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EP0815929B1 - Static mixer - Google Patents

Static mixer Download PDF

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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
Authority
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
Application number
EP96810441A
Other languages
German (de)
French (fr)
Other versions
EP0815929A1 (en
Inventor
Markus Fleischli
Rolf Heusser
Felix Streiff
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Sulzer Chemtech AG
Original Assignee
Sulzer Chemtech AG
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Priority to AT96810441T priority Critical patent/ATE195889T1/en
Priority to EP96810441A priority patent/EP0815929B1/en
Priority to ES96810441T priority patent/ES2151650T3/en
Priority to DE29623909U priority patent/DE29623909U1/en
Priority to DE59605822T priority patent/DE59605822D1/en
Application filed by Sulzer Chemtech AG filed Critical Sulzer Chemtech AG
Priority to US08/871,317 priority patent/US5851067A/en
Priority to JP15398997A priority patent/JP4031556B2/en
Publication of EP0815929A1 publication Critical patent/EP0815929A1/en
Application granted granted Critical
Publication of EP0815929B1 publication Critical patent/EP0815929B1/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F25/00Flow mixers; Mixers for falling materials, e.g. solid particles
    • B01F25/40Static mixers
    • B01F25/42Static mixers in which the mixing is affected by moving the components jointly in changing directions, e.g. in tubes provided with baffles or obstructions
    • B01F25/43Mixing tubes, e.g. wherein the material is moved in a radial or partly reversed direction
    • B01F25/431Straight mixing tubes with baffles or obstructions that do not cause substantial pressure drop; Baffles therefor
    • B01F25/4315Straight mixing tubes with baffles or obstructions that do not cause substantial pressure drop; Baffles therefor the baffles being deformed flat pieces of material
    • B01F25/43151Straight 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
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F25/00Flow mixers; Mixers for falling materials, e.g. solid particles
    • B01F25/40Static mixers
    • B01F25/42Static mixers in which the mixing is affected by moving the components jointly in changing directions, e.g. in tubes provided with baffles or obstructions
    • B01F25/43Mixing tubes, e.g. wherein the material is moved in a radial or partly reversed direction
    • B01F25/432Mixing 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
    • B01F25/4321Mixing 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

A static mixer has a bundle of chambered passages (A,B,C.) which include at least some chambers which bring about a mixing effect. The bundle is located inside a tube, and the mixing chambers are arranged in a series extending in the direction of the axis of the tube, each chamber being bounded by two transverse end walls. Two adjacent side walls of the mixing chambers have four openings (a1, b1,a2,b2) arranged on alternate sides, which create connections with two upstream (A1,B1) and two downstream chambers (A2,B2). Between at least two sections of the mixer which contain mixing chambers, are placed transfer chambers (S1,S2,) which have two closed ends and three side openings to adjoining chambers.

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 claim 1. Here is 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.

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. Claim 1 defines such a mixer with rearrangement cells. The dependent claims 2 to 11 relate to different embodiments of the inventive Mixer.

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.
The invention is explained below with reference to the drawings. Show it:
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 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 '. At the level of Deflection disks 3, 3 'are two open Subareas 4, 4 '(outer boundaries 4a, 4a'), which are also known as Through holes have been designated.

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 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.

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.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. On the edge 20 at the exit passage a2 takes place Separation of a first partial flow (arrows 6a, 7a), the enters strand A. The remaining partial flow (Arrows 6b, 7b) enters via the exit passage b2 strand B. Ideally, there is an even one Redistribution, as indicated by the arrows, where each arrow has an equal amount transported mix corresponds.

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 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.

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 Mixer structure 1 according to the invention “rearrangement chambers” S1, S2 - see Fig. 5 - and S1 ', S2' (not in Fig. 5 visible). 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 '. Lead the intermediate chambers T and T ' continue to rearrangement chambers S2 '(not visible) or S2, each having an entry passage and contain two exit passages. For S2 these are Passages with t2 'or a2 and b2 designated passages. Chambers S1 and S2 ' or S1 'and S2 each form one by one Transfer chamber T, T 'connected pair. In these A rearrangement of the stratification takes place in pairs of chambers, to improve the mixing quality according to the invention leads. In the second rearrangement chamber S2, S2 'takes place another mixing step takes place simultaneously.

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 Mixer structures 1 over their scope in the plane unwinds. Such developments are in Figures 7 to 9 shown. The two side edges that are parallel to the z-axis, are in each case by the strand B with the chambers B1, B2, B3, ... in Fig. 7, B1, T ', B2, ... in Fig. 8 and B1, S1 ', B2 ... in Fig. 9.

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 mixer structures 1 outer corners of the deflection plates 3, 3 '(Fig.1) not marked; they are in the middle of each horizontal stretches of meandering lines. By Arrows indicate the flow of the mix: diagonally arrows standing at the entry points of the chambers, horizontal at the exit points. In Fig. 7 (cf. Fig.1) all chambers are equivalent; there are Mixing chambers. In Fig. 8 are particularly those Chamber arrangements S1 - T - S2 'and S1' - T '- S2 too note (see Fig. 5). In Fig. 9 there are especially those Chamber arrangements S1 - S2 'and S1' - S2 must be observed (cf. Fig. 6).

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 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.

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 Mixer structure 1. These pressure gradients decrease, if the wall thicknesses are reduced. With thin Walls of the mixer structure 1, however, there is Danger of the structure being crushed. With suitable The mixer structure 1 in can be reinforced bring a more stable shape. Figures 11 and 12 show Reinforcements by strips 12 and 13 on the Periphery of the mixer structure 1 arranged in the z direction are. Such reinforcements can of course also be used for Provide mixer structures that are not according to the invention Transfer chambers included.

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 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.

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)

  1. 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.
  2. 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.
  3. 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.
  4. 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.
  5. 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.
  6. 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.
  7. 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.
  8. 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.
  9. 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).
  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.
EP96810441A 1996-07-05 1996-07-05 Static mixer Expired - Lifetime EP0815929B1 (en)

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

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EP0815929A1 EP0815929A1 (en) 1998-01-07
EP0815929B1 true EP0815929B1 (en) 2000-08-30

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US (1) US5851067A (en)
EP (1) EP0815929B1 (en)
JP (1) JP4031556B2 (en)
AT (1) ATE195889T1 (en)
DE (1) DE59605822D1 (en)
ES (1) ES2151650T3 (en)

Cited By (13)

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Publication number Priority date Publication date Assignee Title
EP1125625A2 (en) 2000-02-18 2001-08-22 Schröder & Boos, Misch- und Anlagentechnik GmbH & Co. KG Homogenizer
DE10322922A1 (en) * 2003-05-21 2004-12-16 Fischerwerke Artur Fischer Gmbh & Co. Kg Static mixer, for mixing at least two components with paste consistency, e.g. in plastics injection molding, has successive mixing elements within pipe, with deflectors to move material to center with low flow resistance
US8936391B2 (en) 2008-11-27 2015-01-20 Medmix Systems Ag Static mixer
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Publication number Priority date Publication date Assignee Title
DE19827851A1 (en) * 1998-06-23 1999-12-30 Bayer Ag Static mixing device
EP0993864A1 (en) * 1998-09-18 2000-04-19 Sulzer Chemtech AG Apparatus and method for mixing and dispensing several fluid components
JP2000126569A (en) * 1998-09-18 2000-05-09 Sulzer Chemtech Ag Device for mixing and distributing a plurality of flowing components
GB9910738D0 (en) * 1999-05-11 1999-07-07 Statiflo International Limited Static miker
DE50107866D1 (en) * 2000-02-17 2005-12-08 Sulzer Chemtech Ag Winterthur Static mixer
KR100892864B1 (en) 2001-08-02 2009-04-15 주식회사 엘지생명과학 Processes for the production of amino-protected derivatives of 4-aminomethylene-pyrrolidin-3-one and/or 4-aminomethylene-pyrrolidin-3-alkoxyimino derivatives and/or gemifloxacin or a salt thereof
DE10158651B4 (en) * 2001-11-30 2016-02-04 Ritter Gmbh Static mixing element
ATE242045T1 (en) * 2002-03-22 2003-06-15 Sulzer Chemtech Ag TUBE MIXER WITH A LONGITUDINAL BUILT-IN BODY
US6773156B2 (en) * 2002-07-10 2004-08-10 Tah Industries, Inc. Method and apparatus for reducing fluid streaking in a motionless mixer
US20040141413A1 (en) * 2002-12-06 2004-07-22 Wilhelm A. Keller Static mixer
US7198400B2 (en) * 2003-05-03 2007-04-03 Husky Injection Molding Systems Ltd. Static mixer and a method of manufacture thereof
EP1510247B1 (en) * 2003-08-26 2008-04-30 Sulzer Chemtech AG Static mixer with polymorphous structure
WO2005065808A1 (en) * 2003-12-26 2005-07-21 Shinyou Technologies Inc. Static mixer
JP2007527283A (en) * 2004-02-27 2007-09-27 ヘレーウス クルツァー ゲゼルシャフト ミット ベシュレンクテル ハフツング Method for producing dental impression material and apparatus therefor
DE102004046226A1 (en) * 2004-09-22 2006-04-06 Heraeus Kulzer Gmbh Molding material production system for dentistry has a widened by phone reservoir not separated from the mixing cavity and containing string parts
TWI354577B (en) * 2004-04-22 2011-12-21 Sulzer Chemtech Ag A static mixer for a curing mixed product
ES2309445T3 (en) 2004-12-17 2008-12-16 Borealis Technology Oy PROCESS FOR THE POLYMERIZATION OF OLEFINS IN THE PRESENCE OF A POLYMERIZATION CATALYST OF THE SAME.
KR100711352B1 (en) * 2005-06-23 2007-04-27 삼성전자주식회사 Wavelength-division-multiplexed passive optical network using wavelength-locked optical transmitter
JP4713397B2 (en) * 2006-01-18 2011-06-29 株式会社リコー Microchannel structure and microdroplet generation system
DE202008007801U1 (en) 2007-09-19 2008-08-21 Kettenbach Gmbh & Co. Kg container
US8083397B2 (en) 2008-06-13 2011-12-27 Nordson Corporation Static mixer
US8397495B2 (en) * 2008-06-26 2013-03-19 Tenneco Automotive Operating Company Inc. Exhaust gas additive/treatment system and mixer for use therein
WO2010009233A2 (en) * 2008-07-18 2010-01-21 3M Innovative Properties Company Offset path mixers and fluid systems including the same
US8764279B2 (en) * 2008-07-18 2014-07-01 3M Innovation Properties Company Y-cross mixers and fluid systems including the same
US20110150703A1 (en) * 2008-07-18 2011-06-23 Castro Gustavo H Tortuous path static mixers and fluid systems including the same
SG161141A1 (en) * 2008-10-17 2010-05-27 Sulzer Mixpac Ag Static mixer
US8215940B2 (en) * 2009-03-20 2012-07-10 The United States Of America As Represented By The Secretary Of The Army Layer multiplying apparatus
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DE102009054652A1 (en) * 2009-12-15 2011-06-16 Hilti Aktiengesellschaft Static mixer
WO2011119820A1 (en) 2010-03-25 2011-09-29 Nordson Corporation Inline static mixer
ES2836798T3 (en) 2010-04-28 2021-06-28 Ips Adhesives Llc Apparatus for mixing and dispensing multiple fluid components
WO2011162728A1 (en) * 2010-06-23 2011-12-29 Gluetec Gmbh & Co. Kg Static mixer with asymmetric mixing elements
MX2013000618A (en) 2010-07-20 2013-03-20 Sulzer Mixpac Ag Static spray mixer.
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DE202011050465U1 (en) 2011-06-16 2011-08-17 Vosschemie Gmbh Static mixer for mixing at least two flowable components
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KR20150013276A (en) 2012-05-14 2015-02-04 술저 믹스팩 아게 Spray mixer for mixing and spraying at least two flowable components
US9375692B2 (en) 2012-08-21 2016-06-28 Medmix Systems Ag Mixing device for a discharge unit
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CN113477115B (en) 2015-11-13 2023-12-05 雷米克瑟斯公司 Static mixer
US10232327B2 (en) * 2016-03-03 2019-03-19 Nordson Corporation Flow inverter baffle and associated static mixer and methods of mixing
US9839883B2 (en) * 2016-03-18 2017-12-12 Komax Systems, Inc. Channel mixing apparatus
EP3241611B1 (en) 2016-05-02 2020-03-04 Borealis AG A process for feeding a polymerisation catalyst
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CH713229A1 (en) 2016-12-14 2018-06-15 Streiff Felix Mixing elements with high strength and mixing effect.
DE102017112440A1 (en) * 2017-06-06 2018-12-06 Shin-Etsu Silicones Europe B.V. Container and dosing device for viscous materials
US10722853B2 (en) * 2017-08-04 2020-07-28 Nordson Corporation Static mixer without mixing baffle sidewalls and associated mixing conduit
US11278924B2 (en) * 2017-11-21 2022-03-22 Wagner Spray Tech Corporation Plural component spray gun system
DE202018106654U1 (en) 2018-11-22 2019-02-06 Sulzer Mixpac Ag Static mixer
CH717390A2 (en) 2020-05-06 2021-11-15 Streiff Felix Assemblies / installation elements made of deflection surfaces with separators for installation in pipes / ducts or in the shell of tube bundle heat exchangers.
DE102021105414B9 (en) * 2021-03-05 2022-11-17 Kulzer Gmbh Static mixer for impression materials
EP4282516A1 (en) 2022-05-23 2023-11-29 Henkel AG & Co. KGaA Device and method for spraying a multicomponent plastic material
EP4309772A1 (en) 2022-07-19 2024-01-24 Glue Tec Industrieklebstoffe GmbH & Co. Kg Static mixer
EP4371657A1 (en) 2022-11-18 2024-05-22 medmix Switzerland AG Static mixer
EP4371656A1 (en) 2022-11-18 2024-05-22 medmix Switzerland AG Static mixer with separating means
WO2024189099A1 (en) * 2023-03-13 2024-09-19 Medmix Switzerland Ag Static mixer insert, static mixer and dispensing system
CH720728A2 (en) 2023-04-24 2024-10-31 Streiff Felix Static mixing element with a separating web and deflection surfaces and static mixer

Family Cites Families (15)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
NL229424A (en) * 1958-07-08 1900-01-01
US3239197A (en) * 1960-05-31 1966-03-08 Dow Chemical Co Interfacial surface generator
US3195865A (en) * 1960-09-09 1965-07-20 Dow Chemical Co Interfacial surface generator
JPS39437B1 (en) * 1961-05-31 1964-01-16
US3328003A (en) * 1965-02-09 1967-06-27 Dow Chemical Co Method and apparatus for the generation of a plurality of layers in a flowing stream
US3406947A (en) * 1966-08-19 1968-10-22 Dow Chemical Co Interfacial surface generator
US3620506A (en) * 1970-07-07 1971-11-16 Fmc Corp Fluid-mixing device
US3928199A (en) * 1971-09-20 1975-12-23 Airco Inc Gas absorption system and method
JPS5141940B2 (en) * 1972-03-15 1976-11-12
JPS5233822B2 (en) * 1972-03-18 1977-08-31
US3963221A (en) * 1974-02-28 1976-06-15 Union Carbide Corporation Mixing apparatus
US4040256A (en) * 1976-07-14 1977-08-09 The Dow Chemical Company Flume mixer
JPS601048B2 (en) * 1979-05-02 1985-01-11 東レ株式会社 Pipe structure for forming fluid flow channels
DE3420290C1 (en) * 1984-05-30 1986-01-02 Ritter-Plastic GmbH, 8931 Untermeitingen Static mixing part
JP3181628B2 (en) * 1991-06-18 2001-07-03 巽工業株式会社 Fluid mixing device

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EP1125625A2 (en) 2000-02-18 2001-08-22 Schröder & Boos, Misch- und Anlagentechnik GmbH & Co. KG Homogenizer
DE10322922A1 (en) * 2003-05-21 2004-12-16 Fischerwerke Artur Fischer Gmbh & Co. Kg Static mixer, for mixing at least two components with paste consistency, e.g. in plastics injection molding, has successive mixing elements within pipe, with deflectors to move material to center with low flow resistance
US8936391B2 (en) 2008-11-27 2015-01-20 Medmix Systems Ag Static mixer
EP3342479A1 (en) 2016-12-29 2018-07-04 Sulzer Mixpac AG Static mixer, a kit of parts and use of said static mixer
EP3342478A1 (en) 2016-12-29 2018-07-04 Sulzer Mixpac AG Static mixer, a kit of parts and use of said static mixer
WO2018122171A1 (en) 2016-12-29 2018-07-05 Sulzer Mixpac Ag Static mixer, a kit of parts and use of said static mixer
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US12064738B2 (en) 2016-12-29 2024-08-20 Medmix Switzerland Ag Static mixer, a kit of parts and use of a static mixer
DE102017117198A1 (en) 2017-07-28 2019-01-31 3lmed GmbH mixer
WO2019020764A1 (en) 2017-07-28 2019-01-31 Kettenbach Gmbh & Co. Kg Mixer
EP4000749A1 (en) 2020-11-11 2022-05-25 medmix Switzerland AG An improved static mixing tip
WO2022101167A1 (en) 2020-11-11 2022-05-19 Sulzer Mixpac Ag An improved static mixing tip
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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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