EP1074605B1 - 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

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Publication number
EP1074605B1
EP1074605B1 EP00112339A EP00112339A EP1074605B1 EP 1074605 B1 EP1074605 B1 EP 1074605B1 EP 00112339 A EP00112339 A EP 00112339A EP 00112339 A EP00112339 A EP 00112339A EP 1074605 B1 EP1074605 B1 EP 1074605B1
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Prior art keywords
rapeseed
rape
crush
rolling
rolling mill
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EP00112339A
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German (de)
English (en)
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EP1074605A1 (fr
Inventor
Felix Horst Prof. Dr.-Ing. Schneider
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    • 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 oilseed after going through a classifying deck is first dried, broken and sighted and finally after preparing a press is fed.
  • the invention further relates to a Establishment for the implementation of the procedure. to 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, where 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 removed 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 extracted oils for fuel purposes or 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 be used directly for the production of fuel 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 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 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 Roll 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 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
  • Rapeseed peeling has gained no importance in practice. Rather, it is usually used in manufacturing of edible oil, the crushed rapeseed first and then pressed. Here pass through the high shin 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.
  • chlorophyll By pressing the whole rapeseed with husks shell-specific ingredients such as chlorophyll, Waxes, free fatty acids and tannins (bitter substances) in the crude oil, thereby reducing the quality of the crude oil about the negative influence of high press temperatures is also negatively influenced.
  • chlorophyll and its breakdown products act as prooxidants; they reduce the durability and impair the sensory quality of the oil.
  • the tannins deteriorate the sensors and give the oil a bitter grassy Taste. Those that cannot be removed even by refining Waxes of the shells remain in the oil and act as Crystallization nuclei in cool storage.
  • 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 To produce cooking oil while avoiding the oil thermally stressful and energetically complex Refining or damping immediately as high quality Cooking oil can be used.
  • trimmings consist of foreign seeds, parts of plants and various contaminants, the cleaned Rapeseed from whole rapeseed and a small one Proportion of plant parts and the caraway grain from stunted or opened rapeseed, plant parts 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 has, the high levels of 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 pre-break than in the Postbreak is set.
  • the mean gap width of the roll gap during the preliminary break the average 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.
  • 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 set such 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 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.
  • 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 advantageous as a continuous one Colander screw press with a reed breaker.
  • the rapeseed AC freed from metal parts is 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.
  • the cleaned and classified rapeseed AE is then dried in a dryer 3 and then broken.
  • the trimmings AD and the Kümmer grain AF are fed to a silo 12 .
  • the dried rapeseed AG is expediently broken 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 sizes, namely in opening AJ, consisting of broken rapeseed or components of 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 into 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 - is returned to 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 peel 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 strainer 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.

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  • 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)

Claims (16)

  1. Procédé pour la préparation d'huile alimentaire à partir de graine de colza ou d'autres graines oléagineuses, procédé au cours duquel la graine de colza ou la graine oléagineuse est, après avoir parcouru un plan de calibrage, d'abord séchées, broyées et triées pour être ensuite, après un conditionnement, conduites ensuite à une presse,
    caractérisé
    1.1 en ce que la graine de colza (A.A) est séparée au moyen d'une machine de criblage (2) en trois fractions ayant des dimensions des particules différentes, à savoir en résidu (A.D), en graine de colza purifiée (A.E) et en grains chétifs (A.F),
    1.2 en ce que la graine de colza purifiée et calibrée (A.E) est ensuite séchée à une température de séchage, en dessous d'une température limite de 40 °C, jusqu'à une teneur en eau du grain de colza entier de 4,5 % à 5,5 %, et le résidu (A.D) ainsi que les grains chétifs (A.F) sont amenés vers un silo (12),
    1.3 en ce que la graine de colza séchée (A.G) est ensuite broyée dans un broyeur à cylindres (4),
    1.4 en ce que la graine de colza broyée - le colza brisé (A.H) - est séparée par triage en trois fractions ayant des dimensions de particules différentes, à savoir en brisures amorcées (A.J), en brisures utilisables (A.M) et en brisures fines (A.N),
    1.5 en ce que les brisures utilisables (A.M) sont séparées dans un séparateur (7) en colza décortiqué (A.O) et en téguments (A.P), et les brisures amorcées (A.J) ainsi que les brisures fines (A.N) sont amenées vers le silo (12),
    1.6 en ce que le colza décortiqué (A.O) est humidifié et est ensuite soumis à la floculation dans un autre broyeur à cylindres - un broyeur à cylindres de floculation (9),
    1.7 en ce que le colza soumis à floculation (P.C) est ensuite soumis à un pressage à froid dans une presse (10),
    1.8 et en ce que l'huile alimentaire (P.F) est enfin produite par purification de l'huile de pressage (P.D) sortant de la presse (10) à la suite d'une séparation des produits troubles (matières solides).
  2. Procédé suivant la revendication 1, caractérisé en ce que la séparation de la graine de colza (A.A) en trois fractions se déroule de telle façon que la dimension des particules du résidu (A.D) est supérieure par un facteur de 1,1 fois au diamètre moyen du grain de colza, que la dimension de la graine de colza purifiée (A.E) se situe entre 0,7 fois et 1,1 fois cette valeur, et que la dimension des grains chétifs (A.F) est plus petite que 0,7 fois cette valeur.
  3. Procédé suivant la revendication 1 ou 2, caractérisé en ce que la température de séchage de la graine de colza purifiée et calibrée (A.E) s'élève à un maximum de 35 °C.
  4. Procédé suivant la revendication 1, 2 ou 3, caractérisé en ce que le broyage de la graine de colza purifiée et séchée (A.G) est effectué en deux passages consécutifs dans le broyeur à cylindre, à savoir qu'on effectue d'abord un pré-broyage et ensuite un post-broyage, chaque fois dans un broyeur à cylindres (4) avec des cylindres lisses, alors que l'ouverture moyenne de la fente résultant de l'écartement des cylindres est réglée de façon plus large lors du pré-broyage que lors du post-broyage.
  5. Procédé suivant la revendication 4, caractérisé en ce que le réglage de l'ouverture moyenne de la fente est effectué de telle manière que l'ouverture moyenne de la fente résultant de l'écartement des cylindres est ajustée lors du pré-broyage à 0,4 fois jusqu'à 0,5 fois la valeur du diamètre moyen du grain de colza, et à 0,3 fois jusqu'à 0,4 fois cette même valeur lors du post-broyage.
  6. Procédé suivant l'une des revendications 1 à 5, caractérisé en ce que la séparation des brisures de colza (A.H) en trois fractions se déroule de telle façon que la dimension des particules des brisures amorcées (A.J) est supérieure à 0,7 fois le diamètre moyen du grain de colza, que la dimension des particules des brisures utilisables (A.M) se situe entre 0,2 fois et 0,7 fois cette valeur, et que la dimension des particules des brisures fines (A.N) est inférieure à 0,2 fois cette valeur.
  7. Procédé suivant l'une des revendications 1 à 6, caractérisé en ce que le conditionnement du colza décortiqué (P.A) par une humidification est effectué à une température inférieure à une température limite de 40 °C, et en ce que la teneur en eau est alors ajustée à 5 % jusqu'à 7 %.
  8. Procédé suivant la revendication 7, caractérisé en ce que le conditionnement du colza décortiqué (P. A) est effectué de telle façon que la teneur en eau s'élève à 5,5 % jusqu'à 6,5 %.
  9. Procédé suivant la revendication 7 ou 8, caractérisé en ce que le conditionnement du colza décortiqué (P.A) est effectué à une température d'au maximum 35 °C.
  10. Procédé suivant la revendication 7, 8 ou 9, caractérisé en ce que le colza décortiqué humidifié (P.B) est désagrégé dans un broyeur à cylindres de floculation (9) avec des cylindres lisses et un glissement d'environ de 5 %.
  11. Procédé suivant la revendication 10, caractérisé en ce que, lors de la floculation du colza décortiqué (P.B) l'ouverture de la fente entre cylindres pour les cylindres lisses du broyeur à cylindres de floculation (9) est réglée de telle façon que l'ouverture moyenne de la fente résultant de l'écartement des cylindres s'élève à 0,4 fois jusqu'à 0,5 fois la valeur du diamètre moyen du grain de colza.
  12. Installation pour l'exécution du procédé suivant l'une des revendications 1 à 11, caractérisé en ce que les unités suivantes sont disposées les unes après les autres dans la direction de passage de la graine de colza ou d'un produit semblable,
    une machine de tamisage (2),
    un sécheur (3)
    un broyeur à cylindres (4),
    une autre machine de tamisage (5),
    un séparateur (7),
    un conditionneur (8),
    un broyeur à cylindres de floculation (9),
    et une presse (10).
  13. Installation suivant la revendication 12, caractérisée en ce que le broyeur à cylindres (4) comporte deux paires de cylindres qui sont disposées l'une au-dessus de l'autre et qui sont équipées de cylindres lisses, l'ouverture de la fente résultant de l'écartement des cylindres pour la paire de cylindres supérieure étant alors choisie plus grande que l'ouverture de la fente résultant de l'écartement des cylindres pour la paire de cylindres inférieure.
  14. Installation suivant la revendication 13, caractérisée en ce que l'ouverture de la fente résultant de l'écartement des cylindres pour la paire de cylindres supérieure est ajustée à 0,4 fois jusqu'à 0,5 fois la valeur du diamètre moyen du grain de colza, et en ce que l'ouverture de la fente résultant de l'écartement des cylindres pour la paire de cylindres inférieure est ajustée à 0,3 fois jusqu'à 0,4 fois cette valeur.
  15. Installation suivant l'une des revendications 12 à 14, caractérisée en ce que le séparateur (7), dans lequel les brisures utilisables (A.M) sont subdivisées en colza décortiqué (A.O) et en téguments (A.P), est configuré comme un séparateur à air.
  16. Installation suivant l'une des revendications 12 à 15, caractérisée en ce que la presse (10) est configurée comme une extrudeuse à vis filtrante continue avec un broyeur de fibres.
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
DE19937081 1999-08-06
DE19937081A DE19937081C2 (de) 1999-08-06 1999-08-06 Verfahren und Einrichtung zur Herstellung von Speiseöl aus Rapssaat

Publications (2)

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

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

Cited By (4)

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WO2011029612A2 (fr) 2009-09-11 2011-03-17 Teutoburger Ölmühle GmbH & Co. KG Utilisation de graines de colza décortiquées
WO2017059354A1 (fr) * 2015-10-02 2017-04-06 Crown Iron Works Company Récupération de chaleur pour le fonctionnement de conditionneur et cuiseur de graines
DE102016014735A1 (de) 2016-12-12 2018-06-14 Teutoburger Ölmühle GmbH Bearbeitung von ölhaltigen Saaten
RU2788094C1 (ru) * 2019-04-09 2023-01-16 Юро-Протеин ГмбХ Способ и устройство для промышленного производства рапсового масла и концентрата рапсового белка из рапсового семени

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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
FR2873129B1 (fr) * 2004-07-16 2006-11-03 Univ Compiegne Tech Procede d'extraction d'huile a partir de graines oleagineuses ou proteagineuses incluant un traitement par decharges electriques de haute tension
PL208504B1 (pl) 2007-08-09 2011-05-31 Inst Agrofizyki Im Bohdana Dobrzańskiego Polskiej Akademii Nauk Sposób wytwarzania oleju jadalnego z rzepaku
DE102012013756A1 (de) 2011-07-13 2013-01-17 Contec Maschinenbau Klocke Gmbh Verfahren und Einrichtung zur Gewinnung von Pflanzenölen aus ölhaltigen Pflanzenprodukten
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
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
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
EP3550004B1 (fr) 2018-04-03 2020-09-09 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
CN108745450B (zh) * 2018-08-18 2020-04-21 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
CN109825361A (zh) * 2019-03-21 2019-05-31 安徽农业大学 一种马泡瓜油的制备方法
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
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
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
CA3185127A1 (fr) * 2020-07-06 2022-01-13 Chad Wakeland-Rosen Produits a base de graines de chanvre et procedes et systemes pour leur fabrication
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
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
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WO2011029612A2 (fr) 2009-09-11 2011-03-17 Teutoburger Ölmühle GmbH & Co. KG Utilisation de graines de colza décortiquées
WO2011029611A2 (fr) 2009-09-11 2011-03-17 Teutoburger Ölmühle GmbH & Co. KG Utilisation de graines de colza décortiquées
DE102009040925A1 (de) 2009-09-11 2011-03-31 Teutoburger Ölmühle GmbH & Co. KG Nutzung von geschälten Rapssamen
WO2017059354A1 (fr) * 2015-10-02 2017-04-06 Crown Iron Works Company Récupération de chaleur pour le fonctionnement de conditionneur et cuiseur de graines
DE102016014735A1 (de) 2016-12-12 2018-06-14 Teutoburger Ölmühle GmbH Bearbeitung von ölhaltigen Saaten
DE102016014735B4 (de) 2016-12-12 2019-02-07 Christian Schein Bearbeitung von ölhaltigen Saaten
RU2788094C1 (ru) * 2019-04-09 2023-01-16 Юро-Протеин ГмбХ Способ и устройство для промышленного производства рапсового масла и концентрата рапсового белка из рапсового семени

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EP1074605A1 (fr) 2001-02-07
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PL201206B1 (pl) 2009-03-31
DK1074605T3 (da) 2003-12-01
PL341836A1 (en) 2001-02-12
DE19937081A1 (de) 2001-02-15
DE50003425D1 (de) 2003-10-02

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