EP0704248A1 - Procédé et dispositif pour l'extraction centrifuge d'huile de premier et second pressages - Google Patents
Procédé et dispositif pour l'extraction centrifuge d'huile de premier et second pressages Download PDFInfo
- Publication number
- EP0704248A1 EP0704248A1 EP95202424A EP95202424A EP0704248A1 EP 0704248 A1 EP0704248 A1 EP 0704248A1 EP 95202424 A EP95202424 A EP 95202424A EP 95202424 A EP95202424 A EP 95202424A EP 0704248 A1 EP0704248 A1 EP 0704248A1
- Authority
- EP
- European Patent Office
- Prior art keywords
- radial
- centrifugal extractor
- oil
- fluid component
- component
- 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
- 238000003825 pressing Methods 0.000 title claims abstract description 21
- 238000000605 extraction Methods 0.000 title claims abstract description 20
- 238000000034 method Methods 0.000 title claims abstract description 17
- 239000003921 oil Substances 0.000 claims abstract description 56
- 239000012530 fluid Substances 0.000 claims abstract description 42
- 239000007787 solid Substances 0.000 claims abstract description 31
- 238000000926 separation method Methods 0.000 claims abstract description 15
- 230000014759 maintenance of location Effects 0.000 claims abstract description 8
- 238000005119 centrifugation Methods 0.000 claims abstract description 6
- 230000000717 retained effect Effects 0.000 claims abstract description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 16
- 238000007789 sealing Methods 0.000 claims 1
- 240000007817 Olea europaea Species 0.000 description 6
- 238000013517 stratification Methods 0.000 description 5
- 238000011084 recovery Methods 0.000 description 4
- 241000207836 Olea <angiosperm> Species 0.000 description 3
- 230000004888 barrier function Effects 0.000 description 2
- 230000005484 gravity Effects 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 238000000819 phase cycle Methods 0.000 description 2
- 239000002699 waste material Substances 0.000 description 2
- 230000001133 acceleration Effects 0.000 description 1
- 238000005352 clarification Methods 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
Images
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
- C11B1/06—Production of fats or fatty oils from raw materials by pressing
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B04—CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
- B04B—CENTRIFUGES
- B04B1/00—Centrifuges with rotary bowls provided with solid jackets for separating predominantly liquid mixtures with or without solid particles
- B04B1/20—Centrifuges with rotary bowls provided with solid jackets for separating predominantly liquid mixtures with or without solid particles discharging solid particles from the bowl by a conveying screw coaxial with the bowl axis and rotating relatively to the bowl
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B04—CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
- B04B—CENTRIFUGES
- B04B1/00—Centrifuges with rotary bowls provided with solid jackets for separating predominantly liquid mixtures with or without solid particles
- B04B1/20—Centrifuges with rotary bowls provided with solid jackets for separating predominantly liquid mixtures with or without solid particles discharging solid particles from the bowl by a conveying screw coaxial with the bowl axis and rotating relatively to the bowl
- B04B2001/2041—Centrifuges with rotary bowls provided with solid jackets for separating predominantly liquid mixtures with or without solid particles discharging solid particles from the bowl by a conveying screw coaxial with the bowl axis and rotating relatively to the bowl with baffles, plates, vanes or discs attached to the conveying screw
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B04—CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
- B04B—CENTRIFUGES
- B04B1/00—Centrifuges with rotary bowls provided with solid jackets for separating predominantly liquid mixtures with or without solid particles
- B04B1/20—Centrifuges with rotary bowls provided with solid jackets for separating predominantly liquid mixtures with or without solid particles discharging solid particles from the bowl by a conveying screw coaxial with the bowl axis and rotating relatively to the bowl
- B04B2001/2083—Configuration of liquid outlets
Definitions
- the object of this invention is a process for the drawing of quantities of oil of different qualities by means of a centrifugal extractor and an appropriate centrifugal extractor capable of performing such differentiated extraction.
- centrifugal extractors substantially comprising a scroll fitted inside a rotary drum and rotating in turn relative to the latter, which effect within the drum the separation and stratification of the various components of the product which is comprised of a solid part and two fluid parts of varying specific gravity.
- the product to be separated comprises a substantially solid part, known as olive residue, which constitutes the waste; a first heavier fluid part, substantially consisting of water, which is also considered as waste; and a second, lighter fluid part substantially consisting of oil which forms the valuable part to be separated and recovered independently of the other two.
- centrifugal separating machines of known type the product to be separated is normally fed to the machine in the form of crushed pulp with added water which, in the centrifugation phase becomes disposed radially to increase an intermediate separating layer between the solid and the oil, thereby bringing about improved separation of the oily component from the solid component.
- the first oil to flow out is that extracted from the oil-bearing cell which, being already agglomerated, is readily extractable, while the last oil obtained from pressing is that located in the interstice between one cell and another, which is less mature and therefore of inferior quality.
- the solid bottom residue on flowing out of the centrifuge, carries with it part of such valuable fluid component with a consequent reduction of yield and/or the need for a subsequent additional recovery operation, as well as part of the heavy fluid component which makes it necessary to maintain the product at a low level within the drum to enable the solid residue to drain to the greatest possible extent from the valuable component prior to flowing out of the extractor.
- a further aim of this invention is the provision of a centrifugal extractor for products consisting of several components of varying specific gravity which make it possible to reduce to a minimum the quantity of valuable lighter fluid component flowing out of the separator together with the solid residue and to achieve at the same time the direct drawing of oils of different qualities including direct drawing of the oil of second or third choice which is normally lost with the residue, or recovered by subsequent separating operations applied to the said solid residue.
- a further aim of the invention is to provide centrifuging systems capable of performing differentiated extraction of oils of different qualities.
- a centrifugal extractor is essentially comprised of a fixed, substantially cylindrical casing 1, provided at its opposite ends with annular sections separated from one another and opening downward, forming radial collectors 1a, 1b, 1c for the recovery of the different components of the product to be separated which, in the particular case of processing of olives, are formed respectively by solid residue, known as olive residue, heavy fluid residue, consisting of water, and oil.
- a rotary hollow drum 2 of substantially cylindrical-truncated cone shape, which is mounted on bearings 2a to enable it to rotate relative to casing 1, the drive for the said drum being of conventional type and therefore not shown in detail.
- Such scroll 4 is substantially comprised of a hollow cylindrical-truncated cone body on which are formed outflow apertures for product 5 fed into it, in the direction of arrow P, by means of a pump, not shown, and a coaxial duct 5a.
- a helix 4b which, on rotating in the direction opposite that of the drum, forces the solid residue to flow toward appropriate outlet 1a.
- tube 5a concentrically to tube 5a is located a further tube 105 for the supply of water to the extractor.
- Such water flows under pressure from holes or nozzles 105a and brings about fluid stratification which tends to promote a cleaner separation between the oil and the olive residue in the water outflow zone.
- Front wall 2b of drum 2 has three pairs of holes, the first two pairs 6 and 7 of which are respectively located according to diameters perpendicular to one another, with different circumferences concentric to one another, and the third pair 8 is located according to a diameter forming an angle of 45° relative to the other two and a circumference with a radius smaller than that of the two pairs of holes 6 and 7.
- the two pairs of holes 6 and 7 are located at a greater distance from the axis of rotation of scroll 4 and drum 2 than that of the third pair of holes 8, which are therefore closer to such axis of rotation.
- holes 6 are associated with an outflow duct 6a ending in radial collector 1b where the lighter fluid component is collected, while holes 7 are associated with an inverted overfall duct 7a ending in radial collector 1c where the heavier component of product 5 is collected.
- Holes 6 are furthermore closed in the axial direction by plugs 6b shaped with extensions 6c in order to bring about the opening or closure of duct 6a following the rotation of plug 6b in one direction or the other, thereby bringing about, in one case, the outflow of water on its own via hole 6 or, in the other case, the outflow of water together with the solid residue via opposite collector 1a.
- the extractor operates with only two outlets (figs. 5 and 6): one 8 for the oil and one 1a for the olive residue and water.
- a disc 9 provided with a concentric circular aperture having diametrically opposed, substantially rectangular slots 9a, capable of bringing about the opening of ducts 8 for the outflow of the light fluid component, in the case of an extractor having only two outlets.
- the scroll of the centrifuge according to the invention is completed by a disc 11 or like solid piece fitted concentrically to said scroll 4.
- the outside diameter of such disc is greater than the diameter of the circumference on which are located holes 8, so that the disc constitutes a barrier for separation in an axial direction of the oil of first pressing, which is forced into the drawing zone in an axial direction via such holes 8.
- the centrifugal extractor according to the invention also provides further means for drawing the lighter fluid component in a radial direction, consisting of tubular pieces 12 inserted radially into drum 2 via holes 2d thereof, in such a way as to emerge at a point axially posterior to disc 11 in the direction of flow of the solid towards its own outlet 1a.
- Such tubular pieces 12 have an inner end 12a located in relation to the level of stratification of the fluid component which it is required to collect, while opposite end 12b, located outside drum 2, flows into a collector 101 within fixed casing 1.
- Such collector makes it possible to convey the drawn fluid toward duct 101a for the outflow and collection of the said fluid.
- tubular pieces provision is also made for such tubular pieces to be located on the circumference of the drum in positions such as to maintain the dynamic balance of the separator during rotation. Furthermore, although the inclination of the tubular pieces with respect to the surface of drum 2 may be at any angle, it is obvious that the arrangement of radial tubes makes it possible to utilize the full centrifugal force determined by the rotary movement for the extraction of the oil in a radial direction.
- the operation of the device is as follows: whether it is desired to process the product according to a so-called two-phase cycle (that is, with a single axial outflow of the valuable fluid and a single outlet for the intermixed solid residues and fluid), (fig. 5), or whether it is desired to process the product according to a so-called three-phase cycle (that is, with separate outflows of oil, water and solid), (fig. 2), there is brought about via disc 9 the opening or closure of the various extraction ducts from wall 2b, so that, as shown in fig.
- Such radial drawing therefore reduces the quantity of oil which flows out with the residue, thereby increasing the overall output of the centrifugal extractor.
- Such radially recovered oil constitutes the so-called oil of second pressing, i.e. that which requires longer centrifugation time in order to become separated from the oily pulp and which therefore, by not emerging rapidly, cannot be extracted axially to avoid reducing the quality of the oil of first pressing.
- centrifugal extractor may be extended to processing with a liquid ring of thick section (fig. 5) and to the production of olive residue with a high moisture content.
- the outlets in this case would be three in number, because of the presence of the new radial outlet.
- annular zone of containment of the valuable fluid of second pressing which, in addition to being maintained more steady with respect to the direct current flow toward the outlet of the solid, may be better purged of the occurrence of any residues of water and solids still suspended in the oil.
- Each radial drawing corresponds to a well-defined quality of oil which, if drawn via corresponding collectors 101 independent of one another, may be maintained separate.
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)
- Extraction Or Liquid Replacement (AREA)
- Fats And Perfumes (AREA)
- Centrifugal Separators (AREA)
Applications Claiming Priority (4)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| ITMI941985A IT1270102B (it) | 1994-09-29 | 1994-09-29 | Procedimento per l'estrazione di olio di prima e seconda spremitura mediante separatore centrifugo orizzontale e relativo separatore |
| ITMI941985 | 1994-09-29 | ||
| ITMI951564 | 1995-07-20 | ||
| ITMI951564 IT1275574B (it) | 1995-07-20 | 1995-07-20 | Procedimento per l'estrazione di olio di prima e seconda spremitura mediante estrattore centrifugo orizzontale e relativo estrattore |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| EP0704248A1 true EP0704248A1 (fr) | 1996-04-03 |
| EP0704248B1 EP0704248B1 (fr) | 1997-12-17 |
Family
ID=26331191
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| EP95202424A Expired - Lifetime EP0704248B1 (fr) | 1994-09-29 | 1995-09-07 | Procédé et dispositif pour l'extraction centrifuge d'huile de premier et second pressages |
Country Status (5)
| Country | Link |
|---|---|
| EP (1) | EP0704248B1 (fr) |
| ES (1) | ES2091735T3 (fr) |
| GR (1) | GR3025834T3 (fr) |
| TN (1) | TNSN95096A1 (fr) |
| TR (1) | TR199501176A2 (fr) |
Cited By (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP0785029A1 (fr) * | 1996-01-18 | 1997-07-23 | RAPANELLI FIORAVANTE S.p.A. | Centrifugeuse horizontale pour l'extraction optimale d'huile |
| EP0845296A1 (fr) * | 1996-10-18 | 1998-06-03 | Gennaretti S.p.A. | Centrifugeuse horizontale pour l'extraction d'huile de mélanges oléagineux |
| GR990100394A (el) * | 1998-11-16 | 2000-07-31 | Nuova M.A.I.P. Macchine Agricole Industriali Pieralisi S.P.A. | Συσκευη για τη φυγοκεντρικη εκχυλιση υγρων συστατικων απο ελαιοφορα προιοντα και παρομοια, εφοδιασμενη με μεσα για την ακτινικη εκχυλιση του υγρου συστατικου με μεγαλυτερο ειδικο βαρος |
| GR20000100113A (el) * | 1999-04-06 | 2000-12-29 | Nuova M.A.I.P. Macchine Agricole Industriali Pieralisi S.P.A. | Μεθοδος ληψεως ελαιου απο ελαιοφορα προιοντα και παρομοια με τη βοηθεια φυγοκεντρισεως με διαχωρισμο του στερεου συστατικου σε δυο μερη, και αντιστοιχη εγκατασταση |
| WO2002089992A1 (fr) * | 2001-05-03 | 2002-11-14 | Westfalia Separator Ag | Centrifugeuse a vis a paroi pleine et procede d'extraction d'huile a l'aide d'une centrifugeuse a vis a paroi pleine |
| GR20020100162A (el) * | 2001-04-12 | 2002-12-19 | Nuova M.A.I.P. Macchine Agricole Industriali Pieralisi S.P.A. | Συσκευη για τη φυγοκεντρικη εκχυλιση υγρων συστατικων απο ζυμες / υπολειμματα ελαιουχων καρπων με κινηση του ελαφροτερου υγρου συστατικου κατα την αυτη φορα με εκεινη του στερεου υπολειμματος |
| GR20080100085A (el) * | 2007-02-22 | 2009-09-25 | Nuova M.A.I.P Macchine Agricole Industriali Pieralisi S.P.A | Μεθοδος και συσκευη για την ακτινικη εξαγωγη ενος βαρεος συστατικου απο καρπους που περιεχουν ελαιο |
| CN102600992A (zh) * | 2012-03-28 | 2012-07-25 | 湖南省三力士农机制造有限公司 | 卧式螺旋离心滤油机的油室 |
| CN109999555A (zh) * | 2019-05-16 | 2019-07-12 | 河南龙成煤高效技术应用有限公司 | 一种废水离心脱杂机 |
Families Citing this family (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| ES2189564B1 (es) * | 1998-11-16 | 2004-06-16 | Nuova M.A.I.P. Macchine Agricole Industriali Pieralisi S.P.A. | Aparato para la extraccion centrifuga, a partir de productos que producen aceite, tales como aceitunas y similares, de dos componentes liquidos, utilizacion del mismo y procedimiento para el secado y la separacion del aceite. |
| TNSN04181A1 (en) * | 2003-09-22 | 2007-03-12 | Nuova M A I P -Macchine Agricole Ind Pieralisi S P A | Method and plant for treating a residue resulting from a process for extracting oil from oil-containing produce. |
| ES1304613Y (es) * | 2023-09-07 | 2024-03-06 | Instalacion Mantenimiento Y Sist De Pesaje S L | Aportador de agua perimetral para maquinas separadoras de aceite horizontales |
Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE1918130A1 (de) * | 1968-04-18 | 1969-11-20 | Mario De Martini | Zentrifuge,insbesondere zur Trennung von Gemischen aus Feststoffen und mindestens zwei verschieden schweren Fluessigkeiten |
| FR2054722A5 (en) * | 1969-07-24 | 1971-05-07 | Saget Pierre | Centrifuge sepg two liquids and a solid |
| US4295600A (en) * | 1979-02-23 | 1981-10-20 | Saget Pierre Laurent | Apparatus for the centrifugal separation of at least two liquid phases and one sedimentary phase of a mixture |
| GB2083381A (en) * | 1980-09-09 | 1982-03-24 | Alfa Laval Separation As | Uniflow decanter centrifuge |
| EP0140672A2 (fr) * | 1983-10-28 | 1985-05-08 | THOMAS BROADBENT & SONS LIMITED | Décanteuses centrifuges |
-
1995
- 1995-09-07 ES ES95202424T patent/ES2091735T3/es not_active Expired - Lifetime
- 1995-09-07 EP EP95202424A patent/EP0704248B1/fr not_active Expired - Lifetime
- 1995-09-27 TR TR95/01176A patent/TR199501176A2/xx unknown
- 1995-09-27 TN TNTNSN95096A patent/TNSN95096A1/fr unknown
-
1998
- 1998-01-07 GR GR980400009T patent/GR3025834T3/el unknown
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE1918130A1 (de) * | 1968-04-18 | 1969-11-20 | Mario De Martini | Zentrifuge,insbesondere zur Trennung von Gemischen aus Feststoffen und mindestens zwei verschieden schweren Fluessigkeiten |
| FR2054722A5 (en) * | 1969-07-24 | 1971-05-07 | Saget Pierre | Centrifuge sepg two liquids and a solid |
| US4295600A (en) * | 1979-02-23 | 1981-10-20 | Saget Pierre Laurent | Apparatus for the centrifugal separation of at least two liquid phases and one sedimentary phase of a mixture |
| GB2083381A (en) * | 1980-09-09 | 1982-03-24 | Alfa Laval Separation As | Uniflow decanter centrifuge |
| EP0140672A2 (fr) * | 1983-10-28 | 1985-05-08 | THOMAS BROADBENT & SONS LIMITED | Décanteuses centrifuges |
Cited By (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP0785029A1 (fr) * | 1996-01-18 | 1997-07-23 | RAPANELLI FIORAVANTE S.p.A. | Centrifugeuse horizontale pour l'extraction optimale d'huile |
| EP0845296A1 (fr) * | 1996-10-18 | 1998-06-03 | Gennaretti S.p.A. | Centrifugeuse horizontale pour l'extraction d'huile de mélanges oléagineux |
| GR990100394A (el) * | 1998-11-16 | 2000-07-31 | Nuova M.A.I.P. Macchine Agricole Industriali Pieralisi S.P.A. | Συσκευη για τη φυγοκεντρικη εκχυλιση υγρων συστατικων απο ελαιοφορα προιοντα και παρομοια, εφοδιασμενη με μεσα για την ακτινικη εκχυλιση του υγρου συστατικου με μεγαλυτερο ειδικο βαρος |
| GR20000100113A (el) * | 1999-04-06 | 2000-12-29 | Nuova M.A.I.P. Macchine Agricole Industriali Pieralisi S.P.A. | Μεθοδος ληψεως ελαιου απο ελαιοφορα προιοντα και παρομοια με τη βοηθεια φυγοκεντρισεως με διαχωρισμο του στερεου συστατικου σε δυο μερη, και αντιστοιχη εγκατασταση |
| GR20020100162A (el) * | 2001-04-12 | 2002-12-19 | Nuova M.A.I.P. Macchine Agricole Industriali Pieralisi S.P.A. | Συσκευη για τη φυγοκεντρικη εκχυλιση υγρων συστατικων απο ζυμες / υπολειμματα ελαιουχων καρπων με κινηση του ελαφροτερου υγρου συστατικου κατα την αυτη φορα με εκεινη του στερεου υπολειμματος |
| WO2002089992A1 (fr) * | 2001-05-03 | 2002-11-14 | Westfalia Separator Ag | Centrifugeuse a vis a paroi pleine et procede d'extraction d'huile a l'aide d'une centrifugeuse a vis a paroi pleine |
| GR20080100085A (el) * | 2007-02-22 | 2009-09-25 | Nuova M.A.I.P Macchine Agricole Industriali Pieralisi S.P.A | Μεθοδος και συσκευη για την ακτινικη εξαγωγη ενος βαρεος συστατικου απο καρπους που περιεχουν ελαιο |
| CN102600992A (zh) * | 2012-03-28 | 2012-07-25 | 湖南省三力士农机制造有限公司 | 卧式螺旋离心滤油机的油室 |
| CN102600992B (zh) * | 2012-03-28 | 2013-11-06 | 湖南省三力士农机制造有限公司 | 卧式螺旋离心滤油机的油室 |
| CN109999555A (zh) * | 2019-05-16 | 2019-07-12 | 河南龙成煤高效技术应用有限公司 | 一种废水离心脱杂机 |
Also Published As
| Publication number | Publication date |
|---|---|
| ES2091735T3 (es) | 1998-02-16 |
| EP0704248B1 (fr) | 1997-12-17 |
| TNSN95096A1 (fr) | 1996-02-06 |
| GR3025834T3 (en) | 1998-04-30 |
| ES2091735T1 (es) | 1996-11-16 |
| TR199501176A2 (tr) | 1996-06-21 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| EP0704248B1 (fr) | Procédé et dispositif pour l'extraction centrifuge d'huile de premier et second pressages | |
| CN203380009U (zh) | 直立式三相组合离心分离机 | |
| US4378906A (en) | Solid jacket centrifuge for material exchange between liquids | |
| EP1418998B8 (fr) | Procede de separation de particules de plasma sanguin contenues dans une suspension de plasma sanguin | |
| US5368541A (en) | Method of extraction of mercury and gold from mine tailings | |
| DE2835307C2 (fr) | ||
| JPH0683802B2 (ja) | 遠心分離セル | |
| DE19746914A1 (de) | Verfahren zum Betreiben einer Zentrifugiereinheit, sowie Znetrifugiereinheit zum Durchführen eines solchen Verfahrens | |
| JP2010526654A (ja) | 遠心分離機内の流体を浄化する方法および装置 | |
| GB2113576A (en) | Countercurrent centrifugal extractor | |
| US3117928A (en) | Centrifugal separator | |
| US5965021A (en) | Hydrocyclone | |
| US3484040A (en) | Multiple chamber centrifuge | |
| RU2314166C2 (ru) | Установка для разделения жидкостей по плотностям методом центрифугирования и способ ее изготовления | |
| EP0856360A3 (fr) | Vis pour séparateur centrifuge de l'huile d'olive | |
| CN111729762B (zh) | 一种多锥沉降过滤离心机 | |
| WO2023046495A1 (fr) | Séparateur centrifuge ayant une entrée et une sortie hermétiques | |
| NO850266L (no) | Sentrifuge. | |
| WO1989004214A1 (fr) | Separateur centrifuge | |
| US2040213A (en) | Centrifugal machine | |
| RU2036702C1 (ru) | Газовая центрифуга | |
| EP0845297B1 (fr) | Séparateur centrifuge pour l'huile d'olives | |
| ITMI951564A1 (it) | Procedimento per l'estrazione di olio di prima e seconda spremitura mediante estrattore centrifugo orizzontale e relativo estrattore | |
| US2718353A (en) | Continuous centrifuge | |
| US4220279A (en) | Installation for the centrifugal extraction of one liquid by another |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PUAI | Public reference made under article 153(3) epc to a published international application that has entered the european phase |
Free format text: ORIGINAL CODE: 0009012 |
|
| AK | Designated contracting states |
Kind code of ref document: A1 Designated state(s): ES GR IT PT |
|
| 17P | Request for examination filed |
Effective date: 19960807 |
|
| REG | Reference to a national code |
Ref country code: ES Ref legal event code: BA2A Ref document number: 2091735 Country of ref document: ES Kind code of ref document: T1 |
|
| GRAG | Despatch of communication of intention to grant |
Free format text: ORIGINAL CODE: EPIDOS AGRA |
|
| 17Q | First examination report despatched |
Effective date: 19970219 |
|
| GRAG | Despatch of communication of intention to grant |
Free format text: ORIGINAL CODE: EPIDOS AGRA |
|
| GRAH | Despatch of communication of intention to grant a patent |
Free format text: ORIGINAL CODE: EPIDOS IGRA |
|
| GRAH | Despatch of communication of intention to grant a patent |
Free format text: ORIGINAL CODE: EPIDOS IGRA |
|
| GRAA | (expected) grant |
Free format text: ORIGINAL CODE: 0009210 |
|
| AK | Designated contracting states |
Kind code of ref document: B1 Designated state(s): ES GR IT PT |
|
| REG | Reference to a national code |
Ref country code: ES Ref legal event code: FG2A Ref document number: 2091735 Country of ref document: ES Kind code of ref document: T3 |
|
| ITF | It: translation for a ep patent filed | ||
| REG | Reference to a national code |
Ref country code: PT Ref legal event code: SC4A Free format text: AVAILABILITY OF NATIONAL TRANSLATION Effective date: 19980122 |
|
| PLBE | No opposition filed within time limit |
Free format text: ORIGINAL CODE: 0009261 |
|
| STAA | Information on the status of an ep patent application or granted ep patent |
Free format text: STATUS: NO OPPOSITION FILED WITHIN TIME LIMIT |
|
| 26N | No opposition filed | ||
| PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: GR Payment date: 20130918 Year of fee payment: 19 Ref country code: ES Payment date: 20130916 Year of fee payment: 19 Ref country code: PT Payment date: 20130925 Year of fee payment: 19 |
|
| PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: IT Payment date: 20130927 Year of fee payment: 19 |
|
| REG | Reference to a national code |
Ref country code: PT Ref legal event code: MM4A Free format text: LAPSE DUE TO NON-PAYMENT OF FEES Effective date: 20150309 |
|
| PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: PT Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20150309 |
|
| REG | Reference to a national code |
Ref country code: GR Ref legal event code: ML Ref document number: 980400009 Country of ref document: GR Effective date: 20150403 |
|
| PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: IT Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20140907 Ref country code: GR Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20150403 |
|
| REG | Reference to a national code |
Ref country code: PT Ref legal event code: MM4A Free format text: MAXIMUM VALIDITY LIMIT REACHED Effective date: 20150907 |
|
| REG | Reference to a national code |
Ref country code: ES Ref legal event code: FD2A Effective date: 20151027 |
|
| PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: PT Free format text: LAPSE BECAUSE OF EXPIRATION OF PROTECTION Effective date: 20150915 |
|
| PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: ES Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20140908 |
|
| PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: PT Free format text: LAPSE BECAUSE OF EXPIRATION OF PROTECTION Effective date: 20140907 |