EP1717014A2 - Procédé et dispositif de pressage - Google Patents
Procédé et dispositif de pressage Download PDFInfo
- Publication number
- EP1717014A2 EP1717014A2 EP06003463A EP06003463A EP1717014A2 EP 1717014 A2 EP1717014 A2 EP 1717014A2 EP 06003463 A EP06003463 A EP 06003463A EP 06003463 A EP06003463 A EP 06003463A EP 1717014 A2 EP1717014 A2 EP 1717014A2
- Authority
- EP
- European Patent Office
- Prior art keywords
- extractant
- pressed material
- extract
- pressing
- 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.)
- Granted
Links
Images
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B30—PRESSES
- B30B—PRESSES IN GENERAL
- B30B9/00—Presses specially adapted for particular purposes
- B30B9/02—Presses specially adapted for particular purposes for squeezing-out liquid from liquid-containing material, e.g. juice from fruits, oil from oil-containing material
- B30B9/12—Presses specially adapted for particular purposes for squeezing-out liquid from liquid-containing material, e.g. juice from fruits, oil from oil-containing material using pressing worms or screws co-operating with a permeable casing
-
- 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
Definitions
- a predominant solution of the extractant in the extract with a small excess of extractant to provide a gas pressure is achieved in that the extractant is fed to the crop at most with a weight fraction which is 25 to 35% of the weight of the extract contained in the pressed material.
- the extractant is fed to the pressed material at a pressure of about 150 bar.
- Due to the friction energy generated by the mechanical pressing is usually a temperature range such that the pressing of the extract after the supply of the extractant is carried out at a temperature of about 40 to 45 degrees Celsius.
- a further increased extract yield can be achieved by subjecting the extract added with the extractant to at least two times an increase in pressure and a reduction in pressure.
- a cylinder interior (22) is subdivided into a pre-press zone (23), an extruder zone (24) and a press-off zone (25).
- the Vorpreßzone (23) is with a primary discharge for mechanically pressed Extract provided, in the area of the extruder zone (24) one or more secondary discharges (27) are provided for extractant mixed with the extract or for extractant dissolved in the extract.
- a discharge zone (28) is arranged adjacent to the solids discharge (10).
- the connection (21) for the supply of the extractant is typically located directly in the transport direction (11) behind a first throttle (6) which separates the pre-press zone (23) from the extruder zone (24).
- the storage tank (13) is designed for a pressure of up to 65 bar at an extractant temperature of 22 degrees.
- the cooler (14) also has a compressive strength up to about 65 bar and performs a temperature reduction to a temperature of about 15 to 18 degrees Celsius.
- the high-pressure pump (15) increases the pressure to a range of 150 to 300 bar, wherein a temperature increase to a temperature of 32 to 50 degrees Celsius occurs.
- About the heater (16) there is a further increase in temperature to a temperature of about 60 to 100 degrees Celsius.
- the screw press are fed as pressed material pre-crushed soybeans with an oil content of 18 to 20 percent and a water content of about 10 percent.
- the inlet temperature of the molding material is 20 degrees Celsius and it is a throughput of 100 kilos / hour provided.
- the liquid carbon dioxide is supplied to the screw press (1) at a rate of 15 kilos / hour at a temperature of 20 degrees Celsius.
- a temperature of 35 to 45 degrees Celsius sets along the transport path.
- the squeezed oil immediately after exiting the secondary discharge (27) has a temperature of about 70 degrees Celsius. Due to the combination of the mechanical pressing and the solution of the extractant in the extract and the resulting reduction in the viscosity, the solid discharged from the solids discharge (10) has a residual fat content of at most three percent by weight.
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Life Sciences & Earth Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Wood Science & Technology (AREA)
- Organic Chemistry (AREA)
- Mechanical Engineering (AREA)
- Extraction Or Liquid Replacement (AREA)
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| DE102005019294A DE102005019294A1 (de) | 2005-04-26 | 2005-04-26 | Verfahren und Vorrichtung zum Pressen |
Publications (3)
| Publication Number | Publication Date |
|---|---|
| EP1717014A2 true EP1717014A2 (fr) | 2006-11-02 |
| EP1717014A3 EP1717014A3 (fr) | 2008-09-17 |
| EP1717014B1 EP1717014B1 (fr) | 2017-05-03 |
Family
ID=36571424
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| EP06003463.4A Expired - Lifetime EP1717014B1 (fr) | 2005-04-26 | 2006-02-21 | Procédé et dispositif de pressage |
Country Status (5)
| Country | Link |
|---|---|
| US (1) | US20060283799A1 (fr) |
| EP (1) | EP1717014B1 (fr) |
| DE (1) | DE102005019294A1 (fr) |
| DK (1) | DK1717014T3 (fr) |
| RU (1) | RU2397870C2 (fr) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2008116457A1 (fr) * | 2007-03-28 | 2008-10-02 | Harburg-Freudenberger Maschinenbau Gmbh | Procédé et dispositif de pressage |
| CN115666917A (zh) * | 2020-05-20 | 2023-01-31 | 哈布尔格-弗罗伊登贝格尔机械工程有限公司 | 用于从种子获得油的方法和设备 |
Families Citing this family (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE102008052720B4 (de) * | 2008-10-22 | 2014-01-02 | British American Tobacco (Germany) Gmbh | Extraktive Tabakmaterial-Extrusion |
| JP4871437B1 (ja) * | 2011-01-24 | 2012-02-08 | アムコン株式会社 | 固液分離装置 |
| MX2014001263A (es) * | 2012-02-06 | 2014-11-10 | Dupps Co | Configuracion de eje de alta compresion y metodo relacionado para sistemas de prensa de tornillo usados en aplicaciones de extraccion de grasa. |
| FR3035565B1 (fr) * | 2015-04-30 | 2017-05-26 | Terrena | Procede et installation de trituration de graines d'oleagineux pour l'obtention d'huile et de tourteau |
| US11078176B2 (en) * | 2019-09-30 | 2021-08-03 | Socati Technologies - Oregon, Llc | Pubescent plant shallow moving bed solvent extractor and method of use |
| DE102021125760A1 (de) * | 2021-10-05 | 2023-04-06 | Harburg-Freudenberger Maschinenbau Gmbh | Verfahren und Vorrichtung zum Pressen |
| DE102022107203A1 (de) | 2022-03-28 | 2023-09-28 | Harburg-Freudenberger Maschinenbau Gmbh | Verfahren und Vorrichtung zur Bereitstellung von Kühl- und/oder Extraktionsmitteln für mindestens eine Presse sowie Vorrichtung zum Pressen |
| FR3137303A1 (fr) * | 2022-07-04 | 2024-01-05 | Ocp Sa | Procédé et système de séparation d’un solide et d’au moins un liquide d’une suspension |
Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5290959A (en) | 1985-09-10 | 1994-03-01 | Vitamins, Inc. | Mass separation of materials |
| WO1996033861A1 (fr) | 1995-04-27 | 1996-10-31 | Sucher & Holzer Bauplanungs- Und Handelsgesellschaft Mbh | Presse a vis |
| GB2343898A (en) | 1998-11-17 | 2000-05-24 | Express Separations Limited | Gas assisted press extraction of oil |
Family Cites Families (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE2335385B2 (de) * | 1973-07-12 | 1979-01-11 | Fried. Krupp Gmbh, 4300 Essen | Verfahren und Vorrichtung zur ölgewinnung aus gereinigten Ölfrüchten und ölsaaten |
| IL79838A0 (en) * | 1976-08-26 | 1986-11-30 | Vitamins Inc | Mass transfer extraction of liquids from solids |
| US4397231A (en) * | 1980-03-31 | 1983-08-09 | Burgin Kermit H | Apparatus for producing and collecting a liquid extract and a dry by-product from a mash |
| RU2077912C1 (ru) * | 1995-11-01 | 1997-04-27 | Российский заочный институт текстильной и легкой промышленности | Шнековый экстрактор для растительного сырья |
| NL1016198C2 (nl) * | 2000-09-15 | 2002-03-18 | Matheus Everardus Antonis | Inrichting voor het scheiden van een substantie in twee fasen. |
-
2005
- 2005-04-26 DE DE102005019294A patent/DE102005019294A1/de not_active Withdrawn
-
2006
- 2006-02-21 EP EP06003463.4A patent/EP1717014B1/fr not_active Expired - Lifetime
- 2006-02-21 DK DK06003463.4T patent/DK1717014T3/da active
- 2006-04-25 RU RU2006114169/02A patent/RU2397870C2/ru active
- 2006-04-26 US US11/412,708 patent/US20060283799A1/en not_active Abandoned
Patent Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5290959A (en) | 1985-09-10 | 1994-03-01 | Vitamins, Inc. | Mass separation of materials |
| WO1996033861A1 (fr) | 1995-04-27 | 1996-10-31 | Sucher & Holzer Bauplanungs- Und Handelsgesellschaft Mbh | Presse a vis |
| GB2343898A (en) | 1998-11-17 | 2000-05-24 | Express Separations Limited | Gas assisted press extraction of oil |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2008116457A1 (fr) * | 2007-03-28 | 2008-10-02 | Harburg-Freudenberger Maschinenbau Gmbh | Procédé et dispositif de pressage |
| CN115666917A (zh) * | 2020-05-20 | 2023-01-31 | 哈布尔格-弗罗伊登贝格尔机械工程有限公司 | 用于从种子获得油的方法和设备 |
| CN115666917B (zh) * | 2020-05-20 | 2026-01-02 | 哈布尔格-弗罗伊登贝格尔机械工程有限公司 | 用于从种子获得油的方法和设备 |
Also Published As
| Publication number | Publication date |
|---|---|
| RU2397870C2 (ru) | 2010-08-27 |
| EP1717014B1 (fr) | 2017-05-03 |
| RU2006114169A (ru) | 2007-11-20 |
| DE102005019294A1 (de) | 2006-11-09 |
| DK1717014T3 (da) | 2017-08-28 |
| US20060283799A1 (en) | 2006-12-21 |
| EP1717014A3 (fr) | 2008-09-17 |
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