-07 Christian Schein Bearbeitung von Rapssaaten
DE102021005992A1 (de) 2021-12-04 2023-06-07 Christian Schein Herstellung eines Lebensmittels

Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE131530C (fr)
DE2135173A1 (de) 1971-07-14 1973-03-22 Leslie Palyi Verfahren und vorrichtung zum schaelen von rapssaat
DE2635169A1 (de) * 1976-08-05 1978-02-09 Felix Horst Dr Ing Schneider Verfahren zur enthuellung von oel- und proteinhaltigen saatkoernern
US4083836A (en) * 1974-05-17 1978-04-11 Alfa-Laval Ab Production of rapeseed protein concentrate for human consumption
CH675128A5 (en) * 1986-06-11 1990-08-31 Thaelmann Schwermaschbau Veb Processing oil-rich oil-seeds
DE4041994A1 (de) 1990-12-27 1992-07-02 Thaelmann Schwermaschbau Veb Verfahren und anordnung zur rapsschaelung
US5696278A (en) * 1993-03-17 1997-12-09 Unilever Patent Holdings B.V. Degumming of crude glyceride oils not exposed to prior enzymatic activity

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE4109229C2 (de) * 1991-03-21 1995-08-17 Bauss Hans Werner Schnecken-Ölpresse

Patent Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE131530C (fr)
DE2135173A1 (de) 1971-07-14 1973-03-22 Leslie Palyi Verfahren und vorrichtung zum schaelen von rapssaat
US4083836A (en) * 1974-05-17 1978-04-11 Alfa-Laval Ab Production of rapeseed protein concentrate for human consumption
DE2635169A1 (de) * 1976-08-05 1978-02-09 Felix Horst Dr Ing Schneider Verfahren zur enthuellung von oel- und proteinhaltigen saatkoernern
CH675128A5 (en) * 1986-06-11 1990-08-31 Thaelmann Schwermaschbau Veb Processing oil-rich oil-seeds
DE4041994A1 (de) 1990-12-27 1992-07-02 Thaelmann Schwermaschbau Veb Verfahren und anordnung zur rapsschaelung
US5696278A (en) * 1993-03-17 1997-12-09 Unilever Patent Holdings B.V. Degumming of crude glyceride oils not exposed to prior enzymatic activity

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
WAN ET AL: "Technology and Solvents for Extracting Oilseeds and Nonpetroleum Oils", US,CHAMPAIGN, AOCS PRESS, PAGE(S) 101-120, ISBN: 0-935315-81-0, XP002124895 *

Cited By (26)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2001084949A2 (fr) * 2000-05-09 2001-11-15 Her Majesty The Queen In Right Of Canada As Represented By The Minister Of Fisheries And Oceans Sources de proteines et de lipides utilisees dans l'alimentation de la faune aquatique et dans l'alimentation animale et procede de preparation
WO2001084949A3 (fr) * 2000-05-09 2002-05-02 United Kingdom Government Sources de proteines et de lipides utilisees dans l'alimentation de la faune aquatique et dans l'alimentation animale et procede de preparation
US6955831B2 (en) 2000-05-09 2005-10-18 Her Majesty The Queen In Right Of Canada As Represented By The Minister Of Fisheries And Oceans Protein and lipid sources for use in aquafeeds and animal feeds and a process for their preparation
FR2873129A1 (fr) * 2004-07-16 2006-01-20 Univ Compiegne Tech Procede d'extraction d'huile a partir de graines oleagineuses ou proteagineuses incluant un traitement par decharges electriques de haute tension
WO2009020409A2 (fr) 2007-08-09 2009-02-12 Instytut Agrofizyki Im. Bohdana Dobrzanskiego Polskiej Akademii Nauk Procédé de production d'huile alimentaire à partir de graines de colza
WO2009020409A3 (fr) * 2007-08-09 2009-03-26 Inst Agrofizyki Im Bohdana Dob Procédé de production d'huile alimentaire à partir de graines de colza
US9427013B2 (en) 2009-09-11 2016-08-30 Teutoburger Ölmühle GmbH & Co. KG Use of hulled rapeseed
EP2475268A2 (fr) * 2009-09-11 2012-07-18 Teutoburger Ölmühle GmbH & Co. KG Utilisation de graines de colza décortiquées
EP2475267B1 (fr) * 2009-09-11 2019-06-19 Teutoburger Ölmühle GmbH & Co. KG Utilisation de graines de colza décortiquées
US9642388B2 (en) 2009-09-11 2017-05-09 Teutoburger Ölmühle GmbH & Co. KG Utilization of hulled rape seed
RU2525254C1 (ru) * 2013-02-22 2014-08-10 Федеральное государственное бюджетное образовательное учреждение высшего профессионального образования "Кубанский государственный технологический университет" (ФГБОУ ВПО "КубГТУ") Способ подготовки масличных семян к хранению и переработке
CN103710139B (zh) * 2013-12-20 2015-08-19 南通家惠油脂发展有限公司 菜籽中温压榨生产油脂的方法
CN103710139A (zh) * 2013-12-20 2014-04-09 南通家惠油脂发展有限公司 菜籽中温压榨生产油脂的方法
CN103981013A (zh) * 2014-05-30 2014-08-13 安徽渡民粮油有限公司 一种冷榨菜籽油生产工艺
CN104130854A (zh) * 2014-07-14 2014-11-05 新疆天鹰生物科技有限公司 一种冷榨油方法
EP3550004A1 (fr) 2018-04-03 2019-10-09 Euro-Protein GmbH Procédé et dispositif de traitement de graines de colza industriel permettant d'obtenir l'huile de noyau de colza pressée à froid
CN108745450A (zh) * 2018-08-18 2018-11-06 芜湖市好亦快食品有限公司三山分公司 一种便于高效筛分且易清理的碾米装置
US10982170B2 (en) * 2019-03-21 2021-04-20 Anhui Agricultural University Extraction methods of field muskmelon seed oil
WO2020207565A1 (fr) 2019-04-09 2020-10-15 Neumueller Waldemar Procédé et dispositif de collecte industrielle d'huile de colza et de concentré de protéines de colza à partir de graines de colza
CN114026209A (zh) * 2019-04-09 2022-02-08 W·诺伊米勒 用于从油菜籽工业地获取菜籽油和油菜籽蛋白质浓缩物的方法和装置
CN111635816A (zh) * 2020-06-03 2020-09-08 怀宁县金田园油脂有限公司 一种菜籽榨油精炼工艺
WO2022010776A1 (fr) * 2020-07-06 2022-01-13 Victory Foods, Pbc Produits à base de graines de chanvre et procédés et systèmes pour leur fabrication
US11576400B2 (en) * 2020-07-06 2023-02-14 Victory Foods, Pbc Methods for producing a hemp seed product
US12016349B2 (en) 2020-07-06 2024-06-25 Victory Foods, Pbc Hemp seed products and methods and systems for producing same
DE102020122456B4 (de) 2020-08-27 2024-07-25 Euro-Protein GmbH Verfahren zur industriellen Gewinnung von kaltgepresstem Kernöl aus geschälten ölhaltigen Saaten unter Einsatz einer Saat-eigenen Presshilfe
CN113145223A (zh) * 2021-04-27 2021-07-23 郝飞龙 一种能够防止出油口堵塞的菜籽油生产加工设备

Also Published As

Publication number Publication date
EP1074605B1 (fr) 2003-08-27
DE19937081C2 (de) 2002-05-02
DE19937081A1 (de) 2001-02-15
ATE248213T1 (de) 2003-09-15
DE50003425D1 (de) 2003-10-02
DK1074605T3 (da) 2003-12-01
PL201206B1 (pl) 2009-03-31
PL341836A1 (en) 2001-02-12

Similar Documents

Publication Publication Date Title
EP1074605B1 (fr) Procédé et appareil de production d'huile de cuisson à partir de colza
EP0052218B1 (fr) Procédé de traitement de graines de soja
EP0129739A2 (fr) Procédé et appareil pour l'obtention de graisses et d'huiles
EP3681308B1 (fr) Procédé d'obtention de préparations de protéine issues des graines oléagineuses de tournesols et/ou de colza ainsi que la préparation de protéine
EP2475267B1 (fr) Utilisation de graines de colza décortiquées
DE102008043140A1 (de) Verfahren und Einrichtung zur Herstellung von pflanzlichen Mahlprodukten
EP1311166A2 (fr) Procede pour extraire l'aleurone du son
DE68923481T2 (de) Verfahren zum Behandeln von Sojabohnen.
EP3550004B1 (fr) Procédé et dispositif de traitement de graines de colza industriel permettant d'obtenir l'huile de noyau de colza pressée à froid
EP2550106B1 (fr) Methode et dispositif pour décortiquer les semis de colza
EP3953442A1 (fr) Procédé et dispositif de collecte industrielle d'huile de colza et de concentré de protéines de colza à partir de graines de colza
DE102020122456B4 (de) Verfahren zur industriellen Gewinnung von kaltgepresstem Kernöl aus geschälten ölhaltigen Saaten unter Einsatz einer Saat-eigenen Presshilfe
AT395251B (de) Verfahren zur aufbereitung fettreicher oelsamen
EP2654449B1 (fr) Procédé de fractionnement de graines de jatropha
DE2453911C3 (de) Verfahren zur Gewinnung von Öl aus pflanzlichen Rohstoffen mit mehr als 25 % Ölgehalt
SU810792A1 (ru) Способ получени растительногоМАСлА из ВыСОКО-МАСличНОгОМАТЕРиАлА
SU733722A1 (ru) Способ очистки сем н сои от дурнишника
DE3828941A1 (de) Verfahren und vorrichtung zur gewinnung von fetten und oelen einerseits und direkt als futtermittel geeignetes schrot andererseits aus sojabohnen
DE2916296A1 (de) Verfahren zum entfernen von fremdstoffen aus pflanzlichem proteinhaltigem material
DD275612A1 (de) Verfahren und vorrichtung zur schaelung von leguminosensamen
DE102005035149A1 (de) Kaffeeröstverfahren und Getränkegrundlage
EA024445B1 (ru) Способ переработки семян рапса

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: 20010310

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

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

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: IT

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT;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: 20030827

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: 20030827

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: 20030827

Ref country code: IE

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: 20030827

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: GERMAN

REF Corresponds to:

Ref document number: 50003425

Country of ref document: DE

Date of ref document: 20031002

Kind code of ref document: P

REG Reference to a national code

Ref country code: SE

Ref legal event code: TRGR

GBT Gb: translation of ep patent filed (gb section 77(6)(a)/1977)

Effective date: 20031021

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: 20031127

REG Reference to a national code

Ref country code: DK

Ref legal event code: T3

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 FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20031208

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 FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20040127

REG Reference to a national code

Ref country code: IE

Ref legal event code: FD4D

ET Fr: translation 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: 20040609

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: 20040630

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: 20040528

REG Reference to a national code

Ref country code: FR

Ref legal event code: PLFP

Year of fee payment: 17

REG Reference to a national code

Ref country code: DE

Ref legal event code: R082

Ref document number: 50003425

Country of ref document: DE

Representative=s name: COHAUSZ & FLORACK PATENT- UND RECHTSANWAELTE P, DE

Ref country code: DE

Ref legal event code: R081

Ref document number: 50003425

Country of ref document: DE

Owner name: TEUTOBURGER OELMUEHLE GMBH, DE

Free format text: FORMER OWNER: SCHNEIDER, FELIX HORST, PROF. DR.-ING., 45239 ESSEN, DE

REG Reference to a national code

Ref country code: FR

Ref legal event code: PLFP

Year of fee payment: 18

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

Ref country code: DE

Payment date: 20170622

Year of fee payment: 18

Ref country code: DK

Payment date: 20170621

Year of fee payment: 18

Ref country code: GB

Payment date: 20170620

Year of fee payment: 18

Ref country code: FR

Payment date: 20170621

Year of fee payment: 18

Ref country code: CH

Payment date: 20170620

Year of fee payment: 18

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

Ref country code: SE

Payment date: 20170620

Year of fee payment: 18

Ref country code: NL

Payment date: 20170620

Year of fee payment: 18

Ref country code: BE

Payment date: 20170620

Year of fee payment: 18

Ref country code: AT

Payment date: 20170622

Year of fee payment: 18

REG Reference to a national code

Ref country code: DE

Ref legal event code: R119

Ref document number: 50003425

Country of ref document: DE

REG Reference to a national code

Ref country code: DK

Ref legal event code: EBP

Effective date: 20180630

REG Reference to a national code

Ref country code: SE

Ref legal event code: EUG

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 NON-PAYMENT OF DUE FEES

Effective date: 20180610

REG Reference to a national code

Ref country code: CH

Ref legal event code: PL

REG Reference to a national code

Ref country code: NL

Ref legal event code: MM

Effective date: 20180701

REG Reference to a national code

Ref country code: AT

Ref legal event code: MM01

Ref document number: 248213

Country of ref document: AT

Kind code of ref document: T

Effective date: 20180609

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

Effective date: 20180609

REG Reference to a national code

Ref country code: BE

Ref legal event code: MM

Effective date: 20180630

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: 20180701

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

Ref country code: AT

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

Effective date: 20180609

Ref country code: DE

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

Effective date: 20190101

Ref country code: GB

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

Effective date: 20180609

Ref country code: CH

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

Effective date: 20180630

Ref country code: FR

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

Effective date: 20180630

Ref country code: LI

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

Effective date: 20180630

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: 20180630

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

Ref country code: DK

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

Effective date: 20180630