EP1337343B1 - Screw for a screw-type solid bowl centrifuge and method for producing oil using such a screw-type solid bowl centrifuge - Google Patents
Screw for a screw-type solid bowl centrifuge and method for producing oil using such a screw-type solid bowl centrifuge Download PDFInfo
- Publication number
- EP1337343B1 EP1337343B1 EP01993375A EP01993375A EP1337343B1 EP 1337343 B1 EP1337343 B1 EP 1337343B1 EP 01993375 A EP01993375 A EP 01993375A EP 01993375 A EP01993375 A EP 01993375A EP 1337343 B1 EP1337343 B1 EP 1337343B1
- Authority
- EP
- European Patent Office
- Prior art keywords
- screw
- blade
- recesses
- area
- blade segments
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
Links
- 239000007787 solid Substances 0.000 title claims abstract description 50
- 238000004519 manufacturing process Methods 0.000 title abstract description 11
- 235000013399 edible fruits Nutrition 0.000 claims abstract description 10
- 239000000463 material Substances 0.000 claims abstract description 8
- 238000000926 separation method Methods 0.000 claims description 17
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 16
- 238000000034 method Methods 0.000 claims description 13
- 239000012071 phase Substances 0.000 claims description 13
- 244000025272 Persea americana Species 0.000 claims description 7
- 235000008673 Persea americana Nutrition 0.000 claims description 7
- 239000007791 liquid phase Substances 0.000 claims description 6
- 241000207836 Olea <angiosperm> Species 0.000 claims description 5
- 239000002184 metal Substances 0.000 claims description 2
- 230000000979 retarding effect Effects 0.000 claims 3
- 241000251468 Actinopterygii Species 0.000 abstract description 2
- 241001465754 Metazoa Species 0.000 abstract description 2
- 239000011368 organic material Substances 0.000 abstract description 2
- 235000006085 Vigna mungo var mungo Nutrition 0.000 abstract 1
- 240000005616 Vigna mungo var. mungo Species 0.000 abstract 1
- 210000000577 adipose tissue Anatomy 0.000 abstract 1
- 210000001519 tissue Anatomy 0.000 abstract 1
- 239000003921 oil Substances 0.000 description 28
- 235000019198 oils Nutrition 0.000 description 28
- 230000010006 flight Effects 0.000 description 14
- 238000005191 phase separation Methods 0.000 description 10
- 235000008390 olive oil Nutrition 0.000 description 7
- 239000004006 olive oil Substances 0.000 description 7
- 238000000605 extraction Methods 0.000 description 5
- 241000237858 Gastropoda Species 0.000 description 4
- 230000008901 benefit Effects 0.000 description 4
- 239000000725 suspension Substances 0.000 description 4
- 238000011084 recovery Methods 0.000 description 3
- 230000000694 effects Effects 0.000 description 2
- 238000004898 kneading Methods 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 239000010802 sludge Substances 0.000 description 2
- 230000007704 transition Effects 0.000 description 2
- 201000005569 Gout Diseases 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 230000001419 dependent effect Effects 0.000 description 1
- 239000000839 emulsion Substances 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 230000002093 peripheral effect Effects 0.000 description 1
- 230000003716 rejuvenation Effects 0.000 description 1
- 238000009751 slip forming Methods 0.000 description 1
- 239000002002 slurry Substances 0.000 description 1
- 239000004449 solid propellant Substances 0.000 description 1
Images
Classifications
-
- 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
- B04B2001/205—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 special construction of screw thread, e.g. segments, height
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10S494/00—Imperforate bowl: centrifugal separators
- Y10S494/901—Imperforate bowl: centrifugal separators involving mixture containing oil
Definitions
- the invention relates to a screw for a solid bowl screw centrifuge according to the preamble of claim 1 and a method for oil extraction with a solid bowl centrifuge.
- a method that has proven particularly useful in olive oil production is from EP 0 557 758.
- a two-phase separation performed, in which the oil directly from a solid / water mixture is separated.
- the invention solves this problem on the one hand by a particularly advantageous Worm whose features are specified in claim 1. It also dissolves it a particularly advantageous method for oil extraction, the features in the claim 35 are indicated.
- a screw is provided for a solid bowl centrifuge, the sections in the conveyor track between adjacent Schnekken réellen has additional space segments. Furthermore, the screw blade is preferable provided with recesses which are formed such that a Flow through the material to be centrifuged between adjacent flights possible is.
- the screw according to the invention By the screw according to the invention, the economy of oil production can be considerably increase. In this respect, in particular to the in the figure description referenced experiments, whose results in the figures 4 and 5 are shown. A particular advantage of the invention is to be seen in that the screw also easily retrofit existing centrifuges leaves.
- the screw according to the invention is particularly suitable for use in a process for oil extraction from fruits and seeds and for better drainage and / or de-oiling pulp from organic materials (e.g. Pulp mash, animal tissues such as fish, egg, gout cells).
- a Combination of recesses and blade segments provide, wherein the blade segments and the recesses are preferably formed in the axial direction are that the recesses each in the axial direction (and / or angled or zig-zag to the central axis y) form extending channels in which the Leaf segments are standing.
- blade segments and the recesses are formed only in the cylindrical portion of the screw body and when in the conical section of the screw, especially in the two-phase separation a baffle plate is provided.
- leaf-segment-like screw threads for example from WO 97/23295.
- these leaf segments extend into the conical section, which is unfavorable according to the invention is.
- they are on the circumference of the screw body in its entire area distributed, which has also proved to be of little benefit.
- the additional blade segments in the conveyor track are formed so that they are in the range of solids or the solids but preferably an outer region of e.g. 25 mm is not reached by the leaf segments, since in this area already relative completely de-oiled and permanently discharged solids are present.
- a solids slurry preferably via a rectangular tube, in the drum is fed.
- the rectangular tube must be so long that the incoming, protected to be centrifuged by the oil layer is brought to this subsequently not remix.
- the separation zone is quite close to the screw body a (10, 20 ..., to 40 to 50 mm distance).
- the fresh oil is as clean Phase only 20 to 30 mm outside the slug body recognize.
- the introduced solid as part of the supplied suspension is thus the machine Fill so far that this up to the oil separation zone (about 10, 20 ... to a maximum of 40 to 50 mm outside the screw body) is filled with solid suspensions.
- the oil separation zone about 10, 20 ... to a maximum of 40 to 50 mm outside the screw body
- solid suspensions are filled with solid suspensions.
- the solid is drier on the outside than inside In other words, the dry matter content on the drum side is much higher than the dry matter content towards the interior.
- the solid In the area of the leading leaf segments, the solid additionally becomes axially pressed together. He is then relaxed in the area of the recesses. It results thus an effect of pressure increases and relaxation. Essentially in the relaxation area the oil release takes place, which is thus more effective than without the additional relaxation zones.
- the worm body has a cylindrical in its rear region Section and in its adjoining front area one substantially conically uniform or uneven - e.g. stepped - tapered section on, with the recesses and leaf segments exclusively are formed in the region of the cylindrical portion.
- the screw body in the cylindrical portion initially at least one helix, which is free of recesses and free of leaf segments is formed, which is followed by further worm threads, which with the Recesses and leaf segments are provided.
- Oil drain channels are formed.
- the recesses have a remaining portion of the screw blade on the circumference of the screw body.
- the leaf segments - based on one or more flights - Evenly or unevenly distributed on the circumference of the screw body.
- the area of the recesses is about 25-60%, in particular 40 - 50% of the worm gear area.
- the recesses in the screw blades are designed such that they project radially beyond at least the area of the solid zone (for example 70-95%, preferably 70-100% of the screw blade height).
- the height of the leaf segments is about 0 - 30% lower than that Screw blade height.
- the blade segments are designed as rectangular plates conceivable are also trapezoidal, rounded and / or from the snail body outwardly tapering or widening shaped elements.
- Fig. 1 shows a screw 1 for a solid bowl screw centrifuge, wherein the Screw a worm body 3 and here a worm body 3 several times surrounding worm blade 5, which has a plurality of flights (x, x + 1, x + 2, etc.).
- a conveyor track 7 for Fördem / transport formed to be processed centrifuged is a conveyor track 7 for Fördem / transport formed to be processed centrifuged.
- the screw body 3 has in its rear in Fig. 1 area a cylindrical Section 9 and in his in Fig. 1 adjoining the front area a conically tapering section 11.
- the centrifuged material S is through the centrally disposed, adjustable inlet pipe 14th in an inlet chamber 15 and from there through openings 17 in the drum space 19 with the screw 1 and the screw 1 surrounding drum 21 passed.
- these Einlaufkammem 15 and openings 17 (or special Distributor) in the embodiment of Fig. 1 at the rear end of the cylindrical Section 3 arranged.
- the centrifuged material S is accelerated to the operating speed.
- the solid particles settle in the shortest possible time Time off at the drum wall.
- the screw 1 rotates at a speed slightly lower or higher than the drum 21 and promotes the ejected solid F to the conical section 11 out of the drum 21 for solids 23.
- the liquid L flows toward the larger drum diameter at the rear End of the drum 21 and is derived there (overflow 25).
- the worm 1 of Figure 1 points from its second flight (X + 1) to its fifth flight (X + 4) recesses 27 in the screw on.
- recesses 27 are formed in the embodiment of FIG. 1 such that in the axial direction from the second to the fifth screw blade forming extending axial channels K.
- a single helix with Recesses 27 and blade segments 29 is in a simplified embodiment also conceivable.
- additional leaf segments 29 are arranged here as Metal strips are formed here from the outer periphery of the Schnekken stresses 3 outwardly widening trapezoidal shape.
- the separation of the leaf sections or segments can either take place in such a way that that the screw blade 5 is separated to the circumference of the screw body 3 becomes. Alternatively, however, a remaining portion 30 of the screw blade 5 on The circumference of the screw body 3 stop. Is the removal essentially radially to the drum and screw axis y, resulting trapezoidal Leaf segments 29.
- Fig. 6a, b show the velocity profiles in a helix in the area the recesses and leaf segments.
- Fig. 6a it is clear that "in the shade" of the leaf segment, the velocity of the particles increases from the inside to the outside.
- the maximum value is reached, which According to Fig. 6b at the upper leaf segment edge again substantially constant is.
- the screw 1 - in Fig. 1 from the rear inlet zone forward looking at the conical section - at first some turns x-1, x, x + 1 on, in the area of the screw blade 5 each continuous or free of recesses is trained.
- at least one or two flights are x continuously formed. In this area are also no additional Leaf segments 29 provided in the conveyor track 7.
- This zone is followed by some worm threads x + 2, ... x + 5, which with the recesses 27 are provided and in the interstices or in the Conveyor tracks 7 each formed the blade segments 29 or erected (welded) are.
- This zone extends maximally to the beginning of the conical section 11th the screw 1.
- the baffle plate 13 is arranged.
- the snail should be formed free of recesses, also in the conveyor track 7 and no additional Leaf segments 29 are arranged.
- Per screw flight are preferably 2 to 6, especially 3 to 5, especially preferably 4 recesses 27 formed.
- the blade segments 29 are uniformly on the circumference of the screw body 3 distributed.
- the worm threads x are relative to the central axis or to the axis of symmetry y Screw 1 each arranged at an angle or close to the central axis one Angle ⁇ on.
- the amount of the angle ⁇ (measured at the bottom of the Schnekkenblattes 5), is preferably between 60 and 85 °, in particular at 75 to 80 °.
- the blade segments close with the symmetry axis y a Angle ⁇ one smaller than ⁇ .
- ⁇ is between 40 and 70 °, in particular 50 to 55 °.
- the blade segments 29 are substantially parallel to the To align the worm blade 5 (maximum difference angle between ⁇ and ⁇ preferably about 10 - 11 °).
- the surface of the recesses is about 50 ° of the checkered surface.
- the angular size ( ⁇ ) is determined by the fact that the Width of the distance (a) - viewed in orthogonal extension of the edges - between the blade longitudinal edge and the recess edge 27 at 0 to 28%, in particular at 15 to 25% of the distance of a pair of flights - preferably considered at the base of the snail (inside), depending on the shape - lies.
- the height h of the Blade segments (measured from the outer circumference of the screw body 3).
- the height h of Blade segments 29 is selected such that it extends into the region of the solid zone extend. Accordingly, the screw blades 5 should have recesses 27, which project radially beyond at least the region of the solid zone.
- the height h is selected about 30 mm lower than the Schneckenblatt height k.
- the worm blade closes with the peripheral wall of the worm body 3 according to FIG. 2b further includes an angle ⁇ . This is preferably smaller as the angle ⁇ , which the blade segment 29 encloses with the screw body 3.
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- Centrifugal Separators (AREA)
Abstract
Description
Die Erfindung betrifft eine Schnecke für eine Vollmantel-Schneckenzentrifuge
nach dem Oberbegriff des Anspruches 1 und ein Verfahren zur Ölgewinnung mit
einer Vollmantel-Schneckenzentrifuge.The invention relates to a screw for a solid bowl screw centrifuge
according to the preamble of
Ein Verfahren, welches sich bei der Olivenölgewinnung besonders bewährt hat, ist
aus der EP 0 557 758 bekannt. Bei diesem Verfahren wird eine Zweiphasen-Trennung
durchgeführt, bei welcher das Öl direkt von einem Feststoff-/Wassergemisch
abgetrennt wird.A method that has proven particularly useful in olive oil production is
from
Die Effizienz dieses bekannten Verfahrens ist an sich bereits sehr gut.The efficiency of this known method is already very good in itself.
Dennoch ist es wünschenswert, den Restölgehalt im Trester nochmals zu senken, um die Wirtschaftlichkeit der Ölgewinnung zu steigern.Nevertheless, it is desirable to reduce the residual oil content in the pomace again, to increase the profitability of oil production.
Die Lösung dieses Problems sowohl in konstruktiver als auch in verfahrenstechnischer Hinsicht ist die Aufgabe der Erfindung.The solution of this problem both constructively and procedurally Regard, the object of the invention.
Die Erfindung löst diese Aufgabe einerseits durch eine besonders vorteilhafte
Schnecke, deren Merkmale im Anspruch 1 angegeben sind. Sie löst sie ferner durch
ein besonders vorteilhaftes Verfahren zur Ölgewinnung, dessen Merkmale im Anspruch
35 angegeben sind.The invention solves this problem on the one hand by a particularly advantageous
Worm whose features are specified in
Nach Anspruch 1 wird eine Schnecke für eine Vollmantel-Schneckenzentrifuge geschaffen,
die in der Förderbahn abschnittsweise zwischen benachbarten Schnekkengängen
zusätzliche Platzsegmente aufweist. Ferner ist das Schneckenblatt vorzugsweise
mit Aussparungen versehen, welche derart ausgebildet sind, daß ein
Durchströmen des Schleudergutes zwischen benachbarten Schneckengängen möglich
ist. According to
In Hinsicht auf das Verfahren zur Ölgewinnung hat sich ferner als besonders vorteilhaft herausgestellt, wenn das Öl als Flüssigkeitsphase wiederum direkt in einem Zweiphasen-Trennschritt von einer zweiten Mischphase aus Wasser und Feststoffen abgetrennt wird, wobei die Saaten oder zerkleinerten Früchte wie Oliven oder Avocados zunächst in eine Vollmantel-Schneckenzentrifuge durch eine Trennzone mit einer oder mehreren Schneckengängen geleitet werden, in dem das Schneckenblatt vorzugsweise aussparungsfrei ausgebildet ist, wobei im Förderbahnbereich zwischen den Schneckengängen vorzugsweise keine Blattsegmente in der Förderbahn ausgebildet sind. Daraufhin wird in der Trennzone ein weiterer Schneckenbereich durchlaufen, in dem Aussparungen im Schneckenblatt ausgebildet sind und Blattsegmente in der Förderbahn stehen. Daraufhin werden die Feststoffe und das Wasser an einer Stauscheibe vorbei aus der Trennzone in den konischen Abschnitt der Schnecke gefördert.With regard to the method of oil extraction has also been found to be particularly advantageous Turned out when the oil is again in a liquid phase as a liquid phase Two-phase separation step from a second mixed phase of water and solids is separated, with the seeds or crushed fruits such as olives or Avocados first into a solid bowl centrifuge through a separation zone be guided with one or more flights, in which the Schneckenblatt preferably formed free of recesses, wherein in the conveying path area preferably no blade segments in the conveyor track between the screw flights are formed. Then, in the separation zone, another screw area go through, are formed in the recesses in the screw blade and Leaf segments are in the conveyor track. Then the solids and the Water past a baffle plate from the separation zone into the conical section promoted the snail.
Mit der erfindungsgemäßen Schnecke läßt sich auch die Dreiphasen-Ölgewinnung verbessern, die gelegentlich noch zum Einsatz kommt. Dabei wird das Öl als Flüssigkeitsphase in einem Dreiphasen-Trennschnitt von einer zweiten Phase - im wesentlichen aus Wasser - und einer dritten - im wesentlichen aus Feststoffen - abgetrennt,
- wobei die zerkleinerten Früchte wie Oliven oder Avocados oder Saaten zunächst in einer Vollmantelschneckenzentrifuge durch eine Trennzone mit einer oder mehreren Schneckengängengeleitet wird, in dem das Schneckenblatt vorzugsweise aussparungsfrei ausgebildet ist, wobei im Förderbahnbereich zwischen den Schneckengängen vorzugsweise keine Blattsegmente in der Förderbahn ausgebildet sind,
- woraufhin in der Trennzone ein Schneckenbereich durchlaufen wird, in dem die Aussparungen im Schneckenblatt und die Blattsegmente in der Förderbahn ausgebildet sind,
- woraufhin die drei Phasen aus der Zentrifuge geleitet/gefördert werden.
- wherein the minced fruits such as olives or avocados or seeds are first passed in a solid bowl screw centrifuge through a separation zone with one or more flights in which the screw blade is preferably free of recesses, preferably in the conveying path between the screw flights no blade segments are formed in the conveyor track,
- whereupon in the separation zone a screw section is passed, in which the recesses in the screw blade and the blade segments are formed in the conveyor track,
- whereupon the three phases are passed / conveyed from the centrifuge.
Durch die erfindungsgemäße Schnecke läßt sich die Wirtschaftlichkeit der Ölgewinnung beträchtlich steigern. Insofern wird insbesondere auf die in der Figurenbeschreibung näher erläuterten Versuche verwiesen, deren Ergebnisse in den Figuren 4 und 5 dargestellt sind. Ein besonderer Vorteil der Erfindung ist darin zu sehen, daß sich die Schnecke auch problemlos bei bestehenden Zentrifugen nachrüsten läßt. Die erfindungsgemäße Schnecke eignet sich insbesondere zur Anwendung in einem Verfahren zur Ölgewinnung aus Früchten und Saaten und zur besseren Entwässerung und/oder Entölung von Breis aus organischen Materialien (z.B. Saatenbreis, Fruchtfleischmaische, tierische Gewebe wie Fisch, Ei, Gettgewebezellen).By the screw according to the invention, the economy of oil production can be considerably increase. In this respect, in particular to the in the figure description referenced experiments, whose results in the figures 4 and 5 are shown. A particular advantage of the invention is to be seen in that the screw also easily retrofit existing centrifuges leaves. The screw according to the invention is particularly suitable for use in a process for oil extraction from fruits and seeds and for better drainage and / or de-oiling pulp from organic materials (e.g. Pulp mash, animal tissues such as fish, egg, gout cells).
Als besonders vorteilhaft hat es sich im Rahmen der Erfindung herausgestellt, eine Kombination aus Aussparungen und Blattsegmenten vorzusehen, wobei die Blattsegmente und die Aussparungen vorzugsweise in axialer Richtung derart ausgebildet sind, daß die Aussparungen jeweils in axialer Richtung (und/oder winklig oder zick-zackartig zur Mittelachse y) sich erstreckende Kanäle ausbilden, in denen die Blattsegmente stehen.It has been found to be particularly advantageous in the context of the invention, a Combination of recesses and blade segments provide, wherein the blade segments and the recesses are preferably formed in the axial direction are that the recesses each in the axial direction (and / or angled or zig-zag to the central axis y) form extending channels in which the Leaf segments are standing.
Besonders vorteilhaft ist es ferner, wenn die Blattsegmente und die Aussparungen lediglich im zylindrischen Abschnitt des Schneckenkörpers ausgebildet sind und wenn im konischen Abschnitt der Schnecke insbesondere bei der Zweiphasen-Trennung eine Stauscheibe vorgesehen ist.It is also particularly advantageous if the blade segments and the recesses are formed only in the cylindrical portion of the screw body and when in the conical section of the screw, especially in the two-phase separation a baffle plate is provided.
Aus dem Stand der Technik sind zwar bereits Vollmantel-Schneckenzentrifugen bekannt, bei denen Aussparungen im Schneckenblatt vorgesehen sind, so z.B. aus der DE 41 32 593 A1. Aus US-A-5 222 935 ist es bekannt gauze Blattsegmente auszusparen.Although from the prior art already Vollmantel-screw centrifuges known in which recesses are provided in the screw blade, such. out DE 41 32 593 A1. From US-A-5 222 935 it is known to save out gauze leaf segments.
Nach der Erfindung genügt das Vorsehen derartiger Aussparungen jedoch nicht für eine nennenswerte Effizienzsteigerung. Eine besonders vorteilhafte Effizienzsteigerung läßt sich vielmehr erst dadurch erreichen, daß neben den Aussparungen insbesondere in der Mitte der Vorderbahn zwischen benachbarten Schneckengängen die zusätzlichen Blattsegmente aufgestellt sind.According to the invention, however, the provision of such recesses is not sufficient for a notable increase in efficiency. A particularly advantageous increase in efficiency Rather, can be achieved only by the fact that in addition to the recesses in particular in the middle of the front track between adjacent flights the additional leaf segments are placed.
Zwar ist es auch bereits bekannt, blattsegmentartige Schneckengänge auszubilden, so beispielsweise aus der WO 97/23295. Diese Blattsegmente erstrecken sich jedoch bis in den konischen Abschnitt hinein, was nach der Erfindung unvorteilhaft ist. Ferner sind sie am Umfang des Schneckenkörpers in dessen gesamtem Bereich verteilt, was sich ebenfalls als wenig vorteilhaft herausgestellt hat. Zudem werden nicht etwa zusätzliche Blattsegmente in der Förderbahn zwischen den Schneckengängen aufgestellt, sondern die Blattsegmente selbst bilden an sich die Schneckengänge aus. Auch mit dieser Schnecke läßt sich keine zufriedenstellende Wirtschaftlichkeit bei der Olivenölgewinnung erreichen.Although it is already known to form leaf-segment-like screw threads, for example from WO 97/23295. However, these leaf segments extend into the conical section, which is unfavorable according to the invention is. Furthermore, they are on the circumference of the screw body in its entire area distributed, which has also proved to be of little benefit. In addition, will be not about additional leaf segments in the conveyor track between the flights placed, but the leaf segments themselves form the screw flights out. Even with this screw can be no satisfactory economy reach the olive oil production.
Besonders vorteilhaft ist es, wenn die zusätzlichen Blattsegmente in der Förderbahn derart ausgebildet sind, daß sie sich bis in den Bereich der Feststoffe bzw. des Feststoffbereichs erstrecken, wobei aber vorzugsweise ein äußerer Bereich von z.B. 25 mm nicht von den Blattsegmenten erreicht wird, da in diesem Bereich bereits relativ vollständig entölte und permanent ausgetragene Feststoffe vorliegen.It is particularly advantageous if the additional blade segments in the conveyor track are formed so that they are in the range of solids or the solids but preferably an outer region of e.g. 25 mm is not reached by the leaf segments, since in this area already relative completely de-oiled and permanently discharged solids are present.
Meßergebnisse zeigen, daß die erfindungsgemäße Schnecke ca. 1 bis 1,5 % weniger Öl im ausgetragenen Feststoffschlamm hinterläßt. Bei einer Kampagne der Olivenölgewinnung entspricht dies durchaus einem finanziellen Vorteil von ca. DM 300.000,- bis 500.000,- pro Maschine.Measurement results show that the screw according to the invention about 1 to 1.5% less Oil in the discharged solids sludge leaves. In a campaign of olive oil production This is quite a financial advantage of about DM 300,000, - to 500,000, - per machine.
Besonders vorteilhaft ist es, wenn die Knetschnecke im Bereich des feuchten Orujos wirkt, da insbesondere hier eine besondere Entölung durch die zusätzlichen Blattsegmente erreichbar ist.It is particularly advantageous if the kneading screw in the area of the moist Orujos acts, because in particular here a special Entölung by the additional Leaf segments is reached.
Mit der Erfindung wird ein Feststoffbrei, vorzugsweise über ein Rechteckrohr, in die Trommel eingespeist. Das Rechteckrohr muß so lang sein, daß die eintretende, zu zentrifugierende Masse geschützt durch die Ölschicht einbracht wird, um diese nachträglich nicht rückzuvermischen.With the invention, a solids slurry, preferably via a rectangular tube, in the drum is fed. The rectangular tube must be so long that the incoming, protected to be centrifuged by the oil layer is brought to this subsequently not remix.
In der gefüllten Maschine stellt sich die Trennzone ziemlich eng am Schneckenkörper ein (10, 20 ..., bis 40 bis 50 mm Abstand). Das frische Öl ist als saubere Phase nur 20 bis 30 mm außerhalb des Schneckenkörpers zu erkennen. Hier herrscht eine saubere Trennlinie vor. In the filled machine, the separation zone is quite close to the screw body a (10, 20 ..., to 40 to 50 mm distance). The fresh oil is as clean Phase only 20 to 30 mm outside the slug body recognize. Here There is a clean dividing line.
Der eingebrachte Feststoff als Teil der zugeführten Suspension wird also die Maschine so weit füllen, daß diese bis zur Öltrennzone (ca. 10, 20 ... bis maximal 40 bis 50 mm außerhalb des Schneckenkörpers) mit Feststoffsuspensionen gefüllt ist. In der Regel ist nämlich nur so wenig Wasser in der Orujomasse, daß keine oder nur eine äußerst geringe Schicht an freiem Wasser zwischen dem Öl und der Feststoffsuspension ausgebildet ist. Dabei ist der Feststoff außen trockener als innen oder anders ausgedrückt, ist der Trockensubstanzanteil trommelseitig viel höher als der Trockensubstanzanteil zum Inneren hin.The introduced solid as part of the supplied suspension is thus the machine Fill so far that this up to the oil separation zone (about 10, 20 ... to a maximum of 40 to 50 mm outside the screw body) is filled with solid suspensions. As a rule, only so little water is in the Orujomasse that no or only a very small layer of free water between the oil and the solid suspension is trained. The solid is drier on the outside than inside In other words, the dry matter content on the drum side is much higher than the dry matter content towards the interior.
Im Bereich der Aussparungen und Blattsegmente erfährt die Feststoffsuspension insbesondere im Knetbereich der Blattsegmente genau wie das Öl und die dazwischen liegende Emulsion vom Schneckenkörper bis zum radialen Ende drei axiale Geschwindigkeiten.In the area of the recesses and leaf segments experiences the solid suspension especially in the kneading area of the leaf segments just like the oil and the between them lying emulsion from the screw body to the radial end three axial Speeds.
So herrscht eine normale Geschwindigkeit im Bereich der Wand-Reststücke vor. Im Bereich der Aussparungen beträgt die axiale Geschwindigkeit dagegen im wesentlichen null. Dagegen wird die Geschwindigkeit im Bereich der eigentlichen Blattsegmente in der Förderbahn bis zum Fünffachen der normalen Geschwindigkeit betragen. Dadurch wird der viskoelastische Schlamm im Bereich der stehenden Feststoffschicht verformt, insbesondere zusammengedrückt und entspannt.So there is a normal speed in the area of the wall remnants. In the area of the recesses, however, the axial velocity is substantially zero. In contrast, the speed is in the range of the actual Blade segments in the conveyor up to five times the normal speed be. This causes the viscoelastic sludge in the area of standing Solid layer deformed, in particular compressed and relaxed.
Im Bereich der vorauseilenden Blattsegmente wird der Feststoff zusätzlich axial zusammengedrückt. Im Bereich der Aussparungen wird er dann entspannt. Es ergibt sich damit ein Effekt von Druckerhöhungen und Entspannungen. Im wesentlichen im Entspannungsbereich erfolgt die Ölfreisetzung, die somit effektiver ist als ohne die zusätzlichen Entspannungszonen.In the area of the leading leaf segments, the solid additionally becomes axially pressed together. He is then relaxed in the area of the recesses. It results thus an effect of pressure increases and relaxation. Essentially in the relaxation area the oil release takes place, which is thus more effective than without the additional relaxation zones.
Vorzugsweise weist der Schneckenkörper in seinem hinteren Bereich einen zylindrischen Abschnitt und in seinem sich daran anschließenden vorderen Bereich einen sich im wesentlichen konisch gleichmäßig oder ungleichmäßig - z.B. gestuft - verjüngenden Abschnitt auf, wobei die Aussparungen und Blattsegmente ausschließlich im Bereich des zylindrischen Abschnittes ausgebildet sind. Preferably, the worm body has a cylindrical in its rear region Section and in its adjoining front area one substantially conically uniform or uneven - e.g. stepped - tapered section on, with the recesses and leaf segments exclusively are formed in the region of the cylindrical portion.
Vorzugsweise weist der Schneckenkörper im zylindrischen Abschnitt zunächst mindestens einen Schneckengang auf, der aussparungsfrei sowie blattsegmentfrei ausgebildet ist, woran sich weitere Schneckengänge anschließen, welche mit den Aussparungen und Blattsegmenten versehen sind.Preferably, the screw body in the cylindrical portion initially at least one helix, which is free of recesses and free of leaf segments is formed, which is followed by further worm threads, which with the Recesses and leaf segments are provided.
Es ist auch denkbar, daß vorzugsweise im ersten Schneckengang optionale Ölablaufkanäle ausgebildet sind.It is also conceivable that preferably in the first flight optional Oil drain channels are formed.
Vorzugsweise weisen die Aussparungen einen Restabschnitt des Schneckenblattes am Umfang des Schneckenkörpers auf.Preferably, the recesses have a remaining portion of the screw blade on the circumference of the screw body.
Bevorzugt sind die Blattsegmente - bezogen auf einen oder mehrere Schneckengänge - gleichmäßig oder ungleichmäßig am Umfang des Schneckenkörpers verteilt.Preferably, the leaf segments - based on one or more flights - Evenly or unevenly distributed on the circumference of the screw body.
Vorzugsweise beträgt die Fläche der Aussparungen etwa 25 - 60%, insbesondere 40 - 50% der Schneckengangfläche.Preferably, the area of the recesses is about 25-60%, in particular 40 - 50% of the worm gear area.
Vorzugsweise sind die Aussparungen in den Schneckenblättern derart ausgebildet, daß sie radial zumindest den Bereich der Feststoffzone überragen (z.B. 70 - 95 %, vorzugsweise 70 - 100 % der Schneckenblatthöhe).Preferably, the recesses in the screw blades are designed such that they project radially beyond at least the area of the solid zone (for example 70-95%, preferably 70-100% of the screw blade height).
Insbesondere ist die Höhe der Blattsegmente ca. 0 - 30% niedriger ist als die Schneckenblatthöhe.In particular, the height of the leaf segments is about 0 - 30% lower than that Screw blade height.
Vorzugsweise sind die Blattsegmente als rechtwinklige Bleche ausgebildet Denkbar sind auch trapezförmige, abgerundete und/oder sich vom Schneckenkörper nach außen verjüngend oder verbreiternd geformte Elemente.Preferably, the blade segments are designed as rectangular plates conceivable are also trapezoidal, rounded and / or from the snail body outwardly tapering or widening shaped elements.
Besonders vorteilhafte Ausführungen der Erfindung sind den übrigen Unteransprüchen zu entnehmen. Particularly advantageous embodiments of the invention are the remaining dependent claims refer to.
Nachfolgend werden Ausführungsbeispiele anhand der Zeichnung näher beschrieben. Es zeigt:
- Fig. 1
- eine perspektivische Darstellung einer erfindungsgemäßen Schnecke für eine Vollmantel-Schneckenzentrifuge;
- Fig. 2a
- eine Draufsicht auf einen Abschnitt einer Schnecke;
- Fig. 2b
- einen Schnitt längs der Linie A-A aus Fig. 2a;
- Fig. 3
- eine Vollmantelschneckenzentrifuge nach der Erfindung;
- Fig. 4 und 5
- Diagramme, welche die Restölgehalte im Trester bei der Olivenölgewinnung mit Vollmantel-Schneckenzentrifugen im Zweiphasen-Trennver-fahren unter Einsatz von Schnecken nach der Erfindung und von Schnecken nach dem Stand der Technik vergleichen; und
- Fig. 6a,b
- die Geschwindigkeitsprofile in einem Schneckengang im Bereich der Aussparungen und Blattsegmente.
- Fig. 1
- a perspective view of a screw according to the invention for a solid bowl screw centrifuge;
- Fig. 2a
- a plan view of a portion of a screw;
- Fig. 2b
- a section along the line AA of Fig. 2a;
- Fig. 3
- a solid bowl screw centrifuge according to the invention;
- 4 and 5
- Charts comparing the residual oil levels in the pomace in the olive oil recovery with solid bowl centrifuges in the two-phase separation process using screws according to the invention and of screws according to the prior art; and
- Fig. 6a, b
- the velocity profiles in a helix in the area of the recesses and leaf segments.
Die Maßangaben der Beschreibung beziehen sich beispielhaft auf bevorzugte Ausführungen.The dimensions of the description relate by way of example to preferred embodiments.
Fig. 1 zeigt eine Schnecke 1 für eine Vollmantel-Schneckenzentrifuge, wobei die
Schnecke einen Schneckenkörper 3 sowie hier ein den Schneckenkörper 3 mehrfach
umgebendes Schneckenblatt 5 aufweist, das mehrere Schneckengänge (x, x+1,
x+2 usw.) ausbildet.Fig. 1 shows a
Zwischen den Schneckengängen x, x+1, ... ist eine Förderbahn 7 zum Fördem/Transport
eines zu verarbeitenden Schleudergutes ausgebildet.Between the worm threads x, x + 1, ... is a
Der Schneckenkörper 3 weist in seinem in Fig. 1 hinteren Bereich einen zylindrischen
Abschnitt 9 und in seinem in Fig. 1 sich daran anschließenden vorderen Bereich
einen sich konisch verjüngenden Abschnitt 11 auf.The
Im Übergangsbereich zwischen dem zylindrischen Abschnitt 9 und dem konischen
Abschnitt 11 ist hier eine (Stau-)Scheibe 13 auf den Schneckenkörper 3 aufgesetzt. In the transition region between the
Diese hat sich insbesondere bei der Zweiphasen-Trennung bewährt. Bei einer Dreiphasen-Trennung in die Phasen Öl, Wasser und Feststoffe ist sie nicht erforderlich.This has proven particularly in the two-phase separation. In a three-phase separation it is not required in the phases of oil, water and solids.
Die Funktion dieser Vollmantel-Schneckenzentrifuge, deren übrige wesentliche Bestandteile sich aus Fig. 3 erschließen, ist wie folgt.The function of this solid bowl centrifuge, the remaining essential Components of FIG. 3 are as follows.
Das Schleudergut S wird durch das zentral angeordnete, verstellbare Einlaufrohr 14
in eine Einlaufkammer 15 und von dort durch Öffnungen 17 in den Trommelraum
19 mit der Schnecke 1 und der die Schnecke 1 umgebenden Trommel 21 geleitet.
Vorzugsweise werden diese Einlaufkammem 15 und Öffnungen 17 (oder spezielle
Verteiler) bei der Ausführungsform der Fig. 1 am hinteren Ende des zylindrischen
Abschnitt 3 angeordnet.The centrifuged material S is through the centrally disposed, adjustable inlet pipe 14th
in an
Im Trommelraum 19 wird das Schleudergut S auf die Betriebsdrehzahl beschleunigt.
Durch Einwirkung der Schwerkraft setzen sich die Feststoffteilchen in kürzester
Zeit an der Trommelwand ab.In the
Die Schnecke 1 rotiert mit einer etwas kleineren oder größeren Geschwindigkeit als
die Trommel 21 und fördert den ausgeschleuderten Feststoff F zum konischen Abschnitt
11 hin aus der Trommel 21 zum Feststoffaustrag 23.The
Die Flüssigkeit L strömt dagegen zum größeren Trommeldurchmesser am hinteren
Ende der Trommel 21 und wird dort abgeleitet (Überlauf 25).On the other hand, the liquid L flows toward the larger drum diameter at the rear
End of the
Die Schnecke 1 der Fig.1 weist von ihrem zweiten Schneckengang (X+1) bis zu ihrem
fünften Schneckengang (X+4) Aussparungen 27 im Schneckenblatt auf.The
Diese Aussparungen 27 sind bei dem Ausführungsbeispiel der Fig. 1 derart ausgebildet,
daß in axialer Richtung ein sich vom zweiten bis zum fünften Schneckenblatt
erstreckende axiale Kanäle K ausbilden. Ein einzelner Schneckengang mit
Aussparungen 27 und Blattsegmenten 29 ist bei einer vereinfachten Ausführung
ebenfalls denkbar. These
In der zwischen den Schneckengängen (X, ...) des Schneckenblattes 5 ausgebildete
Förderbahn 7 sind dagegen zusätzliche Blattsegmente 29 angeordnet, die hier als
Metallstreifen ausgebildet sind, die hier eine sich vom Außenumfang des Schnekkenkörpers
3 nach außen verbreiternde Trapezform aufweisen.In between the worm threads (X, ...) of the
Vorteilhaft und auf einfache sowie kostengünstige Weise werden diese Blattsegmente
29 dadurch ausgebildet, daß die Blattabschnitte- bzw. -segmente, welche
beim Abtrennen von Material zum Ausbilden der Aussparungen 27 abgetrennt
werden, in die Förderbahn 7 gesetzt und dort verschweißt werden.Advantageously and in a simple and cost-effective manner, these
Das Abtrennen der Blattabschnitte bzw. -segmente kann entweder derart erfolgen,
daß das Schneckenblatt 5 bis zum Umfang des Schneckenkörpers 3 ausgetrennt
wird. Alternativ kann aber auch ein Restabschnitt 30 des Schneckenblattes 5 am
Umfang des Schneckenkörpers 3 stehenbleiben. Erfolgt das Austrennen im wesentlichen
radial zur Trommel- und Schneckenachse y, ergeben sich trapezförmige
Blattsegmente 29.The separation of the leaf sections or segments can either take place in such a way that
that the
Mit einer derartigen Kombination aus Aussparungen 27 und "Zwischen-"Blattsegmenten
29 in der Förderbahn 7 läßt sich die Effizienz verschiedener der
zentrifugalen Trennvorgänge überraschend deutlich steigern.With such a combination of
Insbesondere hat sich die Schneckenausbildung mit Aussparungen 27 und 29 im Bereich der Olivenölgewinnung bewährt. Besonders bewährt hatte sich bei der Olivenölgewinnung bereits eine Zweiphasen-Trennung, bei der das Öl direkt von einem Feststoff-/Wassergemisch abgetrennt wird. Ein derartiges Verfahren wird in der EP 557 758 beschrieben. Die Effizienz dieses an sich bereits hervorragenden Verfahrens läßt sich durch die Schnecke 1 der Erfindung nochmals deutlich steigern. Als besonders vorteilhaft hat es sich dabei erwiesen, wenn
- das Öl als Flüssigkeitsphase direkt in einem Zweiphasen-Trennschritt von einer zweiten Mischphase aus Wasser und Feststoffen abgetrennt wird,
- wobei die zerkleinerten Früchte wie Oliven oder Avocados zunächst in einer
Vollmantelschneckenzentrifuge durch eine Trennzone mit einem oder mehreren
Schneckengängen X, ... geleitet wird, in
dem das Schneckenblatt 5keine Aussparungen 27 aufweist und indem keine Blattsegmente 29 in der Förderbahn ausgebildet sind - woraufhin in der Trennzone ein zweiter Schneckenbereich durchlaufen wird, in
dem die Aussparungen 27im Schneckenblatt 5 und dieBlattsegmenten 29 inder Förderbahn 7 ausgebildet sind, - woraufhin die Feststoffe und das Wasser an einer Stauscheibe 13 vorbei aus der Trennzone in den konischen Abschnitt der Schnecke 1 gefördert werden.
- the oil as liquid phase is separated from a second mixed phase of water and solids directly in a two-phase separation step,
- wherein the minced fruit such as olives or avocados is first passed in a solid bowl centrifuge through a separation zone with one or more flights X, ..., in which the
screw blade 5 has norecesses 27 and in which noleaf segments 29 are formed in the conveyor track - whereupon in the separation zone, a second screw region is traversed, in which the
recesses 27 in thescrew blade 5 and theblade segments 29 are formed in theconveyor track 7, - whereupon the solids and the water are conveyed past a baffle plate 13 from the separation zone into the conical section of the
screw 1.
Die Vorteile dieses Verfahrens werden aus Fig. 4 und 5 deutlich.The advantages of this method are clear from FIGS. 4 and 5.
Fig. 4 zeigt Vergleiche der Verbesserung der Effizienz der Ölgewinnung in Abhängigkeit
von der Durchsatzleistung. Fig. 5 veranschaulicht ferner, daß bei der Olivenölgewinnung
mit einer erfindungsgemäßen Schnecke 1 der Restölgehalt im Trester
um bis zu 2 oder sogar 2,5 % gesenkt werden konnte. Die Wirtschaftlichkeit
der Ölgewinnung wird also gegenüber der bereits hervorragenden Resultat der
Zweiphasen-Trennung a) Öl und b) Wasser/Feststoff nochmals beachtlich gesteigert.
Der Umbau oder Austausch der herkömmlichen Schnecke gegen die erfindungsgemäße
amortisiert sich damit bereits in kurzer Zeit.Fig. 4 shows comparisons of improving the efficiency of oil recovery in dependence
from the throughput. Fig. 5 further illustrates that in olive oil production
with a
Fig. 6a,b zeigen die Geschwindigkeitsprofile in einem Schneckengang im Bereich der Aussparungen und Blattsegmente. In Fig. 6a wird deutlich, daß "im Schatten" des Blattsegmentes die Geschwindigkeit der Teilchen von innen nach außen zunimmt. Am oberen Rand des Blattsegmentes wird der Maximalwert erreicht, welcher gemäß Fig. 6b am oberen Blattsegmentrand wiederum im wesentlichen konstant ist.Fig. 6a, b show the velocity profiles in a helix in the area the recesses and leaf segments. In Fig. 6a it is clear that "in the shade" of the leaf segment, the velocity of the particles increases from the inside to the outside. At the upper edge of the leaf segment, the maximum value is reached, which According to Fig. 6b at the upper leaf segment edge again substantially constant is.
Verschiedene Abmessungen sowie Ausrichtungen und Anordnungen der Aussparungen
27 und der Blattsegmente 29 haben sich in der Praxis besonders bewährt.
Durch Variation dieser Parameter lassen sich auch die Mischeffekte zwischen den
Schneckengänge variieren, was einen direkten Einfluß auf die Effizienz der Trennverfahren
hat. Diese Parameter werden nachfolgend unter Bezug auf die Fig. 1 und
2 noch näher beschrieben. Different dimensions and orientations and arrangements of the
Zunächst sei die bevorzugte Lage der Aussparungen und Segment näher beschrieben.First, the preferred location of the recesses and segment described in more detail.
Vorteilhaft weist die Schnecke 1 - in Fig. 1 aus der hinteren Einlaufzone nach vorne
zum konischen Abschnitt hin betrachtet - zunächst einige Wendelgänge x-1, x,
x+1 auf, in deren Bereich das Schneckenblatt 5 jeweils durchgehend bzw. aussparungsfrei
ausgebildet ist. Vorzugsweise sind wenigstens ein oder zwei Schneckengänge
x durchgehend ausgebildet. In diesem Bereich sind auch keine zusätzlichen
Blattsegmente 29 in der Förderbahn 7 vorgesehen.Advantageously, the screw 1 - in Fig. 1 from the rear inlet zone forward
looking at the conical section - at first some turns x-1, x,
x + 1 on, in the area of the
An diese Zone schließen sich einige Schneckengänge x+2, ... x+5 an, welche mit
den Aussparungen 27 versehen sind und in deren Zwischenräumen bzw. in deren
Förderbahnen 7 jeweils die Blattsegmente 29 ausgebildet bzw. aufgestellt (angeschweißt)
sind.This zone is followed by some worm threads x + 2, ... x + 5, which with
the
Diese Zone erstreckt sich maximal bis an den Beginn des konischen Abschnittes 11
der Schnecke 1. Im Übergangsbereich vom zylindrischen zum konischen Bereich
ist ferner die Stauscheibe 13 angeordnet. Im konischen Bereich sollte die Schnecke
aussparungsfrei ausgebildet sein, ferner sollten in der Förderbahn 7 auch keine zusätzlichen
Blattsegmente 29 angeordnet werden.This zone extends maximally to the beginning of the conical section 11th
the
Pro Schneckengang werden vorzugsweise 2 bis 6, insbesondere 3 bis 5, ganz besonders
bevorzugt 4 Aussparungen 27 ausgebildet.Per screw flight are preferably 2 to 6, especially 3 to 5, especially
preferably 4
Entsprechend empfiehlt es sich, pro Schneckengang in der Förderbahn auch vorzugsweise
2 bis 6, insbesondere 3 bis 5, ganz besonders bevorzugt 4 Blattsegmente
29 vorzusehen.Accordingly, it is also recommended, preferably per worm gear in the
Bevorzugt werden die Blattsegmente 29 gleichmäßig am Umfang des Schneckenkörpers
3 verteilt. Preferably, the
Die Schneckengänge x sind relativ zur Mittelachse bzw. zur Symmetrieachse y der
Schnecke 1 jeweils winklig angeordnet bzw. schließen mit der Mittelachse eine
Winkel α auf. Der Betrag des Winkels α (gemessen am unteren Rand des Schnekkenblattes
5), liegt vorzugsweise zwischen 60 und 85°, insbesondere bei 75 bis 80°.The worm threads x are relative to the central axis or to the axis of
Vorzugsweise schließen die Blattsegmente dagegen mit der Symmetrieachse y einen
Winkel δ ein der kleiner als α ist. Vorzugsweise liegt δ zwischen 40 und 70°,
insbesondere 50 bis 55°. Im letzten Schneckengang vor der Stauscheibe 13 empfiehlt
es sich dagegen, die Blattsegmente 29 im wesentlichen parallel zu dem
Schneckenblatt 5 auszurichten (max. Differenzwinkel zwischen α und δ vorzugsweise
ca. 10 - 11°).Preferably, however, the blade segments close with the symmetry axis y a
Angle δ one smaller than α. Preferably, δ is between 40 and 70 °,
in particular 50 to 55 °. In the last flight in front of the baffle plate 13 recommends
on the other hand, the
Vorzugsweise beträgt die Fläche der Aussparungen etwa 50° der Scheckengangfläche.Preferably, the surface of the recesses is about 50 ° of the checkered surface.
In der Praxis hat es sich ferner als vorteilhaft herausgestellt, die Winkelgröße δ
dadurch festzulegen, daß die Breite des Abstandes d (in axialer Verlängerung der
Kanten betrachtet) zwischen dem Blattsegmentrand und dem Aussparungsrand 27
bei 0 bis 5mm, insbesondere bei 2 bis 3 mm liegt (am oberen Segmentrand). Bei
einer Trapezform der Blattsegmente variiert die Größe der Strecken "d" vom
Schneckenkörper 3 nach außen hin, nach Fig. 1 wird "d" nach außen hin beispielsweise
größer.In practice, it has also proved to be advantageous, the angle size δ
specify that the width of the distance d (in the axial extension of the
Seen edges) between the leaf segment edge and the recess edge 27th
at 0 to 5mm, especially at 2 to 3 mm (at the upper edge of the segment). at
a trapezoidal shape of the leaf segments varies the size of the stretches "d" of
Ferner ist es vorteilhaft, wenn die Winkelgröße (δ) dadurch festgelegt ist, daß die
Breite des Abstandes (a) - in orthogonaler Verlängerung der Kanten betrachtet -
zwischen dem Blattlängsrand und dem Aussparungsrand 27 bei 0 bis 28%, insbesondere
bei 15 bis 25 % des Abstandes eines Schneckengangpaares beträgt - vorzugsweise
am Fußpunkt der Schnecke (innen) betrachtet, abhängig von der Form -
liegt.Furthermore, it is advantageous if the angular size (δ) is determined by the fact that the
Width of the distance (a) - viewed in orthogonal extension of the edges -
between the blade longitudinal edge and the
Nach einer Variante der Erfindung empfiehlt es sich, das Blattsegment 29 derart in
der Förderbahn 7 anzuordnen, daß seine Mittelachse M (in der Draufsicht der Fig.
2a) genau in der Mitte der Förderbahn 7 sowie vorzugsweise auch in der Mitte der
Verbindungslinie der Verbindungslinie der Mittelsenkrechten der Aussparungen 27
liegt (Kreuzungspunkt der gegenüberliegenden Aussparungsränder).According to a variant of the invention, it is recommended that the
Alternativ ist es auch möglich, den Mittelpunkt der Blattsegmente etwas gegenüber dieser Ideallage zu verschieben.Alternatively, it is also possible to slightly oppose the midpoint of the leaf segments to shift this ideal situation.
Ganz besonders entscheidend für die Effizienz der Erfindung ist die Höhe h der Blattsegmente (gemessen vom Außenumfang des Schneckenkörpers 3).Especially important for the efficiency of the invention is the height h of the Blade segments (measured from the outer circumference of the screw body 3).
Hier hat es sich als besonders vorteilhaft herausgestellt, wenn die Höhe h der
Blattsegmente 29 derart gewählt ist, daß sie sich bis in den Bereich der Feststoffzone
erstrecken. Entsprechend sollten die Schneckenblätter 5 Aussparungen 27 aufweisen,
welche radial zumindest den Bereich der Feststoffzone überragen.Here it has proved to be particularly advantageous if the height h of
Dies sei wie folgt erläutert. Bei der Zentrifugaltrennung lagern sich die Feststoffe
relativ weit außen in der Trommel an. Reichen die Blattsegmente (Paddel) nicht
wenigstens bis in diese Feststoffzone herein, bleibt ihre Effizienz gering. Gerade
durch die Mischwirkung der Aussparungen 27 und Blattsegmente 29 in diesem Bereich
wird die Effizienz der Zentrifugaltrennung bei der Ölgewinnung deutlich gesteigert.This is explained as follows. In the centrifugal separation, the solids are stored
relatively far out in the drum. The blade segments (paddle) are not enough
at least into this solid zone, their efficiency remains low. Just
by the mixing action of the
In der Praxis wird die Höhe h ca. 30 mm niedriger gewählt als die Schneckenblatthöhe
k. Das Schneckenblatt schließt mit der Umfangswandung des Schnekkenkörpers
3 nach Fig. 2b ferner einen Winkel γ ein. Dieser ist vorzugsweise kleiner
als der Winkel β, den das Blattsegment 29 mit dem Schneckenkörper 3 einschließt. In practice, the height h is selected about 30 mm lower than the Schneckenblatt height
k. The worm blade closes with the peripheral wall of the
- Schneckeslug
- 11
- Schneckenkörperscrew body
- 33
- Schneckenblattscrew blade
- 55
- Schneckengängescrew flights
- x, x+1, x+2 usw.x, x + 1, x + 2, and so on.
- Förderbahnconveyor track
- 77
- zylindrischer Abschnittcylindrical section
- 99
- verjüngender Abschnittrejuvenating section
- 1111
- Scheibedisc
- 1313
- Schleudergutcentrifuged
- SS
- Einlaufrohrinlet pipe
- 1414
- Einlaufkammerinlet chamber
- 1515
- Öffnungenopenings
- 1717
- Trommelraumdrum space
- 1919
- Trommeldrum
- 2121
- Feststoffsolid fuel
- FF
- Feststoffaustragsolids
- 2323
- Überlaufoverflow
- 2525
- Aussparungenrecesses
- 2727
- Kanälechannels
- KK
- Blattsegmenteleaf segments
- 2929
- Restabschnitteremaining sections
- 3030
- Winkelangle
- α, β,δ,γα, β, δ, γ
- Segmenthöhesegment height
- hH
- SchneckenblatthöheScrew blade height
- kk
- Trommel- und SchneckenachseDrum and screw axis
- yy
- Abständedistances
- dd
Claims (36)
- Screw for a solid-bowl screw-type centrifuge, having the following:characterized in thata screw body,at least one screw blade which surrounds the screw body several times and forms several screw spirals (x, x+1),a delivery path for conveying material to be centrifuged being formed between the screw spirals,additional blade segments (29) are arranged in the delivery path (7) in sections between adjacent screw spirals (x, x+1, ...),in the area of the screw blade segments (29), the screw blade (5) is provided with recesses (27) which are formed such that the material (S) to be centrifuged can flow through between adjacent screw spirals (x, x+1, ...).
- Screw according to Claim 1, characterized in that, in its rearward area, the screw body (3) has a cylindrical section (9) and, in its adjoining forward area, has a section (11) which tapers essentially conically uniformly or nonuniformly, the recesses (27) and the blade segments (29) being formed only in the area of the cylindrical section (9).
- Screw according to Claim 1 or 2, characterized in that, in the cylindrical section (9), the screw body first has at least one screw spiral which is formed without recesses and blade segments, and which is followed by additional screw spirals (X, X+1 ... ) which are provided with the recesses (27) and blade segments (29).
- Screw according to Claim 3, characterized in that optional oil drainage ducts are formed preferably in the first screw spiral (X).
- Screw according to Claim 3 or 4, characterized in that the section with the recesses (27) and the blade segments (29) extends to the conically tapering section (11) but not into it.
- Screw according to one of the preceding claims, characterized in that, at the beginning of the conically tapering section (11), a retarding disc (13) is placed on the screw body (3).
- Screw according to one of the preceding claims, characterized in that the inlet of the screw is formed at the rearward end of the cylindrical section (9).
- Screw according to one of the preceding claims, characterized in that the recesses (27) are formed on the screw (1) in such a way as to form, in the axial direction, at least one axial duct (K) which extends over several screw spirals (x+1, ...) and/or a duct which is angular with respect to the centre axis of the screw (1) and/or a zigzag-type duct.
- Screw according to one of the preceding claims, characterized in that the blade segments (29) are formed in that, when material is cut off for forming the recesses (27), the resulting blade sections are placed as blade segments (29) in the delivery path (7) and are fastened there.
- Screw according to one of the preceding claims, characterized in that the recesses have a residual section (30) of the screw blade (5) on the circumference of the screw body (3).
- Screw according to one of the preceding claims, characterized in that two to six recesses (27) are formed for each screw spiral.
- Screw according to one of the preceding claims, characterized in that three to five recesses (27) are formed for each screw spiral.
- Screw according to one of the preceding claims, characterized in that two to six blade segments (29) are provided for each screw spiral in the delivery path.
- Screw according to one of the preceding claims, characterized in that three to five blade segments (29) are provided for each screw spiral in the delivery path (7).
- Screw according to one of the preceding claims, characterized in that, relative to one or more screw spirals, the blade segments (29) are uniformly distributed on the circumference of the screw body (3).
- Screw according to one of the preceding claims, characterized in that, relative to one or more screw spirals, the blade segments (29) are non-uniformly distributed on the circumference of the screw body (3).
- Screw according to one of the preceding claims, characterized in that, relative to the centre axis (Y) of the screw (1), the screw spirals (X) are arranged at an angle to form an angle (α) with this centre axis, the magnitude of the angle (α) preferably being between 60 and 85, particularly at 75° to 80°, the blade segments enclosing an angle (δ), which is smaller than (α), with the axis (Y) .
- Screw according to one of the preceding claims, characterized in that that angle (δ) is between 40 and 70°.
- Screw according to one of the preceding claims, characterized in that the angle (δ) is at 45 to 60°.
- Screw according to one of the preceding claims,. characterized in that, in the last screw spiral in front of the retarding disc (13), the blade segments (29) are aligned essentially parallel to the screw blade (5) and have a maximal differential angle with respect to the angle (α) of 10 to 11°.
- Screw according to one of the preceding claims, characterized in that the area of the recesses (27) amounts to approximately 25 to 60% of the screw spiral area.
- Screw according to one of the preceding claims, characterized in that the area of the recesses (27) amounts to approximately 40 to 50% of the screw spiral area.
- Screw according to one of the preceding claims, characterized in that the angle size (δ) is defined such that the width of the distance (d)- viewed in an axial extension of the edges - between the longitudinal blade edge and the edge of the recess (27) is >=0.
- Screw according to one of the preceding claims, characterized in that the distance d - viewed from the screw body (3)- varies with increasing height of the blade segment (29) and particularly becomes smaller.
- Screw according to one of the preceding claims, characterized in that the angle size (δ) is defined such that the width of the distance (a) - viewed in the orthogonal extension of the edges - between the longitudinal edge of the blade and the edge (27) of the recess amounts to 0 to 28%, particularly to 15 to 25%, of the distance of a pair of screw spirals, preferably viewed at the low end of the screw, as a function of the shape.
- Screw according to one of the preceding claims, characterized in that the blade segment (29) is arranged in the delivery path (7) such that its centre axis (M) is situated precisely in the centre of the delivery path (7) as well as in the centre of the connection line of the apothem of the recesses (27).
- Screw according to one of the preceding claims, characterized in that the centre point of the blade segments (29) is slightly shifted with respect to the centre of the delivery path and/or the centre of the connection line of the apothem of the recess (27).
- Screw according to one of the preceding claims, characterized in that the height (h) of the blade segments (29), viewed from the circumference of the screw body (3), is selected such that the blade segments (29) extend into the area of the solids zone during the centrifugal separation.
- Screw according to one of the preceding claims, characterized in that the recesses (27) in the screw blades (5) are formed such that they radially project at least over the area of the solids zone.
- Screw according to one of the preceding claims, characterized in that the height (h) of the blade segments (29) is approximately 0-30% less than the height (k) of the screw blade.
- Screw according to one of the preceding claims, characterized in that the radial extent of the recesses amounts to 70-95%, preferably 70-100%, of the height (k) of the screw blade.
- Screw according to one of the preceding claims, characterized in that the blade segments (29) are formed as rectangular metal plates.
- Screw according to one of the preceding claims, characterized in that the blade segments (29) are formed as rectangular, trapezoidal, rounded elements and/or elements shaped to taper or widen from the screw body toward the outside.
- Screw according to one of the preceding claims, characterized in that the screw blade (5) encloses an angle (y) with the circumferential wall of the screw body (3), which angle (γ) is smaller than the angle (β) which the blade segment (29) encloses with the screw body (3).
- Method for extracting oil from fruit or seeds, characterized in that the oil is directly separated as a liquid phase in a two-phase separating step from a second mixing phase of water and solids,the reduced fruit, such as olives or avocados or seeds, being first guided in a solid-bowl screw-type centrifuge through a separating zone with one or more screw spirals (X ...) in which the screw blade (5) is preferably formed without recesses, preferably no blade segments (29) being formed in the delivery path in the delivery path area between the screw spirals,then passing through a screw area in the separating zone, in which screw area the recesses (27) are formed in the screw blade (5) and the blade segments (29) are formed in the delivery path (7),then the solids and the water being conveyed past a retarding disc (13) out of the separating zone into the conical section (9) of the screw (1) and the oil being conveyed in the opposite direction out of the screw (1).
- Method of extracting oil from fruit or seeds, characterized in that the oil is separated as a liquid phase in a three-phase separating step from a second phase - essentially consisting of water - and a third phase - essentially consisting of solids,the reduced fruit, such as olives or avocados or seeds, being first guided in a solid-bowl screw-type centrifuge through a separating zone with one or more screw spirals (X ...) in which the screw blade (5) is preferably formed without recesses, preferably no blade segments (29) being formed in the delivery path in the delivery path area between the screw spirals,then passing through a screw area in the separating zone, in which screw area the recesses (27) are formed in the screw blade (5) and the blade segments (29) are formed in the delivery path (7),then the three phases being guided/conveyed essentially separately out of the centrifuge.
Applications Claiming Priority (3)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| DE10055798 | 2000-11-10 | ||
| DE10055798A DE10055798A1 (en) | 2000-11-10 | 2000-11-10 | Screw for a solid bowl screw centrifuge and process for oil extraction with a solid bowl screw centrifuge |
| PCT/EP2001/012069 WO2002038278A1 (en) | 2000-11-10 | 2001-10-18 | Screw for a screw-type solid bowl centrifuge and method for producing oil using such a screw-type solid bowl centrifuge |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| EP1337343A1 EP1337343A1 (en) | 2003-08-27 |
| EP1337343B1 true EP1337343B1 (en) | 2005-02-09 |
Family
ID=7662853
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| EP01993375A Expired - Lifetime EP1337343B1 (en) | 2000-11-10 | 2001-10-18 | Screw for a screw-type solid bowl centrifuge and method for producing oil using such a screw-type solid bowl centrifuge |
Country Status (10)
| Country | Link |
|---|---|
| US (1) | US6908423B2 (en) |
| EP (1) | EP1337343B1 (en) |
| JP (1) | JP2004512945A (en) |
| AR (1) | AR031307A1 (en) |
| AT (1) | ATE288790T1 (en) |
| DE (2) | DE10055798A1 (en) |
| DK (1) | DK1337343T3 (en) |
| ES (2) | ES1048837Y (en) |
| PT (1) | PT1337343E (en) |
| WO (1) | WO2002038278A1 (en) |
Families Citing this family (17)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE10055798A1 (en) * | 2000-11-10 | 2002-05-23 | Westfalia Separator Ind Gmbh | Screw for a solid bowl screw centrifuge and process for oil extraction with a solid bowl screw centrifuge |
| DE20208119U1 (en) * | 2002-05-24 | 2002-08-14 | Hiller GmbH, 84137 Vilsbiburg | Decanter centrifuge for the extraction of fruit or vegetable juices |
| US7001324B2 (en) * | 2003-01-08 | 2006-02-21 | Hutchison Hayes, L. P. | Method of retrofitting a decanting centrifuge |
| JP2006124424A (en) * | 2004-10-26 | 2006-05-18 | Miyoshi Oil & Fat Co Ltd | Oil and fat separation treatment method |
| DE102005061461A1 (en) * | 2005-12-22 | 2007-07-05 | Westfalia Separator Ag | Solid bowl-helical conveyor centrifuge for separating oil from solid/water mixture, exhibits rotatable drum with a tapering cylindrical area, and a rotatable helical conveyor with a conveyor body surrounded by main conveyor sheet |
| DE102006056934A1 (en) * | 2006-11-30 | 2008-06-05 | Westfalia Separator Ag | Method for the centrifugal clarification of an oily sand |
| DE102010027598A1 (en) | 2010-07-20 | 2012-01-26 | Gea Mechanical Equipment Gmbh | Process for clarifying a wine-laundromat |
| CN102199891B (en) * | 2011-05-17 | 2013-05-01 | 江西洪都精工机械有限公司 | Combined rotor with functions of helical propelling and stirring breaking and manufacturing method |
| ES2754754T3 (en) * | 2011-10-28 | 2020-04-20 | Flottweg Se | Solid jacketed screw centrifuge with one screw |
| KR101508057B1 (en) | 2013-07-19 | 2015-04-07 | 주식회사 일성 | A Vacuum dranage pump |
| KR101490746B1 (en) | 2014-06-09 | 2015-02-06 | 주식회사 화인 | Centrifugal dehydrator |
| CN109482370A (en) * | 2018-12-20 | 2019-03-19 | 上海市离心机械研究所有限公司 | A kind of decanter centrifuge helical structure mutually extracted for olive oil oil |
| KR102170275B1 (en) * | 2019-01-30 | 2020-10-26 | 백도선 | dredging soil treating system |
| DE102019102623A1 (en) | 2019-02-04 | 2020-08-06 | Gea Mechanical Equipment Gmbh | Process for clarifying a suspension of solids |
| CN111729763B (en) * | 2020-07-27 | 2025-03-18 | 坚纳森(青岛)机械有限公司 | Centrifuge rotor structure |
| CN112827665B (en) * | 2021-01-21 | 2024-11-22 | 江苏巨能机械有限公司 | Screw conveyor with auxiliary blades and screw discharge sedimentation centrifuge |
| TWM640656U (en) * | 2022-12-29 | 2023-05-01 | 何人東 | Labor-saving and anti-loosening screw |
Family Cites Families (16)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB733515A (en) * | 1952-05-28 | 1955-07-13 | Separator Ab | Improvements in or relating to the separating of liquids and solids |
| JPS57194061A (en) * | 1981-05-26 | 1982-11-29 | Kobe Steel Ltd | Centrifugal concentrating device |
| DE3301099A1 (en) * | 1983-01-14 | 1984-12-06 | KHD Humboldt Wedag AG, 5000 Köln | Apparatus for dehumidifying sludge in the centrifugal field of a solid bowl centrifuge |
| DE3318793A1 (en) * | 1983-05-24 | 1985-01-24 | KHD Humboldt Wedag AG, 5000 Köln | DEVICE FOR DEHUMIDIFYING SLUDGE |
| GB8620436D0 (en) * | 1986-08-22 | 1986-10-01 | Mozley R H | Centrifugal solids-liquids separator |
| ATE114508T1 (en) * | 1988-06-24 | 1994-12-15 | Mozley Ltd Richard | SOLID LIQUID SEPARATOR. |
| US5222935A (en) * | 1991-06-21 | 1993-06-29 | Flottweg Gmbh | Centrifuge with a screw and bristles for separating a suspension into a solids phase and at least one liquid phase |
| DE4132593A1 (en) * | 1991-09-30 | 1993-04-01 | Linde Kca Dresden Gmbh | REACTOR FOR COUNTERFLOW TREATMENT OF SOLID AND LIQUID |
| DE4132693A1 (en) | 1991-10-01 | 1993-04-08 | Messer Griesheim Gmbh | METHOD AND DEVICE FOR PRODUCING POWDERS |
| DE4206006C1 (en) | 1992-02-27 | 1993-09-16 | Westfalia Separator Ag, 59302 Oelde, De | |
| US5354255A (en) * | 1992-12-17 | 1994-10-11 | Alfa Laval Separation Inc. | Decanter centrifuge with conveyor capable of high speed and higher flow rates |
| IT1269436B (en) * | 1994-01-17 | 1997-04-01 | Nuova Maip Macchine Agric | PROCEDURE FOR OBTAINING MUST FROM GRAPES OF GRAPES INCLUDING AT LEAST A CENTRIFUGAL PHASE OF THE BUNCH |
| SE505557C2 (en) | 1995-12-21 | 1997-09-15 | Alfa Laval Separation Ab | decanter |
| DE10055798A1 (en) * | 2000-11-10 | 2002-05-23 | Westfalia Separator Ind Gmbh | Screw for a solid bowl screw centrifuge and process for oil extraction with a solid bowl screw centrifuge |
| DE20208119U1 (en) * | 2002-05-24 | 2002-08-14 | Hiller GmbH, 84137 Vilsbiburg | Decanter centrifuge for the extraction of fruit or vegetable juices |
| ES2217926B1 (en) * | 2002-05-28 | 2006-02-16 | Josep Sallent Soler | CONTINUOUS PROCESS FOR OBTAINING OLIVE OIL WITH VACUUM EXTRACTION OR NEGATIVE PRESSURE. |
-
2000
- 2000-11-10 DE DE10055798A patent/DE10055798A1/en not_active Withdrawn
-
2001
- 2001-04-04 ES ES200100838U patent/ES1048837Y/en not_active Expired - Fee Related
- 2001-10-18 US US10/311,874 patent/US6908423B2/en not_active Expired - Fee Related
- 2001-10-18 DE DE50105332T patent/DE50105332D1/en not_active Expired - Lifetime
- 2001-10-18 EP EP01993375A patent/EP1337343B1/en not_active Expired - Lifetime
- 2001-10-18 DK DK01993375T patent/DK1337343T3/en active
- 2001-10-18 PT PT01993375T patent/PT1337343E/en unknown
- 2001-10-18 WO PCT/EP2001/012069 patent/WO2002038278A1/en not_active Ceased
- 2001-10-18 AT AT01993375T patent/ATE288790T1/en not_active IP Right Cessation
- 2001-10-18 ES ES01993375T patent/ES2233712T3/en not_active Expired - Lifetime
- 2001-10-18 JP JP2002540851A patent/JP2004512945A/en active Pending
- 2001-11-07 AR ARP010105218A patent/AR031307A1/en unknown
Also Published As
| Publication number | Publication date |
|---|---|
| AR031307A1 (en) | 2003-09-17 |
| ES1048837U (en) | 2001-10-01 |
| PT1337343E (en) | 2005-04-29 |
| DE50105332D1 (en) | 2005-03-17 |
| ES2233712T3 (en) | 2005-06-16 |
| EP1337343A1 (en) | 2003-08-27 |
| ES1048837Y (en) | 2002-02-16 |
| DE10055798A1 (en) | 2002-05-23 |
| WO2002038278A1 (en) | 2002-05-16 |
| DK1337343T3 (en) | 2005-05-30 |
| US6908423B2 (en) | 2005-06-21 |
| US20030129042A1 (en) | 2003-07-10 |
| JP2004512945A (en) | 2004-04-30 |
| ATE288790T1 (en) | 2005-02-15 |
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