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EP1260571A2 - Procédé et installation pour l'extraction d'huile de fruits et de semences - Google Patents

Procédé et installation pour l'extraction d'huile de fruits et de semences Download PDF

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Publication number
EP1260571A2
EP1260571A2 EP02008998A EP02008998A EP1260571A2 EP 1260571 A2 EP1260571 A2 EP 1260571A2 EP 02008998 A EP02008998 A EP 02008998A EP 02008998 A EP02008998 A EP 02008998A EP 1260571 A2 EP1260571 A2 EP 1260571A2
Authority
EP
European Patent Office
Prior art keywords
pressure
fruit pulp
pressure section
seeds
fruits
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
EP02008998A
Other languages
German (de)
English (en)
Other versions
EP1260571B1 (fr
EP1260571A3 (fr
Inventor
Dr. Steffen Hruschka
Klemens Geissen
Jose Antonio Venegas Rodriguez
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.)
GEA Mechanical Equipment GmbH
Original Assignee
Westfalia Separator Industry GmbH
Westfalia Separator GmbH
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 Westfalia Separator Industry GmbH, Westfalia Separator GmbH filed Critical Westfalia Separator Industry GmbH
Publication of EP1260571A2 publication Critical patent/EP1260571A2/fr
Publication of EP1260571A3 publication Critical patent/EP1260571A3/fr
Application granted granted Critical
Publication of EP1260571B1 publication Critical patent/EP1260571B1/fr
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Classifications

    • CCHEMISTRY; METALLURGY
    • C11ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
    • C11BPRODUCING, 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
    • C11B1/00Production of fats or fatty oils from raw materials
    • C11B1/02Pretreatment
    • C11B1/04Pretreatment of vegetable raw material
    • CCHEMISTRY; METALLURGY
    • C11ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
    • C11BPRODUCING, 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
    • C11B1/00Production of fats or fatty oils from raw materials
    • C11B1/10Production of fats or fatty oils from raw materials by extracting
    • CCHEMISTRY; METALLURGY
    • C11ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
    • C11BPRODUCING, 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
    • C11B1/00Production of fats or fatty oils from raw materials
    • C11B1/10Production of fats or fatty oils from raw materials by extracting
    • C11B1/102Production 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 extracting oil from fruits or seeds, preferably olives or avocados, with a solid-bowl screw centrifuge and a plant for oil production according to the preamble of claim 29.
  • the olives are preprocessed after washing by chopping in a grinder, which the olives without the addition of water or at the Use of dried olives under a water additive, which the Restores the fresh water content of fresh olives, turns them into fruit pulp, which is disrupted in a Malaxeur downstream of the mill.
  • This Digestion in the malaxeur is used to release the oil and then in the Malaxeur downstream solid bowl screw centrifuge in the oil components as well as being able to separate solid and water.
  • the invention solves this problem on the one hand by a method for oil production, which is specified in feature 1. It also solves it through an oil production facility, whose features are specified in claim 29.
  • the fruits or seeds are crushed and during or after subjected to high pressure crushing and subsequent relaxation, whereupon the chopped fruit pulp of the solid bowl screw centrifuge is fed.
  • the invention also provides a plant for extracting oil from fruit or seeds, preferably olives or avocados, with a chopper the fruits or seeds into a pulp, preferably a mill or a Extruder, one of the devices for comminuting - e.g. when using one Extruder - or downstream high pressure section to unlock the Fruit pulp, and a solid bowl screw centrifuge downstream of the high pressure section, preferably provided with a plunger for separation of the pulp in different phases, preferably in oil as the first phase and in a solid / water mixture as the second phase.
  • crushing in one Mill conceivable, either in the mill or preferably after passing through the mill will go through the high pressure section.
  • a particular advantage of the invention is that preprocessing of the pulp when replacing the malaxer with a high pressure path relative can be done quickly. It has been found, for example, that there is a dwell time of just 6 minutes in the high-pressure section can suffice to achieve the Unlock olives enough to use in a solid bowl screw centrifuge to be able to process further.
  • the quality of the oil is the same as in the processing comparable or even better with a quality that can be achieved with a malax.
  • avocados in particular are particularly good with the invention Processable.
  • the high-pressure section can be a pipe - with an upstream one designed accordingly Pumping device - which has a length of more than 10, preferably has a length of 10 to 30 meters.
  • the fruit pulp before entering the high pressure line and / or when passing through the high pressure section - heated by means of a heating device becomes.
  • the fruit pulp is preferred to max. Heated to 40 ° C and when processing avocados to more than 40 ° C, especially 40 ° - 80 ° C.
  • the residence time of the fruit pulp in the high-pressure section is preferably 2 to 12, especially 4 to 8 minutes.
  • the pressure in the high-pressure section more than 10 bar, preferably more than 30 bar, in particular more than 50 bar.
  • a pressure between 50 and 80 is very particularly preferred even more specifically chosen between 60 and 70 bar. So when using a relatively high pressure, the dwell time in the high-pressure section can be reduced to 6 min be lowered.
  • the fruits or seeds are preferred first washed and then crushed, preferably in a mill, in particular in a hammer mill.
  • the fruit pulp is preferably brought out of the high-pressure section with the help of a relief valve relaxed and then directly and / or after further relaxation fed to the solid bowl screw centrifuge in a further buffer tank becomes.
  • the washed olives are first a mill 1 (e.g. hammer mill) fed. No water is added to the olives, provided they are fresh Olives are processed. Only when processing dried olives So much water is added to the olives that the natural water content is fresher Olive is restored.
  • a mill 1 e.g. hammer mill
  • the olives are then transferred from the mill 1, preferably with a pump 2 a pipe 3 is fed to a first buffer tank 4.
  • the first buffer tank 4 relieved the stable operation of the system.
  • Buffer tank 4 and the fruit pulp produced in the mill directly above one or more pumps feed pump 5, this downstream piston pump 6) to be fed to a high-pressure section 7.
  • the high pressure section 7 comprises the pressure zone 7a and the expansion valve 7b.
  • the pressure zone 7a can be, for example, as be designed as a simple pipeline or as another homogenizer.
  • the high pressure section 7 is to be designed such that in the pressure zone 7a and by means of the subsequent relaxation with an expansion valve 7b is sufficient The pulp is unlocked or the oil is released. This is preferred in the high pressure section 7 generates a pressure of more than 50 bar and the High-pressure section 7 or the delivery rate is designed such that the dwell time the fruit pulp in the high pressure section preferably 2 to 12, in particular Is 4 to 8 minutes. Particularly good results were obtained from one Lingering of the pulp in the high pressure section reached at 6 minutes.
  • the temperature of the Fruit pulp should, however, not exceed 40 ° C (production of a high quality Olive oil).
  • the fruit pulp is preferably heated to 30 ° C in the buffer tank. It is also conceivable to heat directly when passing through the high-pressure section. When processing other products such as avocados, there is also a warming to more than 40 ° C - especially 40 - 80 ° C) conceivable.
  • the fruit pulp is either directly or, for example via a further, preferably heatable buffer tank 8 and / or a feed pump 9 the inlet 10 of a solid bowl screw centrifuge (in the Drawing briefly "VS centrifuge") 11 supplied.
  • a further, preferably heatable buffer tank 8 and / or a feed pump 9 the inlet 10 of a solid bowl screw centrifuge (in the Drawing briefly "VS centrifuge") 11 supplied.
  • the pulp is crushed by means of an extruder 12, in which there is an increased pressure in relation to the environment, so that the Extruder 12 itself forms the high pressure section 7.
  • the extruder 12 is the open pulp then directly or via one or more buffers 4 and / or a feed pump 5 is passed into the solid bowl screw centrifuge.
  • the test table of Fig. 4 illustrates that it is with the inventive Process is readily possible to produce an olive oil, in particular It should be borne in mind that the expenditure on equipment compared to the use of a malaxer is significantly reduced. As you can see, it decreases with increasing Temperature of the residual oil content in the Orujo.
  • the experiments for Fig. 4 were carried out with a Structure carried out that corresponds to that of FIG. 1

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)
  • Paper (AREA)
  • Preparation Of Fruits And Vegetables (AREA)
  • Extraction Or Liquid Replacement (AREA)
  • Disintegrating Or Milling (AREA)
EP02008998A 2001-05-15 2002-04-23 Procédé et installation pour l'extraction d'huile de fruits et de graines Expired - Lifetime EP1260571B1 (fr)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
DE10123651A DE10123651A1 (de) 2001-05-15 2001-05-15 Verfahren und Anlage zur Ölgewinnung aus Früchten oder Saaten
DE10123651 2001-05-15

Publications (3)

Publication Number Publication Date
EP1260571A2 true EP1260571A2 (fr) 2002-11-27
EP1260571A3 EP1260571A3 (fr) 2004-01-07
EP1260571B1 EP1260571B1 (fr) 2005-09-28

Family

ID=7684886

Family Applications (1)

Application Number Title Priority Date Filing Date
EP02008998A Expired - Lifetime EP1260571B1 (fr) 2001-05-15 2002-04-23 Procédé et installation pour l'extraction d'huile de fruits et de graines

Country Status (5)

Country Link
EP (1) EP1260571B1 (fr)
AT (1) ATE305501T1 (fr)
DE (2) DE10123651A1 (fr)
ES (1) ES2245999T3 (fr)
PT (1) PT1260571E (fr)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE102011053527A1 (de) 2011-09-12 2013-03-14 Gea Mechanical Equipment Gmbh Verfahren und Anlage zur Aufarbeitung von Alpeorujo
EP2596707A1 (fr) * 2011-11-25 2013-05-29 Universita' Degli Studi di Bari Procédé et dispositif pour le conditionnement thermique d'olives ou d'autres fruits oléagineux, en combinaison avec un système de broyage et de malaxage desdits olives et d'autres fruits oléagineux, sous une atmospère controlée ou modifiée
IT201800007016A1 (it) * 2018-07-06 2020-01-06 Gramolatrice per frantoio oleario e relativo metodo di funzionamento
WO2022200644A1 (fr) 2021-03-26 2022-09-29 Naranjo Lopez Rafael Procédé de production d'huile, produit d'huile et appareil de production d'huile
WO2023287271A1 (fr) * 2021-07-15 2023-01-19 Universidad Autónoma De Nayarit Procédé d'extrusion pour l'extraction d'huiles de la pulpe de fruits de persea spp.

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GR1010263B (el) * 2021-04-08 2022-07-06 Στυλιανος Ιωαννη Τζανακακης Παραγωγη διατροφικων πολτων και παστων χαμηλης ελαιοπεριεκτικοτητας με υβριδισμο της μεθοδου παστοποιησης υδραυλικης αμεσης πιεσης εν ψυχρω με την μεθοδο ελαιοποιησης διφασικου φυγοκεντρικου διαχωρισμου

Family Cites Families (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB418107A (en) * 1934-03-09 1934-10-18 Aage Nyrop Process and device for extracting fats and oils from animal and vegetable material
DE2632045C2 (de) * 1976-07-16 1982-12-02 Emmy 5014 Kerpen Helwig Vorrichtung zur Explosionszerkleinerung von Samen, Früchten oder Pflanzen
FR2442716A1 (fr) * 1978-11-28 1980-06-27 Blanie Paul Procede et dispositifs d'extraction de composants de substances naturelles et artificielles
DE3021083A1 (de) * 1980-06-04 1981-12-10 Gefi Gesellschaft für Industriewärme und Verfahrenstechnik mbH, 4150 Krefeld Verfahren zum zerkleinern von stoffgemischen, insbesondere aus pflanzenprodukten, sowie vorrichtung zur durchfuehrung des verfahrens
EP0212391B1 (fr) * 1985-08-14 1992-06-03 Amandus Kahl Nachf. (GmbH & Co.) Procédé et appareil pour le conditionnement et le prétraitement de graines oléagineuses et fruits oléagineux, en particulier les graines légumineuses
DE4206006C1 (fr) * 1992-02-27 1993-09-16 Westfalia Separator Ag, 59302 Oelde, De
DE10121434B4 (de) * 2001-05-03 2004-08-12 Westfalia Separator Ag Vollmantel-Schneckenzentrifuge

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE102011053527A1 (de) 2011-09-12 2013-03-14 Gea Mechanical Equipment Gmbh Verfahren und Anlage zur Aufarbeitung von Alpeorujo
WO2013037751A1 (fr) 2011-09-12 2013-03-21 Gea Mechanical Equipment Gmbh Procédé et installation de traitement de grignons pâteux d'olive
US9750276B2 (en) 2011-09-12 2017-09-05 Gea Mechanical Equipment Gmbh Method for processing wet olive pomace
EP2596707A1 (fr) * 2011-11-25 2013-05-29 Universita' Degli Studi di Bari Procédé et dispositif pour le conditionnement thermique d'olives ou d'autres fruits oléagineux, en combinaison avec un système de broyage et de malaxage desdits olives et d'autres fruits oléagineux, sous une atmospère controlée ou modifiée
WO2013076592A1 (fr) * 2011-11-25 2013-05-30 Università Degli Studi Di Bari Procédé et appareil pour le conditionnement thermique d'olives ou d'autres fruits oléagineux, combiné avec un système de broyage et de malaxage d'olives ou d'autres fruits oléagineux dans une atmosphère contrôlée ou modifiée
IT201800007016A1 (it) * 2018-07-06 2020-01-06 Gramolatrice per frantoio oleario e relativo metodo di funzionamento
WO2022200644A1 (fr) 2021-03-26 2022-09-29 Naranjo Lopez Rafael Procédé de production d'huile, produit d'huile et appareil de production d'huile
WO2023287271A1 (fr) * 2021-07-15 2023-01-19 Universidad Autónoma De Nayarit Procédé d'extrusion pour l'extraction d'huiles de la pulpe de fruits de persea spp.

Also Published As

Publication number Publication date
ATE305501T1 (de) 2005-10-15
EP1260571B1 (fr) 2005-09-28
PT1260571E (pt) 2005-11-30
EP1260571A3 (fr) 2004-01-07
DE50204364D1 (de) 2006-02-09
DE10123651A1 (de) 2002-11-28
ES2245999T3 (es) 2006-02-01

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