EP1260571A2 - Process and plant for oil extraction from fruits and seeds - Google Patents
Process and plant for oil extraction from fruits and seeds Download PDFInfo
- 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
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- Prior art keywords
- pressure
- fruit pulp
- pressure section
- pulp
- seeds
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- 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
- C11B1/10—Production of fats or fatty oils from raw materials by extracting
-
- 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 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
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- 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)
Abstract
Description
Die Erfindung betrifft ein Verfahren zur Ölgewinnung aus Früchten oder Saaten, vorzugsweise Oliven oder Avocados, mit einer Vollmantel-Schneckenzentrifuge und eine Anlage zur Ölgewinnung nach dem Oberbegriff des Anspruches 29.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.
Ein gattungsgemäßes Verfahren und eine gattungsgemäße Anlage, welche sich bei der Olivenölgewinnung besonders bewährt haben, sind aus der EP 0 557 758 bekannt. Bei diesem Verfahren wird eine Zweiphasen-Trennung in einer Vollmantel-Schneckenzentrifuge durchgeführt, bei welcher das Öl als die eine Phase direkt von einem Feststoff-/Wassergemisch als der zweiten Phase abgetrennt wird.A generic method and a generic system, which are at have proven particularly useful in olive oil production are known from EP 0 557 758. This process involves a two-phase separation in a solid bowl screw centrifuge performed in which the oil as the one phase directly from a solid / water mixture is separated as the second phase.
Die Vorverarbeitung der Oliven erfolgt nach einem Waschen mittels eines Zerkleinerns in einer Mühle, welche die Oliven ohne den Zusatz von Wasser oder bei der Verwendung eingetrockneter Oliven unter einem Wasserzusatz, welcher den Frischwassergehalt frischer Oliven wieder herstellt, zu einem Fruchtbrei verarbeitet, welcher in einem der Mühle nachgeschalteten Malaxeur aufgeschlossen wird. Dieses Aufschließen im Malaxeur dient der Freisetzung des Öls, um es dann in der dem Malaxeur nachgeschalteten Vollmantel-Schneckenzentrifuge in die Bestandteile Öl sowie Feststoff und Wasser trennen zu können.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.
Die Effizienz dieses bekannten Verfahrens ist an sich bereits sehr gut. Dennoch ist es wünschenswert, alternative Lösungen der Vorverarbeitung des Fruchtbreis vor dem Eintritt in die Vollmantel-Schneckenzentrifuge zu schaffen und insbesondere den apparativen Aufwand zu senken, wobei die Qualität des Öls möglichst gut im Vergleich zum betriebenen apparativen Aufbau sein soll. Die Lösung dieses Problems in verfahrenstechnischer Hinsicht sowie auch in Hinsicht auf die Anlage zur Olivenölgewinnung ist die Aufgabe der Erfindung.The efficiency of this known method is in itself very good. Still is it is desirable to provide alternative solutions to preprocessing the pulp to create entry into the solid bowl screw centrifuge and in particular to reduce the expenditure on equipment, the quality of the oil being as good as possible Should be compared to the operated apparatus structure. The solution to this problem in procedural terms as well as in terms of the plant for Olive oil production is the object of the invention.
Die Erfindung löst diese Aufgabe einerseits durch ein Verfahren zur Ölgewinnung,
welches im Merkmal 1 angegeben ist. Sie löst es ferner durch eine Anlage zur Ölgewinnung,
deren Merkmale im Anspruch 29 angegeben sind.The invention solves this problem on the one hand by a method for oil production,
which is specified in
Mit der Erfindung werden die Früchte oder Saaten zerkleinert und beim oder nach dem Zerkleinern einem Hochdruck und einem nachfolgenden Entspannen ausgesetzt, woraufhin der zerkleinerte Fruchtbrei der Vollmantel-Schneckenzentrifuge zugeführt wird.With the invention, 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.
Die Erfindung schafft ferner eine Anlage zur Ölgewinnung aus Früchten oder Saaten, vorzugsweise Oliven oder Avocados, mit einer Einrichtung zum Zerkleinern der Früchte oder Saaten zu einem Fruchtbrei, vorzugsweise eine Mühle oder ein Extruder, einer der Einrichtung zum Zerkleinern zugeordneten - z.B. beim Einsatzeines Extruders - oder nachgeschalteten Hochdruckstrecke zum Aufschließen des Fruchtbreis, und einer der Hochdruckstrecke nachgeschalteten Vollmantel-Schneckenzentrifuge, vorzugsweise mit einer Tauchscheibe versehen, zur Trennung des Fruchtbreis in verschiedene Phasen, vorzugsweise in Öl als erste Phase und in ein Feststoff-/Wassergemisch als zweite Phase. 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.
Bei dem erfindungsgemäßen Verfahren sowie bei der erfindungsgemäßen Anlage wird also jeweils der bisher notwendige Malaxeur zum Aufschließen des Fruchtbreis dadurch ersetzt, daß der Fruchtbrei beim oder vorzugsweise nach dem Zerkleinern dem Hochdruck und dem nachfolgenden Entspannen ausgesetzt wird. Denkbar ist es beispielsweise, direkt einen Extruder zum Zerkleinern und den im Extruder herrschenden Druck und ein nachfolgendes Entspannen zum Aufschließen der Früchte oder Saaten zu nutzen. Alternativ ist auch ein Zerkleinern in einer Mühle denkbar, wobei entweder in der Mühle oder vorzugsweise nach dem Durchlaufen der Mühle die Hochdruckstrecke durchlaufen wird.In the method according to the invention and in the system according to the invention each time the malaxeur necessary to unlock the pulp becomes replaced by the fruit pulp during or preferably after chopping is exposed to the high pressure and the subsequent relaxation. For example, it is conceivable to directly use an extruder for shredding and the Extruder prevailing pressure and a subsequent relaxation to unlock the fruit or seeds. Alternatively, crushing in one Mill conceivable, either in the mill or preferably after passing through the mill will go through the high pressure section.
Ein besonderer Vorteil der Erfindung ist darin zu sehen, daß die Vorverarbeitung des Fruchtbreis beim Ersetzen des Malaxeurs durch eine Hochdruckstrecke relativ schnell erfolgen kann. So hat es sich herausgestellt, daß beispielsweise eine Verweilzeit von nur 6 Minuten in der Hochdruckstrecke schon ausreichen kann, um die Oliven genügend aufzuschließen, um sie in der Vollmantel-Schneckenzentrifuge weiter verarbeiten zu können. Die Qualität des Öles ist dabei mit der bei der Verarbeitung mit einem Malaxeur erzielbaren Qualität vergleichbar oder sogar besser. Neben Oliven sind insbesondere auch Avocados besonders gut mit dem erfindungsgemäßen Verfahren verarbeitbar.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. In addition to olives, avocados in particular are particularly good with the invention Processable.
Zur Realisierung der Hochdruckstrecke mit einer Hochdruckzone und dem Entspannungsventil stehen dem Fachmann verschiedenste Möglichkeiten zur Verfügung.To implement the high pressure line with a high pressure zone and the relief valve Various possibilities are available to the expert.
So kann die Hochdruckstrecke ein Rohr - mit vorgeschalteter entsprechend ausgelegter Pumpeinrichtung - aurweisen, welches eine Länge von mehr als 10, vorzugsweise eine Länge von 10 bis 30 Metern aufweist.For example, 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.
Zur leichteren Verarbeitung bzw. zum leichteren Aufschließen des Fruchtbreis ist es ferner denkbar, daß der Fruchtbrei vor dem Eintritt in die Hochdruckstrecke und/oder beim Durchlaufen der Hochdruckstrecke - mittels einer Heizeinrichtungerwärmt wird. Bei der Verarbeitung von Oliven wird der Fruchtbrei vorzugsweise auf max. 40°C erwärmt und bei der Verarbeitung von Avocados auf mehr als 40°C, insbesondere 40° - 80°C.It is for easier processing or for easier opening of the pulp also conceivable that 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. When processing olives, the fruit pulp is preferred to max. Heated to 40 ° C and when processing avocados to more than 40 ° C, especially 40 ° - 80 ° C.
Vorzugsweise beträgt die Verweildauer des Fruchtbreis in der Hochdruckstrecke 2 bis 12, insbesondere 4 bis 8 Minuten.The residence time of the fruit pulp in the high-pressure section is preferably 2 to 12, especially 4 to 8 minutes.
Es hat sich ferner als vorteilhaft herausgestellt, wenn der Druck in der Hochdruckstrecke mehr als 10 bar, vorzugsweise mehr als 30 bar, insbesondere mehr als 50 bar beträgt. Ganz besonders bevorzugt wird ein Druck zwischen 50 und 80 und noch spezieller zwischen 60 und 70 bar gewählt. So konnte bei Verwendung eines relativ hohen Druckes kann die Verweildauer in der Hochdruckstrecke auf 6 min gesenkt werden.It has also proven to be advantageous if 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.
Vor dem Eintritt in die Hochdruckstrecke werden die Früchte oder Saaten vorzugsweise zunächst gewaschen und dann zerkleinert, vorzugsweise in einer Mühle, insbesondere in einer Hammermühle.Before entering the high-pressure line, the fruits or seeds are preferred first washed and then crushed, preferably in a mill, in particular in a hammer mill.
Es ist denkbar, daß der Fruchtbrei nach dem Zerkleinern direkt und/oder aus dem ersten Puffertank über mindestens eine Pumpe in die Hochdruckstrecke geleitet wird.It is conceivable that the pulp directly after chopping and / or from the first buffer tank via at least one pump in the high pressure line becomes.
Vorzugsweise wird der Fruchtbrei aus der Hochdruckstrecke kommend mit Hilfe eines Entspannungsventils entspannt und dann direkt und/oder nach weiterer Entspannung in einem weiteren Puffertank der Vollmantel-Schneckenzentrifuge zugeleitet wird.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.
Denkbar ist schließlich, die Verarbeitung des Fruchtbreis in einem hermetischen System durchzuführen, ggf. unter Zuführung eines Inertgases.Finally, it is conceivable to process the pulp in a hermetic manner System, if necessary with the supply of an inert gas.
Zusammenfassend ist festzustellen, daß mit dem Ersetzen des Malaxeurs durch eine Hochdruckstrecke eine Alternative zur Vorverarbeitung in einem Malaxeur geschaffen wird, welche den apparativen Aufwand und insbesondere die Verarbeitungszeit von der ungewaschenen Olive bis zur Herstellung des Öls deutlich verringert. So ist es beispielsweise möglich, in nur 30 Minuten aus Oliven oder Avocados ein fertiges Öl herzustellen. Gegebenenfalls kann das aus der Vollmantel-Schneckenzentrifuge austretende Öl in einem Klärseparator - ggf. unter der Zugabe einiger Gewichtsprozente an Wasser - gereinigt werden.In summary, it can be said that with the replacement of the malaxer with a High pressure path created an alternative to preprocessing in a malaxeur which is the expenditure on equipment and in particular the processing time from the unwashed olive to the production of the oil. So is For example, it is possible to make a ready-made olive or avocado in just 30 minutes To produce oil. If necessary, this can be done from the solid bowl screw centrifuge escaping oil in a clarifier - if necessary with the addition of a few percent by weight in water - to be cleaned.
Weitere vorteilhafte Ausgestaltungen sind den übrigen Unteransprüchen zu entnehmen.Further advantageous embodiments can be found in the remaining subclaims.
Nachfolgend werden Ausführungsbeispiele anhand der Zeichnung erläutert.Exemplary embodiments are explained below with reference to the drawing.
- Figur 1Figure 1
- ein Flußdiagramm eines Verfahrens zur Olivenölgewinnung,a flow diagram of a method for olive oil production,
- Figur 2Figure 2
- ein Flußdiagramm eines zweiten Verfahrens zur Olivenölgewinnung,2 shows a flow diagram of a second method for extracting olive oil,
- Figur 3Figure 3
- ein Flußdiagramm eines dritten Verfahrens zur Olivenölgewinnung, und3 shows a flow diagram of a third method for extracting olive oil, and
- Figur 4Figure 4
- eine Tabelle, welche Versuchsergebnisse der Ölgewinnung mit dem erfindungsgemäßen Verfahren wiedergibt.a table which test results of the oil production with the reproduces method according to the invention.
Nach Figur 1 werden die gewaschenen Oliven zunächst einer Mühle 1 (z.B. Hammermühle) zugeführt. Den Oliven wird dabei kein Wasser zugesetzt, sofern frische Oliven verarbeitet werden. Lediglich bei der Verarbeitung eingetrockneter Oliven wird den Oliven so viel Wasser zugesetzt, daß der natürliche Wassergehalt frischer Oliven wieder hergestellt wird.According to Figure 1, 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.
Vorzugsweise mit einer Pumpe 2 werden die Oliven sodann von der Mühle 1 über
eine Rohrleitung 3 einem ersten Puffertank 4 zugeleitet. Der erste Puffertank 4 erleichtert
das stabile Betreiben der Anlage. Alternativ ist es aber auch denkbar, den
Puffertank 4 fortzulassen und den in der Mühle hergestellten Fruchtbrei direkt über
eine oder mehrere Pumpen (Speisepumpe 5, dieser nachgeschaltete Kolbenpumpe
6) einer Hochdruckstrecke 7 zuzuleiten. Die Hochdruckstrecke 7 umfaßt die Druckzone
7a und das Entspannungsventil 7b. Die Druckzone 7a kann beispielsweise als
einfache Rohrleitung ausgelegt sein oder als sonstiger Homogenisator.The olives are then transferred from the
Die Hochdruckstrecke 7 ist derart auszulegen, daß in der Druckzone 7a und mittels
der nachfolgenden Entspannung mit einem Entspannungsventil 7b ein genügendes
Aufschließen des Fruchtbreis bzw. ein Freisetzen des Öls erfolgt. Hierzu wird vorzugsweise
in der Hochdruckstrecke 7 ein Druck von mehr als 50 bar erzeugt und die
Hochdruckstrecke 7 bzw. die Förderleistung wird derart ausgelegt, daß die Verweildauer
des Fruchtbreis in der Hochdruckstrecke vorzugsweise 2 bis 12, insbesondere
4 bis 8 Minuten beträgt. Besonders gute Ergebnisse wurden bei einem
Verweilen des Fruchtbreis in der Hochdruckstrecke bei 6 Minuten erreicht.The
Besonders vorteilhaft ist es, wenn der Fruchtbrei - z.B. im Puffertank 4 - mittels einer hier nicht dargestellten Heizeinrichtung erwärmt wird. Die Temperatur des Fruchtbreis sollte jedoch nicht mehr als 40 °C betragen (Herstellung eines hochwertigen Olivenöls). Vorzugsweise wird der Fruchtbrei im Puffertank auf 30 °C erwärmt. Denkbar ist auch eine Erwärmung direkt beim Durchtreten der Hochdruckstrecke. Bei der Verarbeitung anderer Produkte wie Avocados ist auch eine Erwärmung auf mehr als 40° C - insbesondere 40 - 80° C) denkbar.It is particularly advantageous if the fruit pulp - e.g. in the buffer tank 4 - by means of a heating device, not shown here, is heated. 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.
Aus der Hochdruckstrecke 7 wird der Fruchtbrei entweder direkt oder aber beispielsweise
über einen weiteren, vorzugsweise beheizbaren Puffertank 8 und/oder
eine Speisepumpe 9 dem Zulauf 10 einer Vollmantel-Schneckenzentrifuge (in der
Zeichnung kurz "VS-Zentrifuge") 11 zugeführt.From the high-
Nach einer besonders vorteilhaften Variante der Erfindung wird diese derart eingestellt, daß in der Vollmantel Schneckenzentrifuge direkt eine Auftrennung des aufgeschlossenen Fruchtbreis in eine erste Phase Öl (Trüböl) und in eine zweite Phase Orujo (Wasser-Feststoff-Gemisch) erfolgt. Denkbar ist aber auch eine Drei-Phasenverarbeitung unter dem Zusatz von Wasser. According to a particularly advantageous variant of the invention, it is set in such a way that that in the solid bowl screw centrifuge directly a separation of the digested Fruit pulp in a first phase of oil (cloudy oil) and in a second phase Orujo (water-solid mixture) takes place. However, three-phase processing is also conceivable with the addition of water.
Fig. 2 reduziert das Verfahren auf nur wenige Schritte. Nach dem Zerkleinern in der
Mühle 1 und dem Durchtreten der Pumpe 2 erfolgt direkt in der aus der Druckzone
7a und dem Entspannungsventil 7b bestehenden Hochdruckstrecke 7 das Aufschließen
der Oliven vor deren Eintritt in die Vollmantel-Schneckenzentrifuge 11, welche
den eintretenden Brei in Öl und Orujo (Wasser-/Feststoffgemisch) auftrennt.2 reduces the method to just a few steps. After crushing in the
Nach Fig. 3 wird das Zerkleinern des Fruchtbreis mittels eines Extruders 12 durchgeführt,
in dem ein gegenüber der Umgebung erhöhter Druck herrscht, so daß der
Extruder 12 selbst die Hochdruckstrecke 7 ausbildet. Aus dem Extruder 12 wird der
aufgeschlossene Fruchtbrei dann direkt oder über einen oder mehrere Puffer 4
und/oder eine Speisepumpe 5 in die Vollmantel-Schneckenzentrifuge geleitet.3, the pulp is crushed by means of an
Die Versuchstabelle der Fig. 4 veranschaulicht, daß es mit dem erfindungsgemäßen Verfahren ohne weiteres möglich ist, ein Olivenöl herzustellen, wobei insbesondere zu bedenken, ist, daß der apparative Aufwand im Vergleich zum Einsatz eines Malaxeurs deutlich verringert wird. Wie zu erkennen, verringert sich mit zunehmender Temperatur der Restölgehalt im Orujo. Die Versuche zu Fig. 4 wurden mit einem Aufbau durchgeführt, der dem der Fig. 1 entspricht 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
- 11
- Hammermühlehammer mill
- 22
- Pumpepump
- 33
- Rohrleitungpipeline
- 44
- Puffertankbuffer tank
- 55
- Speisepumpefeed pump
- 66
- Kolbenpumpepiston pump
- 77
- Druckstreckepressure range
- 7a7a
- Druckzonepressure zone
- 7b7b
- Entspannungsventilexpansion valve
- 88th
- Puffertankbuffer tank
- 99
- Speisepumpefeed pump
- 1010
- ZulaufIntake
- 1111
- Vollmantel-SehneckenzentrifugeSolid bowl centrifuge Sehn corner
- 1212
- Extruderextruder
Claims (30)
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE10123651 | 2001-05-15 | ||
DE10123651A DE10123651A1 (en) | 2001-05-15 | 2001-05-15 | Process and plant for extracting oil from fruit or seeds |
Publications (3)
Publication Number | Publication Date |
---|---|
EP1260571A2 true EP1260571A2 (en) | 2002-11-27 |
EP1260571A3 EP1260571A3 (en) | 2004-01-07 |
EP1260571B1 EP1260571B1 (en) | 2005-09-28 |
Family
ID=7684886
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP02008998A Expired - Lifetime EP1260571B1 (en) | 2001-05-15 | 2002-04-23 | Process and plant for oil extraction from fruits and seeds |
Country Status (5)
Country | Link |
---|---|
EP (1) | EP1260571B1 (en) |
AT (1) | ATE305501T1 (en) |
DE (2) | DE10123651A1 (en) |
ES (1) | ES2245999T3 (en) |
PT (1) | PT1260571E (en) |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE102011053527A1 (en) | 2011-09-12 | 2013-03-14 | Gea Mechanical Equipment Gmbh | Process and plant for processing Alpeorujo |
EP2596707A1 (en) * | 2011-11-25 | 2013-05-29 | Universita' Degli Studi di Bari | Method and apparatus for thermal conditioning of olives or other oleaginous fruits combined with a crushing and kneading system of olives or other oleaginous fruits in controlled or modified atmosphere |
IT201800007016A1 (en) * | 2018-07-06 | 2020-01-06 | Kneading machine for oil mill and its operating method | |
WO2022200644A1 (en) | 2021-03-26 | 2022-09-29 | Naranjo Lopez Rafael | Process for producing oil, oil product, and oil production apparatus |
WO2023287271A1 (en) * | 2021-07-15 | 2023-01-19 | Universidad Autónoma De Nayarit | Extrusion method for extracting oils from persea spp. fruit pulp |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GR1010263B (en) * | 2021-04-08 | 2022-07-06 | Στυλιανος Ιωαννη Τζανακακης | Production of nutritional low oil-content pulps and pastes with a hybridisation method combining the cold-pressure direct hydraulic paste-making method with the two--phase centrifugal oil-making separation method |
Citations (7)
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 |
US4132161A (en) * | 1976-07-16 | 1979-01-02 | Helwig E | Device and process for separating the liquid part from the solid part of seeds and fruit |
FR2442716A1 (en) * | 1978-11-28 | 1980-06-27 | Blanie Paul | Extracting natural or synthetic substances - by subjecting them to successive phases of pressure increase and decompression |
DE3021083A1 (en) * | 1980-06-04 | 1981-12-10 | Gefi Gesellschaft für Industriewärme und Verfahrenstechnik mbH, 4150 Krefeld | Loose material disintegration process by high pressure - involves pressurising with subsequent sudden pressure reducing to above-atmospheric |
US4794011A (en) * | 1985-08-14 | 1988-12-27 | Schumacher Heinz | Process for the treatment of vegetable raw materials |
EP0557758A1 (en) * | 1992-02-27 | 1993-09-01 | Westfalia Separator AG | Process for producing olive oil |
WO2002089992A1 (en) * | 2001-05-03 | 2002-11-14 | Westfalia Separator Ag | Solid bowl spiral centrifuge and a method for obtaining oil using a solid bowl spiral centrifuge |
-
2001
- 2001-05-15 DE DE10123651A patent/DE10123651A1/en not_active Withdrawn
-
2002
- 2002-04-23 EP EP02008998A patent/EP1260571B1/en not_active Expired - Lifetime
- 2002-04-23 DE DE50204364T patent/DE50204364D1/en not_active Expired - Lifetime
- 2002-04-23 AT AT02008998T patent/ATE305501T1/en not_active IP Right Cessation
- 2002-04-23 ES ES02008998T patent/ES2245999T3/en not_active Expired - Lifetime
- 2002-04-23 PT PT02008998T patent/PT1260571E/en unknown
Patent Citations (7)
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 |
US4132161A (en) * | 1976-07-16 | 1979-01-02 | Helwig E | Device and process for separating the liquid part from the solid part of seeds and fruit |
FR2442716A1 (en) * | 1978-11-28 | 1980-06-27 | Blanie Paul | Extracting natural or synthetic substances - by subjecting them to successive phases of pressure increase and decompression |
DE3021083A1 (en) * | 1980-06-04 | 1981-12-10 | Gefi Gesellschaft für Industriewärme und Verfahrenstechnik mbH, 4150 Krefeld | Loose material disintegration process by high pressure - involves pressurising with subsequent sudden pressure reducing to above-atmospheric |
US4794011A (en) * | 1985-08-14 | 1988-12-27 | Schumacher Heinz | Process for the treatment of vegetable raw materials |
EP0557758A1 (en) * | 1992-02-27 | 1993-09-01 | Westfalia Separator AG | Process for producing olive oil |
WO2002089992A1 (en) * | 2001-05-03 | 2002-11-14 | Westfalia Separator Ag | Solid bowl spiral centrifuge and a method for obtaining oil using a solid bowl spiral centrifuge |
Cited By (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE102011053527A1 (en) | 2011-09-12 | 2013-03-14 | Gea Mechanical Equipment Gmbh | Process and plant for processing Alpeorujo |
WO2013037751A1 (en) | 2011-09-12 | 2013-03-21 | Gea Mechanical Equipment Gmbh | Method and plant for processing wet olive pomace |
US9750276B2 (en) | 2011-09-12 | 2017-09-05 | Gea Mechanical Equipment Gmbh | Method for processing wet olive pomace |
EP2596707A1 (en) * | 2011-11-25 | 2013-05-29 | Universita' Degli Studi di Bari | Method and apparatus for thermal conditioning of olives or other oleaginous fruits combined with a crushing and kneading system of olives or other oleaginous fruits in controlled or modified atmosphere |
WO2013076592A1 (en) * | 2011-11-25 | 2013-05-30 | Università Degli Studi Di Bari | Method and apparatus for thermal conditioning of olives or other oleaginous fruits combined with a crushing and kneading system of olives or other oleaginous fruits in controlled or modified atmosphere |
IT201800007016A1 (en) * | 2018-07-06 | 2020-01-06 | Kneading machine for oil mill and its operating method | |
WO2022200644A1 (en) | 2021-03-26 | 2022-09-29 | Naranjo Lopez Rafael | Process for producing oil, oil product, and oil production apparatus |
WO2023287271A1 (en) * | 2021-07-15 | 2023-01-19 | Universidad Autónoma De Nayarit | Extrusion method for extracting oils from persea spp. fruit pulp |
Also Published As
Publication number | Publication date |
---|---|
ES2245999T3 (en) | 2006-02-01 |
DE10123651A1 (en) | 2002-11-28 |
ATE305501T1 (en) | 2005-10-15 |
EP1260571B1 (en) | 2005-09-28 |
PT1260571E (en) | 2005-11-30 |
EP1260571A3 (en) | 2004-01-07 |
DE50204364D1 (en) | 2006-02-09 |
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