EP0591981B1 - Procédé d'extraction de graisses et d'huiles - Google Patents

Procédé d'extraction de graisses et d'huiles Download PDF

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Publication number
EP0591981B1
EP0591981B1 EP93116266A EP93116266A EP0591981B1 EP 0591981 B1 EP0591981 B1 EP 0591981B1 EP 93116266 A EP93116266 A EP 93116266A EP 93116266 A EP93116266 A EP 93116266A EP 0591981 B1 EP0591981 B1 EP 0591981B1
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.)
Expired - Lifetime
Application number
EP93116266A
Other languages
German (de)
English (en)
Other versions
EP0591981A1 (fr
Inventor
Jürgen Dr. Heidlas
Jan Dr. Cully
Heinz-Rüdiger Dr. Vollbrecht
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.)
Evonik Operations GmbH
Original Assignee
SKW Trostberg AG
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
Priority claimed from DE4326399A external-priority patent/DE4326399C2/de
Application filed by SKW Trostberg AG filed Critical SKW Trostberg AG
Publication of EP0591981A1 publication Critical patent/EP0591981A1/fr
Application granted granted Critical
Publication of EP0591981B1 publication Critical patent/EP0591981B1/fr
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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 de-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 For the degreasing of animal raw materials, such as fatty meat, the separation has the largest technical Meaning.
  • 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 process cannot produce fatty meat products with a fat content lower than 10%, otherwise the loss of meat is too high.
  • extractive processes must be used, which have the disadvantages already mentioned in the case of the use of organic solvents.
  • 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 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)

Claims (8)

  1. Procédé pour l'extraction des matières grasses et d'huiles à partir de substances naturelles à l'aide de propane liquide en tant que solvant, caractérisé en ce que l'on effectue l'extraction à une pression de 10 à 30 bars et à une température de 10 à 55°C et l'on procède à la séparation des matières grasses et huiles extraites du solvant par diminution de la pression et ou augmentation de la température jusqu'à ≤ ou égal à 80°C.
  2. Procédé selon la revendication 1, caractérisé en ce que l'on effectue l'extraction à une pression de 15 à 25 bars et à une température de 20 à 45°C.
  3. Procédé selon la revendication 1 ou 2, caractérisé en ce que l'on procède à la séparation par évaporation isobare du solvant.
  4. Procédé selon l'une des revendications 1 à 3, caractérisé en ce que la matière de départ contenant la matière grasse ou l'huile est mise en oeuvre sous la forme granulée ou agglomérée en boulettes.
  5. Procédé selon l'une des revendications 1 à 4, caractérisé en ce que l'on utilise le propane liquide dans une quantité de 2,5 à 500 g. par g. de la matière grasse ou de l'huile à extraire.
  6. Procédé selon l'une des revendications 1 à 5, caractérisé en ce que la charge en gaz des matières grasses et des huiles est de 5 à 25 % en poids.
  7. Procédé selon l'une des revendications 1 à 6, caractérisé en ce que l'on met en oeuvre le propane liquide dans une pureté technique (environ 90 %) et sous forme désodorisée.
  8. Procédé selon l'une des revendications 1 à 7, caractérisé en ce que l'on procède à l'extraction dans plusieurs autoclaves d'extraction montés en série.
EP93116266A 1992-10-08 1993-10-07 Procédé d'extraction de graisses et d'huiles Expired - Lifetime EP0591981B1 (fr)

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 EP0591981A1 (fr) 1994-04-13
EP0591981B1 true 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 (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US7709041B2 (en) 1997-02-07 2010-05-04 Cargill, Incorporated Low-fat cocoa powder

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US5516923A (en) * 1992-04-27 1996-05-14 Agritech International Extracting oil from oil bearing plant parts
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
DE19504101A1 (de) * 1995-02-08 1996-08-22 Sueddeutsche Kalkstickstoff Verfahren zur Reinigung von Kohlenhydratderivaten mit oberflächenaktiver Wirkung
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
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
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
US6177114B1 (en) 1996-10-31 2001-01-23 Carotina Sdn. Bhd. Refining of edible oil rich in natural carotenes and Vitamin E
MY127634A (en) * 1996-10-31 2006-12-29 Global Palm Products Sdn Bhd Refining of edible oil rich in natural carotenes and vitamin e
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
US7201934B2 (en) 2002-10-15 2007-04-10 Cargill, Incorporated Dispersible cocoa products
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
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
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
US20050169876A1 (en) * 2004-01-29 2005-08-04 L'oreal Composition for treating keratin material, process of making, uses thereof
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
US20050170023A1 (en) * 2004-01-29 2005-08-04 L'oreal Composition, process for making using pressurized fluid, and uses thereof
US20050170063A1 (en) * 2004-01-29 2005-08-04 Lalit Chordia Production of powder and viscous material
US20050175717A1 (en) * 2004-01-29 2005-08-11 L'oreal (Cosmetic) composition, 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
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
US9169455B2 (en) * 2011-10-27 2015-10-27 Jerry Hamler Process for extracting oil from plants and animal matter
US8859793B2 (en) * 2011-10-27 2014-10-14 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

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Publication number Priority date Publication date Assignee Title
US7709041B2 (en) 1997-02-07 2010-05-04 Cargill, Incorporated Low-fat cocoa powder

Also Published As

Publication number Publication date
RU2062295C1 (ru) 1996-06-20
ATE146216T1 (de) 1996-12-15
EP0591981A1 (fr) 1994-04-13
ES2097415T3 (es) 1997-04-01
DK0591981T3 (da) 1997-06-09
JPH06207193A (ja) 1994-07-26
US5405633A (en) 1995-04-11
CA2107864A1 (fr) 1994-04-09

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