EP0815929B1 - Static mixer - Google Patents
Static mixer Download PDFInfo
- Publication number
- EP0815929B1 EP0815929B1 EP96810441A EP96810441A EP0815929B1 EP 0815929 B1 EP0815929 B1 EP 0815929B1 EP 96810441 A EP96810441 A EP 96810441A EP 96810441 A EP96810441 A EP 96810441A EP 0815929 B1 EP0815929 B1 EP 0815929B1
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- EP
- European Patent Office
- Prior art keywords
- chambers
- mixer
- mixing
- strings
- passages
- 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
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- 230000003068 static effect Effects 0.000 title claims abstract description 8
- 238000011144 upstream manufacturing Methods 0.000 claims abstract description 3
- 238000001746 injection moulding Methods 0.000 claims description 2
- 238000012546 transfer Methods 0.000 abstract description 5
- 230000000694 effects Effects 0.000 abstract description 2
- 230000008707 rearrangement Effects 0.000 description 10
- 239000000203 mixture Substances 0.000 description 3
- 230000002787 reinforcement Effects 0.000 description 3
- 238000013517 stratification Methods 0.000 description 3
- 230000009466 transformation Effects 0.000 description 3
- 238000011161 development Methods 0.000 description 2
- 230000018109 developmental process Effects 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 230000006855 networking Effects 0.000 description 2
- 238000012545 processing Methods 0.000 description 2
- 229920001817 Agar Polymers 0.000 description 1
- 230000001419 dependent effect Effects 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 230000007246 mechanism Effects 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
Images
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F25/00—Flow mixers; Mixers for falling materials, e.g. solid particles
- B01F25/40—Static mixers
- B01F25/42—Static mixers in which the mixing is affected by moving the components jointly in changing directions, e.g. in tubes provided with baffles or obstructions
- B01F25/43—Mixing tubes, e.g. wherein the material is moved in a radial or partly reversed direction
- B01F25/431—Straight mixing tubes with baffles or obstructions that do not cause substantial pressure drop; Baffles therefor
- B01F25/4315—Straight mixing tubes with baffles or obstructions that do not cause substantial pressure drop; Baffles therefor the baffles being deformed flat pieces of material
- B01F25/43151—Straight mixing tubes with baffles or obstructions that do not cause substantial pressure drop; Baffles therefor the baffles being deformed flat pieces of material composed of consecutive sections of deformed flat pieces of material
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F25/00—Flow mixers; Mixers for falling materials, e.g. solid particles
- B01F25/40—Static mixers
- B01F25/42—Static mixers in which the mixing is affected by moving the components jointly in changing directions, e.g. in tubes provided with baffles or obstructions
- B01F25/43—Mixing tubes, e.g. wherein the material is moved in a radial or partly reversed direction
- B01F25/432—Mixing tubes, e.g. wherein the material is moved in a radial or partly reversed direction with means for dividing the material flow into separate sub-flows and for repositioning and recombining these sub-flows; Cross-mixing, e.g. conducting the outer layer of the material nearer to the axis of the tube or vice-versa
- B01F25/4321—Mixing tubes, e.g. wherein the material is moved in a radial or partly reversed direction with means for dividing the material flow into separate sub-flows and for repositioning and recombining these sub-flows; Cross-mixing, e.g. conducting the outer layer of the material nearer to the axis of the tube or vice-versa the subflows consisting of at least two flat layers which are recombined, e.g. using means having restriction or expansion zones
Definitions
- the invention relates to a static mixer with a Bundle of chambered strands.
- each of the mixing elements includes two axial sections, each section at least one divider dividing the section assigned.
- the dividers of the two sections intersect and divide the pipe cross section into Subareas that are essentially the same size.
- Sub-areas covered by deflection disks are provided and in such a way that exactly on both sides of each divider an open partial area is arranged.
- Relationships that on the one hand neighboring dividers cross and on the other hand the open areas are mutually offset.
- each a mixing-active chamber according to an alternative Assign definition of an open partial area.
- the two closed chamber ends and the neighboring ones Side walls, the passages to other chambers are contained by the deflection plates or formed by the dividers.
- Multiflux mixers contain a linear arrangement of Mixing elements, each with two channels. Everyone of these channels continuously narrows in Flow direction to the middle of the mixing element (Confuser); it widens behind the narrowest part again continuously (diffuser) in a 90 ° rotated level.
- a flowing through the mixing element Medium undergoes a transformation through which the number of partial layers doubled. This transformation continues together from a "cutting" of the medium at the entry into the mixing element in two partial flows, a "upsetting” (in Confuser), a “spread” (in the diffuser) and one Merging the partial streams. Ideally, this is done “Cutting” in such a way that a current with a uniform layering perpendicular to the layers is cut so that after the forming continues an even stratification - with a doubled number Sub-layers - present.
- the static mixer shown in Fig.1 consists of a mixer structure 1 arranged in a tube 10 is.
- the mixer structure 1 is composed of mixing elements 1 'together, each consisting of two dividers 2, 2' and there are two deflection disks 3, 3 '.
- the geometric structure of the mixer structure 1 - see Figures 2 and 2a - can be viewed as one in the z-axis direction oriented bundle of chambered strands A, B, Describe C and D.
- the names for the chambers are A1, A2, ... B1, B2, ... C1, C2, ... and D1, D2, ...
- These chambers are "mixed”; they extend into Direction of the tube 10 between two closed Ends e1, e2, and two adjacent side walls the mixing chamber contain four alternate arranged passages a1, b1, a2 and b2 (with each areas marked with a cross in Fig. 2).
- the chamber C2 is through passages a1 and b1 with the two upstream chambers A1, B1 and via the Passages a2 and b2 with the two downstream Chambers A2, B2 connected. All are in the mixer of Fig.1 Mixing chambers. In general, however, one Mixing chamber also with other chambers (Rearrangement or intermediate chambers, see below) be connected.
- the strands A and B - to be seen as cross sections in Fig.2a - have the same structure; by a 180 ° turn the z-axis (or center line 5) can be used with strand A. the line B are brought to congruence.
- the Strands of a pair A, B are each with the another strand pair C, D via the chamber passages a1, ... connected.
- the two strand pairs differ in that the chambers of one versus those of another offset by half a chamber length in the z direction are arranged.
- Arrows 6a, 6b, 7a and 7b in FIG. 1 indicate reshaped like the medium to be mixed in chamber C2 becomes.
- Two media flows emerge from strands A and B. through the entrance passages a1 (arrows 6a, 6b) and a2 (Arrows 7a, 7b) in the chamber C2 and thus in the strand C a, unite there and influence each other simultaneously moving through chamber C2.
- the remaining partial flow (Arrows 6b, 7b) enters via the exit passage b2 strand B.
- there is an even one Redistribution as indicated by the arrows, where each arrow has an equal amount transported mix corresponds.
- the chambers of the mixer structure 1 are essentially cuboid and the passages rectangular.
- the walls are plate-shaped.
- the walls have to not have constant wall thicknesses. You can for example, be wedge-shaped, as shown in Fig.3 is illustrated.
- the chamber S1 has two entry passages a1 and b1 and an exit passage t1.
- the passage t1 forms the connection to an intermediate chamber T (or Transfer chamber), which has only one entry, namely the Passage t1, and an outlet t2 (not visible) having.
- A is arranged diametrically to T. corresponding intermediate chamber T 'with an access t1' and an exit t2 '.
- FIG. 6 shows a second embodiment of the Mixer structure according to the invention, in pairs existing rearrangement chambers S1, S2 'and S1', S2 are immediately adjacent.
- Fig. 10 shows another means by which a contribution to The object of the invention can be achieved can. It is the following: most of the Passages between neighboring mix-active chambers are laterally limited by the tube 10; to Flow control are individual passages by a rib 11 arranged in the tube 10 limited. Through this rib 11 is mixed material that along the pipe wall flows into the interior of the pipe 10 redirected. This improves the mixing quality.
- Figures 1 to 12 relate to mixers whose Mixing chambers are arranged in four strands. Such a mixer corresponds to the first Embodiment that in the aforementioned Registration has been described; he is in the schematic representation chosen there again in Fig. 13 shown. The other two embodiments are shown in Figures 14 and 15.
- Fig. 13 the two upper levels represent the limits between adjacent axial sections that represent the Have mixing elements. There are two open ones as well as two covered by deflection disks 3, 3 ' Partial areas; and the open partial areas 4, 4 ' offset from each other.
- the lower level gives the designations A, B, C and D of the four chambered Strands on. The same applies to the mixer Figures 14 and 15.
- Mixers according to Fig. 14 contain bundles of nine in Strands arranged in the direction of the tube, six of these strands, namely A, C, B, D, B 'and C', contain mixing-effective chambers and the remaining three Strands that are not labeled, intermediate chambers contain the indirect connections between produce mixing-effective chambers.
- the in the corner strands have arranged intermediate chambers - like the one above called transfer chambers T and T '- two each Passages to neighboring chambers.
- the intermediate chambers the central strand each contain four Passages that are arranged in a ring.
- Mixers according to Fig. 15 contain bundles of sixteen in Strands arranged in the direction of the tube, being eight of these strands, namely A, C, B, D, A ', B', C 'and D', contain mixing-effective chambers and the remaining eight Strands contain intermediate chambers that are indirect Establish connections between mixing-effective chambers.
- the intermediate chambers point again as in the example of Fig. 14 two or four passes to neighboring Chambers on.
- the mixer according to the invention can be manufactured that the bundle of chambered strands A, B, ... in shape a monolithic, especially by injection molding manufactured structure is present.
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- Chemical & Material Sciences (AREA)
- Dispersion Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Processing And Handling Of Plastics And Other Materials For Molding In General (AREA)
- Accessories For Mixers (AREA)
- Disintegrating Or Milling (AREA)
Abstract
Description
Die Erfindung betrifft einen statischen Mischer mit einem Bündel von gekammerten Strängen.The invention relates to a static mixer with a Bundle of chambered strands.
In der nicht vorveröftentlierten EP-A- 0 749 776 ist ein statischer Mischer beschrieben, der nach einem ähnlichen Prinzip wie die bekannten Multiflux- und ISG-Mischer funktioniert; für seine Herstellung wird aber wesentlich weniger Material benötigt. Ein derartiger Mischer, der mit Vorteil zur Behandlung von hochviskosen Medien verwendet wird, besteht aus einem Rohr und einer Vielzahl von in diesem Rohr angeordneten Mischelementen. Jedes der Mischelemente umfasst zwei axiale Abschnitte, wobei jedem Abschnitt mindestens ein den Abschnitt unterteilender Trennsteg zugeordnet ist. Die Trennstege der beiden Abschnitte kreuzen sich und unterteilen den Rohrquerschnitt in Teilflächen, die im wesentlichen gleich gross sind. Bei der Grenze zwischen den Abschnitten sind offene sowie durch Umlenkscheiben abgedeckte Teilfächen vorgesehen und zwar so, dass auf beiden Seiten jedes Trennstegs genau eine offene Teilfläche angeordnet ist. Bezüglich aufeinander folgender Mischelemente bestehen die Beziehungen, dass einerseits benachbarte Trennstege sich kreuzen und andererseits die offenen Teilflächen gegeneinander versetzt angeordnet sind.In the not pre-published EP-A-0 749 776 is a static mixer described on a principle similar to that well-known Multiflux and ISG mixer works; For however, its production becomes much less material needed. Such a mixer, which is advantageous for Treatment of highly viscous media is used consists of a tube and a variety of in it Pipe arranged mixing elements. Each of the mixing elements includes two axial sections, each section at least one divider dividing the section assigned. The dividers of the two sections intersect and divide the pipe cross section into Subareas that are essentially the same size. At the boundary between the sections are open as well Sub-areas covered by deflection disks are provided and in such a way that exactly on both sides of each divider an open partial area is arranged. In terms of successive mixing elements exist Relationships that on the one hand neighboring dividers cross and on the other hand the open areas are mutually offset.
Die in der genannten
EP-A-0 749 776 beschriebenen
Ausführungsbeispiele entsprechen auch der alternativen
Definition des Oberbegriffs von Anspruch 1. Dabei ist
jeweils eine mischaktive Kammer gemäss alternativer
Definition einer offenen Teilfläche zuzuordnen. Die zwei
geschlossenen Kammerenden und die benachbarten
Seitenwände, die Durchgänge zu weiteren Kammern
enthalten, werden durch die Umlenkscheiben
beziehungsweise durch die Trennstege gebildet.Those in the above
EP-A-0 749 776
Embodiments also correspond to the alternative
Definition of the preamble of
Die durch die beiden Definitionen gegebenen Mengen von statischen Mischern sind nicht identisch. Es gibt aber Teilmengen dieser Mengen, für deren Mischer beide Definitionen gelten. Die genannten Ausführungsbeispiele sind Elemente der Teilmengen.The sets of given by the two definitions static mixers are not identical. But there is Subsets of these quantities, for the mixer of which both Definitions apply. The exemplary embodiments mentioned are elements of the subsets.
Multiflux-Mischer enthalten eine lineare Anordnung von Mischelementen, die jeweils zwei Kanäle aufweisen. Jeder dieser Kanäle verengt sich kontinuierlich in Strömungsrichtung bis zur Mitte des Mischelements (Konfusor); hinter der engsten Stelle erweitert er sich wieder kontinuierlich (Diffusor) und zwar in einer um 90° gedrehten Ebene. Ein durch das Mischelement fliessendes Medium erfährt eine Umformung, durch die sich die Anzahl von Teilschichten verdoppelt. Diese Umformung setzt sich zusammen aus einem "Schneiden" des Mediums am Eintritt in das Mischelement in zwei Teilströme, einem "Stauchen" (im Konfusor), einem "Ausbreiten" (im Diffusor) sowie einem Zusammenführen der Teilströme. Im Idealfall erfolgt das "Schneiden" jeweils so, dass ein Strom mit einer gleichmässigen Schichtung senkrecht zu den Schichten geschnitten wird, so dass nach der Umformung weiterhin eine gleichmässige Schichtung - mit verdoppelter Anzahl Teilschichten - vorliegt.Multiflux mixers contain a linear arrangement of Mixing elements, each with two channels. Everyone of these channels continuously narrows in Flow direction to the middle of the mixing element (Confuser); it widens behind the narrowest part again continuously (diffuser) in a 90 ° rotated level. A flowing through the mixing element Medium undergoes a transformation through which the number of partial layers doubled. This transformation continues together from a "cutting" of the medium at the entry into the mixing element in two partial flows, a "upsetting" (in Confuser), a "spread" (in the diffuser) and one Merging the partial streams. Ideally, this is done "Cutting" in such a way that a current with a uniform layering perpendicular to the layers is cut so that after the forming continues an even stratification - with a doubled number Sub-layers - present.
In den mischaktiven Kammern der gattungsgemässen Mischern erfolgt eine entsprechende Umformung der zu behandelnden Medien, allerdings ohne dass dabei Konfusoren und Diffusoren für diese Umformung nötig sind.In the mixing-active chambers of the generic mixers the treatment to be treated is carried out accordingly Media, but without confusors and Diffusers are necessary for this transformation.
Bei der Mischung zweier Medien, die verschiedene Werte der Viskosität aufweisen, beobachtet man Abweichungen von dem idealen Mischmechanismus: Nach Durchlauf mehrerer Mischelemente sind Teilschichten, die am Rand der Schichtung liegen, wesentlich dicker als die übrigen Teilschichten.When mixing two media, the different values of viscosity, deviations from the ideal mixing mechanism: after passing through several Mixing elements are sub-layers on the edge of the Layering are much thicker than the rest Sub-layers.
Es ist Aufgabe der Erfindung, den gattungsgemässen
Mischer derart zu ändern, dass Abweichungen von der
idealen Mischwirkung zumindest teilweise beseitigt
werden. Diese Aufgabe wird dadurch gelöst, dass im
Mischer "Umlagerungskammern" vorgesehen sind, durch die
erreicht wird, dass randständige Teilschichten in das
Innere der Schichtung umgelagert werden. Anspruch 1
definiert einen derartigen Mischer mit Umlagerungszellen.
Die abhängigen Ansprüche 2 bis 11 beziehen sich auf
verschiedene Ausführungsformen des erfindungsgemässen
Mischers.It is an object of the invention, the generic
Modify mixer so that deviations from the
ideal mixing effect at least partially eliminated
become. This task is solved in that in
Mixers "rearrangement chambers" are provided by the
is achieved that marginal sub-layers in the
Interior of the stratification.
Nachfolgend wird die Erfindung anhand der Zeichnungen erläutert. Es zeigen:
- Fig. 1
- einen Abschnitt einer Mischerstruktur, die nur mischwirksame Kammern aufweist,
- Fig. 2
- den geometrische Aufbau der Mischerstruktur gemäss Fig.1,
- Fig. 2a
- einen Querschnitt durch die Struktur der Fig.2,
- Fig. 3
- eine erste Modifikation der in Fig.1 gezeigten Mischerstruktur,
- Fig. 4
- eine zweite Modifikation,
- Fig. 5
- eine erste erfindungsgemässe Mischerstruktur mit Umlagerungskammern,
- Fig. 6
- eine zweite erfindungsgemässe Mischerstruktur mit Umlagerungskammern,
- Fig. 7
- eine Abwicklung der an der Peripherie gelegenen Kanten der Mischerstruktur gemäss Fig.1 in die Ebene,
- Fig. 8
- eine entsprechende Abwicklung für eine Mischerstruktur gemäss Fig.5,
- Fig. 9
- eine Abwicklung für eine Mischerstruktur gemäss Fig.6,
- Fig. 10
- eine Mischerstruktur mit einem zusätzlichen vorteilhaften Strukturelement,
- Fig. 11
- eine erste seitlich verstärkte Mischerstruktur,
- Fig. 12
- eine zweite Mischerstruktur mit seitlicher Verstärkung,
- Fig. 13
- eine schematische Darstellung zu einer Mischerstruktur mit einem Bündel von vier gekammerten Strängen,
- Fig. 14
- eine schematische Darstellung zu einer Mischerstruktur mit neun gekammerten Strängen und
- Fig. 15
- eine schematische Darstellung zu einer Mischerstruktur mit sechzehn gekammerten Strängen.
- Fig. 1
- a section of a mixer structure which has only mixing-effective chambers,
- Fig. 2
- the geometric structure of the mixer structure according to FIG. 1,
- Fig. 2a
- 3 shows a cross section through the structure of FIG. 2,
- Fig. 3
- a first modification of the mixer structure shown in Figure 1,
- Fig. 4
- a second modification,
- Fig. 5
- a first mixer structure according to the invention with rearrangement chambers,
- Fig. 6
- a second mixer structure according to the invention with rearrangement chambers,
- Fig. 7
- development of the edges of the mixer structure located on the periphery according to FIG. 1 into the plane,
- Fig. 8
- a corresponding processing for a mixer structure according to FIG. 5,
- Fig. 9
- a processing for a mixer structure according to Figure 6,
- Fig. 10
- a mixer structure with an additional advantageous structural element,
- Fig. 11
- a first laterally reinforced mixer structure,
- Fig. 12
- a second mixer structure with side reinforcement,
- Fig. 13
- 1 shows a schematic representation of a mixer structure with a bundle of four chambered strands,
- Fig. 14
- a schematic representation of a mixer structure with nine chambered strands and
- Fig. 15
- a schematic representation of a mixer structure with sixteen chambered strands.
Der in Fig.1 dargestellte statische Mischer besteht aus
einer Mischerstruktur 1, die in einem Rohr 10 angeordnet
ist. Die Mischerstruktur 1 setzt sich aus Mischelementen
1' zusammen, die jeweils aus zwei Trennstegen 2, 2' und
zwei Umlenkscheiben 3, 3' bestehen. In der Ebene der
Umlenkscheiben 3, 3' befinden sich zwei offene
Teilflächen 4, 4' (äussere Grenzen 4a, 4a'), die auch als
Durchgangslöcher bezeichnet worden sind.The static mixer shown in Fig.1 consists of
a
Der geometrische Aufbau der Mischerstruktur 1 - siehe
Figuren 2 und 2a - lässt sich als ein in Richtung der z-Achse
orientiertes Bündel von gekammerten Strängen A, B,
C und D beschreiben. Die Bezeichnungen für die Kammern
sind A1, A2, ... B1, B2, ... C1, C2, ... und D1, D2, ...
Diese Kammern sind "mischwirksam"; sie erstrecken sich in
Richtung des Rohrs 10 jeweils zwischen zwei geschlossenen
Enden e1, e2, und zwei zueinander benachbarte Seitenwände
der mischwirksamen Kammer enthalten vier wechselständig
angeordnete Durchgänge a1, b1, a2 und b2 (mit jeweils
einem Kreuz gekennzeichnete Flächen in Fig.2). Die Kammer
C2 ist über die Durchgänge a1 und b1 mit den zwei
stromaufwärts liegenden Kammern A1, B1 sowie über die
Durchgänge a2 und b2 mit den zwei stromabwärts liegenden
Kammern A2, B2 verbunden. Im Mischer der Fig.1 sind alle
Kammern mischwirksam. Im allgemeinen kann jedoch eine
mischwirksame Kammer auch mit anderen Kammern
(Umlagerungs- oder Zwischenkammern, siehe weiter unten)
verbunden sein. The geometric structure of the mixer structure 1 - see
Figures 2 and 2a - can be viewed as one in the z-axis direction
oriented bundle of chambered strands A, B,
Describe C and D. The names for the chambers
are A1, A2, ... B1, B2, ... C1, C2, ... and D1, D2, ...
These chambers are "mixed"; they extend into
Direction of the
Die Stränge A und B - als Querschnitte in Fig.2a zu sehen - haben den gleichen Aufbau; durch eine 180°-Drehung um die z-Achse (oder Mittellinie 5) kann der Strang A mit dem Strang B zur Deckung gebracht werden. Die gleiche Beziehung besteht zwischen den Strängen C und D. Die Stränge des einen Paares A, B sind jeweils mit dem anderen Strangpaar C, D über die Kammerdurchgänge a1, ... verbunden. Die beiden Strangpaare unterscheiden sich dadurch, dass die Kammern des einen gegenüber jenen des anderen in z-Richtung um eine halbe Kammerlänge versetzt angeordnet sind.The strands A and B - to be seen as cross sections in Fig.2a - have the same structure; by a 180 ° turn the z-axis (or center line 5) can be used with strand A. the line B are brought to congruence. The same Relationship exists between strands C and D. The Strands of a pair A, B are each with the another strand pair C, D via the chamber passages a1, ... connected. The two strand pairs differ in that the chambers of one versus those of another offset by half a chamber length in the z direction are arranged.
Durch Pfeile 6a, 6b, 7a und 7b in Fig.1 ist angedeutet,
wie das zu mischende Medium in der Kammer C2 umgeformt
wird. Zwei Medienströme treten aus den Strängen A und B
durch die Eintrittsdurchgänge a1 (Pfeile 6a, 6b) und a2
(Pfeile 7a, 7b) in die Kammer C2 und damit in den Strang
C ein, vereinigen sich dort und beeinflussen sich dabei
gleichzeitig in ihrer Bewegung durch die Kammer C2. An
der Kante 20 bei dem Austrittsdurchgang a2 erfolgt eine
Abtrennung eines ersten Teilstroms (Pfeile 6a, 7a), der
in den Strang A übertritt. Der verbleibende Teilstrom
(Pfeile 6b, 7b) gelangt über den Austrittsdurchgang b2 in
den Strang B. Im Idealfall gibt es eine gleichmässige
Umverteilung, wie sie durch die Pfeile angedeutet ist,
wobei jedem Pfeil eine gleich grosse Menge an
transportiertem Mischgut entspricht.
Die Kammern der Mischerstruktur 1 sind im wesentlichen
quaderförmig und die Durchgänge rechteckig. Die Wände
sind plattenförmig ausgebildet. Die Wände müssen aber
nicht konstante Wandstärken aufweisen. Sie können
beispielsweise keilförmig ausgebildet sein, wie dies in
Fig.3 illustriert ist. The chambers of the
Damit der im Mischgut durch die Mischerstruktur erzeugte Druckabfall kleiner ist als bei der Mischerstruktur der Fig.1, können für die Wände auch gebogene Formen vorgesehen werden, wie dies in Fig.4 dargestellt ist.So that the generated in the mix by the mixer structure Pressure drop is smaller than with the mixer structure Fig.1, curved shapes can also be used for the walls be provided, as shown in Fig.4.
Zusätzlich zu den mischwirksamen Kammern enthält die
Mischerstruktur 1 erfindungsgemäss "Umlagerungskammern"
S1, S2 - siehe Fig.5 - und S1', S2' (in Fig.5 nicht
sichtbar). Die Kammer S1 hat zwei Eintrittsdurchgänge a1
und b1 sowie einen Austrittsdurchgang t1. Der Durchgang
t1 bildet die Verbindung zu einer Zwischenkammer T (oder
Transferkammer), die nur einen Eintritt, nämlich den
Durchgang t1, und einen Austritt t2 (nicht sichtbar)
aufweist. Diametral zu T angeordnet ist eine
entsprechende Zwischenkammer T' mit einem Zutritt t1' und
einem Austritt t2'. Die Zwischenkammern T und T' führen
weiter zu Umlagerungskammern S2' (nicht sichtbar)
beziehungsweise S2, die jeweils einen Eintrittsdurchgang
und zwei Austrittsdurchgänge enthalten. Für S2 sind diese
Durchgänge die mit t2' beziehungsweise a2 und b2
bezeichneten Durchgänge. Die Kammern S1 und S2'
beziehungsweise S1' und S2 bilden jeweils ein durch eine
Transferkammer T, T' verbundenes Paar. In diesen
Kammerpaaren findet eine Umlagerung der Schichtung statt,
die zu der erfindungsgemässen Verbesserung der Mischgüte
führt. In der zweiten Umlagerungskammer S2, S2' findet
gleichzeitig ein weiterer Mischschritt statt.In addition to the mixing-effective chambers, the contains
Fig.6 zeigt eine zweite Ausführungsform der erfindungsgemässen Mischerstruktur, bei der paarweise vorliegende Umlagerungskammern S1, S2' und S1', S2 unmittelbar benachbart sind.6 shows a second embodiment of the Mixer structure according to the invention, in pairs existing rearrangement chambers S1, S2 'and S1', S2 are immediately adjacent.
Anhand der Schrägbilder der Figuren 1, 5 und 6 ist die
Vernetzung der einzelnen Kammern nur schwer oder gar
nicht in ihrer Gesamtheit ersichtlich. Diese Vernetzung
lässt sich gut erkennbar machen, in dem man die
Mischerstrukturen 1 über deren Umfang in die Ebene
abwickelt. Solche Abwicklungen sind in den Figuren 7 bis
9 dargestellt. Die beiden seitlichen Ränder, die parallel
zur z-Achse verlaufen, werden jeweils durch den Strang B
mit den Kammern B1, B2, B3, ... in Fig.7, B1, T', B2, ...
in Fig.8 und B1, S1', B2 ... in Fig.9 gebildet.Based on the oblique images of Figures 1, 5 and 6
Networking of the individual chambers is difficult or even impossible
not visible in their entirety. This networking
can be made easily recognizable by the
Die mäanderartigen Linien in den Figuren 7 bis 9 stellen
die äusseren Wandkanten der Mischerstrukturen 1 dar. Die
äusseren Ecken der Umlenkscheiben 3, 3' (Fig.1) sind
nicht markiert; sie liegen jeweils in der Mitte der
horizontalen Strecken der mäanderartigen Linien. Durch
Pfeile ist der Fluss des Mischgutes angedeutet: schräg
stehende Pfeile bei den Eintrittsstellen der Kammern,
horizontale bei den Austrittsstellen. In Fig.7 (vgl.
Fig.1) sind alle Kammern äquivalent; es sind
mischwirksame Kammern. In Fig.8 sind besonders die
Kammeranordnungen S1 - T - S2' und S1' - T' - S2 zu
beachten (vgl. Fig.5). In Fig.9 sind besonders die
Kammeranordnungen S1 - S2' und S1' - S2 zu beachten (vgl.
Fig.6).Make the meandering lines in Figures 7 to 9
represent the outer wall edges of the
Fig.10 zeigt ein weiteres Mittel, mit dem ein Beitrag zur
Lösung der erfindungsgemässen Aufgabe geleistet werden
kann. Es handelt sich um folgendes: die meisten der
Durchgänge zwischen benachbarten mischaktiven Kammern
sind seitlich durch das Rohr 10 begrenzt; zur
Strömungslenkung sind einzelne der Durchgänge jeweils
durch eine bei dem Rohr 10 angeordneten Rippe 11
begrenzt. Durch diese Rippe 11 wird Mischgut, das entlang
der Rohrwand fliesst, in das Innere des Rohrs 10
umgelenkt. Dadurch verbessert sich die Mischgüte.Fig. 10 shows another means by which a contribution to
The object of the invention can be achieved
can. It is the following: most of the
Passages between neighboring mix-active chambers
are laterally limited by the
Da mit dem erfindungsgemässen Mischer in der Regel
hochviskose Medien behandelt werden, entstehen grosse
Druckgradienten in Richtung der z-Achse entlang der
Mischerstruktur 1. Diese Druckgradienten verringern sich,
wenn die Wandstärken verkleinert werden. Bei dünnen
Wänden der Mischerstruktur 1 besteht allerdings die
Gefahr, dass die Struktur zerdrückt wird. Mit geeigneten
Verstärkungsmitteln lässt sich die Mischerstruktur 1 in
eine stabilere Form bringen. Die Figuren 11 und 12 zeigen
Verstärkungen durch Streifen 12 und 13, die an der
Peripherie der Mischerstruktur 1 in z-Richtung angeordnet
sind. Solche Verstärkungen lassen sich natürlich auch für
Mischerstrukturen vorsehen, die keine erfindungsgemässen
Umlagerungskammern enthalten.As a rule with the mixer according to the invention
highly viscous media are treated, large
Pressure gradients in the direction of the z-axis along the
Die Figuren 1 bis 12 beziehen sich auf Mischer, deren mischwirksamen Kammern in vier Strängen angeordnet sind. Ein derartiger Mischer entspricht dem ersten Ausführungsbeispiel, das in der eingangs genannten Anmeldung beschrieben worden ist; er ist in der dort gewählten schematischen Darstellungsform nochmals in Fig.13 gezeigt. Die beiden anderen Ausführungsbeispiele sind in den Figuren 14 und 15 dargestellt.Figures 1 to 12 relate to mixers whose Mixing chambers are arranged in four strands. Such a mixer corresponds to the first Embodiment that in the aforementioned Registration has been described; he is in the schematic representation chosen there again in Fig. 13 shown. The other two embodiments are shown in Figures 14 and 15.
In Fig.13 stellen die zwei oberen Ebenen die Grenzen
zwischen benachbarten axialen Abschnitten dar, welche die
Mischelemente aufweisen. Dabei liegen jeweils zwei offene
sowie zwei durch Umlenkscheiben 3, 3' abgedeckte
Teilfächen vor; und die offenen Teilflächen 4, 4' sind
gegeneinander versetzt angeordnet. Die untere Ebene gibt
die Bezeichnungen A, B, C und D der vier gekammerten
Stränge an. Entsprechendes gilt für die Mischer der
Figuren 14 und 15.In Fig. 13 the two upper levels represent the limits
between adjacent axial sections that represent the
Have mixing elements. There are two open ones
as well as two covered by
Mischer gemäss Fig.14 enthalten Bündel mit neun in Richtung des Rohrs angeordneten Strängen, wobei sechs dieser Stränge, nämlich A, C, B, D, B' und C', mischwirksame Kammern umfassen und die restlichen drei Stränge, die nicht bezeichnet sind, Zwischenkammern enthalten, die indirekte Verbindungen zwischen mischwirksamen Kammern herstellen. Die in den Ecksträngen angeordneten Zwischenkammern haben - wie die oben genannten Transferkammern T und T' - jeweils zwei Durchgänge zu benachbarten Kammern. Die Zwischenkammern des zentralen Strangs enthalten jeweils vier solche Durchgänge, die ringförmig angeordnet sind.Mixers according to Fig. 14 contain bundles of nine in Strands arranged in the direction of the tube, six of these strands, namely A, C, B, D, B 'and C', contain mixing-effective chambers and the remaining three Strands that are not labeled, intermediate chambers contain the indirect connections between produce mixing-effective chambers. The in the corner strands have arranged intermediate chambers - like the one above called transfer chambers T and T '- two each Passages to neighboring chambers. The intermediate chambers the central strand each contain four Passages that are arranged in a ring.
Mischer gemäss Fig.15 enthalten Bündel mit sechzehn in Richtung des Rohrs angeordneten Strängen, wobei acht dieser Stränge, nämlich A, C, B, D, A', B', C' und D', mischwirksame Kammern umfassen und die restlichen acht Stränge Zwischenkammern enthalten, die indirekte Verbindungen zwischen mischwirksamen Kammern herstellen. Die Zwischenkammern weisen wieder wie beim Beispiel der Fig.14 jeweils zwei oder vier Durchgänge zu benachbarten Kammern auf.Mixers according to Fig. 15 contain bundles of sixteen in Strands arranged in the direction of the tube, being eight of these strands, namely A, C, B, D, A ', B', C 'and D', contain mixing-effective chambers and the remaining eight Strands contain intermediate chambers that are indirect Establish connections between mixing-effective chambers. The intermediate chambers point again as in the example of Fig. 14 two or four passes to neighboring Chambers on.
Der erfindungsgemässe Mischer kann so gefertigt sein, dass das Bündel der gekammerten Stränge A, B, ... in Form einer monolithischen, insbesondere durch Spritzguss hergestellten Struktur vorliegt.The mixer according to the invention can be manufactured that the bundle of chambered strands A, B, ... in shape a monolithic, especially by injection molding manufactured structure is present.
Claims (10)
- Static mixer with a bundle of chambered strings (A, B, ...) which at least partly comprise mixing-active chambers (A1, A2, ...), with the bundle being arranged in a tube, the mixing-active chambers extending in the direction (5) of the tube in each case between two closed ends (e1, e2), and two mutually adjacent side walls of the mixing-active chambers (C2) containing four alternately disposed passages (a1, b1, a2, b2) which produce connections to two chambers lying upstream (A1, B2) and to two chambers lying downstream (A2, B2) respectively, wherein chambers are furthermore arranged between at least two sections of the static mixer which contain mixing-active chambers, namely re-layering chambers (S1, S1', S2, S2') which have two closed ends and three lateral passages to adjacent chambers.
- Mixer in accordance with claim 1 characterised in that the re-layering chambers (S1, S1', S2, S2') occur in pair-wise connection and that a direct or an indirect connection between them is provided via one of the passages in each case.
- Mixer in accordance with claim 2 characterised in that the pair connections at least of individual re-layering chambers is provided indirectly via an intermediate chamber (T) that has two closed ends and two lateral passages.
- Mixer in accordance with one of the claims 1 to 3 characterised in that the bundle has four chambered strings (A, B, C, D), in that all mixing-active chambers (A1, ...) are substantially formed alike and in that adjacent strings connected via chamber passages contain chambers which are each arranged so as to be displaced by half a chamber length in the direction of the tube with respect to one another.
- Mixer in accordance with one of the claims 1 to 3 characterised in that the bundle has nine chambered strings (A, B, B', C, C', D, ...), six of these strings comprising mixing-active chambers and the remaining three strings containing intermediate chambers which produce indirect connections between mixing-active chambers.
- Mixer in accordance with one of the claims 1 to 3 characterised in that the bundle has sixteen chambered strings (A, A', B, B', C, C', D, D', ...), eight of these strings comprising mixing-active chambers and the remaining eight strings containing intermediate chambers which produce indirect connections between mixing-active chambers.
- Mixer in accordance with one of the claims 1 to 6 characterised in that most of the passages (a1, ...) between adjacent mixing-active chambers (A1, ...) are laterally bounded by the tube (10); and in that some individual passages are in each case bounded by a rib (11) arranged at the tube for deflecting the flow.
- Mixer in accordance with one of the claims 1 to 7 characterised in that the chambers (A1, ...) have substantially the form of rectangular prisms and the passages (a1, ...) are substantially rectangular.
- Mixer in accordance with one of the claims 1 to 8 characterised in that the bundle of chambered strings (A, ...) is reinforced by strips (13) which are arranged at the periphery of the bundle in the direction of the tube (10).
- Mixer in accordance with one of the claims 1 to 9 characterised in that the bundle of chambered strings (A, ...) is present in the form of a monolithic structure, in particular one produced by injection moulding.
Priority Applications (7)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
EP96810441A EP0815929B1 (en) | 1996-07-05 | 1996-07-05 | Static mixer |
ES96810441T ES2151650T3 (en) | 1996-07-05 | 1996-07-05 | STATIC MIXER. |
DE29623909U DE29623909U1 (en) | 1996-07-05 | 1996-07-05 | Static mixer with a bundle of chambered strands |
DE59605822T DE59605822D1 (en) | 1996-07-05 | 1996-07-05 | Static mixer |
AT96810441T ATE195889T1 (en) | 1996-07-05 | 1996-07-05 | STATIC MIXER |
US08/871,317 US5851067A (en) | 1996-07-05 | 1997-06-09 | Static mixer with a bundle of chambered strings |
JP15398997A JP4031556B2 (en) | 1996-07-05 | 1997-06-11 | Static stirring apparatus having an assembly of a plurality of chamber strings |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
EP96810441A EP0815929B1 (en) | 1996-07-05 | 1996-07-05 | Static mixer |
Publications (2)
Publication Number | Publication Date |
---|---|
EP0815929A1 EP0815929A1 (en) | 1998-01-07 |
EP0815929B1 true EP0815929B1 (en) | 2000-08-30 |
Family
ID=8225644
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP96810441A Expired - Lifetime EP0815929B1 (en) | 1996-07-05 | 1996-07-05 | Static mixer |
Country Status (6)
Country | Link |
---|---|
US (1) | US5851067A (en) |
EP (1) | EP0815929B1 (en) |
JP (1) | JP4031556B2 (en) |
AT (1) | ATE195889T1 (en) |
DE (1) | DE59605822D1 (en) |
ES (1) | ES2151650T3 (en) |
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- 1996-07-05 AT AT96810441T patent/ATE195889T1/en not_active IP Right Cessation
- 1996-07-05 ES ES96810441T patent/ES2151650T3/en not_active Expired - Lifetime
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1997
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WO2022101167A1 (en) | 2020-11-11 | 2022-05-19 | Sulzer Mixpac Ag | An improved static mixing tip |
EP4059979A1 (en) | 2021-03-18 | 2022-09-21 | Sulzer Management AG | A process of continuously manufacturing a poly(hydroxy acid) homo- or copolymer with tunable molecular weight, structure and composition |
WO2022195019A1 (en) | 2021-03-18 | 2022-09-22 | Sulzer Management Ag | A process of continuously manufacturing a poly(hydroxy acid) copolymer with tunable molecular weight, structure and composition |
EP4445978A1 (en) | 2023-04-11 | 2024-10-16 | Sulzer Management AG | A devolatilization apparatus comprising distributors comprising a static mixer |
EP4445980A1 (en) | 2023-04-11 | 2024-10-16 | Sulzer Management AG | A devolatilization apparatus comprising a perforated roof element |
EP4445979A1 (en) | 2023-04-11 | 2024-10-16 | Sulzer Management AG | A multi-stage devolatilization apparatus comprising at least one static mixer |
WO2024213449A1 (en) | 2023-04-11 | 2024-10-17 | Sulzer Management Ag | A devolatilization apparatus comprising distributors comprising a static mixer |
WO2024213470A1 (en) | 2023-04-11 | 2024-10-17 | Sulzer Management Ag | A devolatilization apparatus comprising a perforated roof element |
WO2024213471A1 (en) | 2023-04-11 | 2024-10-17 | Sulzer Management Ag | A multi-stage devolatilization apparatus comprising at least one static mixer |
Also Published As
Publication number | Publication date |
---|---|
ATE195889T1 (en) | 2000-09-15 |
US5851067A (en) | 1998-12-22 |
ES2151650T3 (en) | 2001-01-01 |
JP4031556B2 (en) | 2008-01-09 |
DE59605822D1 (en) | 2000-10-05 |
EP0815929A1 (en) | 1998-01-07 |
JPH1057791A (en) | 1998-03-03 |
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