EP1426099B1 - Mélangeur statique et procédé - Google Patents
Mélangeur statique et procédé Download PDFInfo
- Publication number
- EP1426099B1 EP1426099B1 EP03405865A EP03405865A EP1426099B1 EP 1426099 B1 EP1426099 B1 EP 1426099B1 EP 03405865 A EP03405865 A EP 03405865A EP 03405865 A EP03405865 A EP 03405865A EP 1426099 B1 EP1426099 B1 EP 1426099B1
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- EP
- European Patent Office
- Prior art keywords
- mixing
- static mixer
- mixer according
- transversal
- deflecting
- 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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- 238000002156 mixing Methods 0.000 claims abstract description 155
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- 230000008859 change Effects 0.000 description 3
- 238000006073 displacement reaction Methods 0.000 description 3
- 230000008569 process Effects 0.000 description 2
- 230000009467 reduction Effects 0.000 description 2
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Images
Classifications
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- 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
-
- 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
-
- 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
-
- 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
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F2101/00—Mixing characterised by the nature of the mixed materials or by the application field
- B01F2101/2305—Mixers of the two-component package type, i.e. where at least two components are separately stored, and are mixed in the moment of application
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F2215/00—Auxiliary or complementary information in relation with mixing
- B01F2215/04—Technical information in relation with mixing
- B01F2215/0413—Numerical information
- B01F2215/0418—Geometrical information
- B01F2215/0427—Numerical distance values, e.g. separation, position
Definitions
- the present invention relates to a static mixer with a bundle of strands according to the preamble of claim 1.
- a static mixer is for example from US-A-5,851,067 known.
- This patent is in turn a further development of US-A-5,944,419 ,
- These patents disclose a mixer which is subdivided into chambered strands, four chambered strands being formed by four mutually-arranged passageways in the former U.S. Patent, and the mixer further comprising repositioning chambers.
- In the second-mentioned mixer either two intersecting webs or two intersecting web pairs are disclosed with passages which are arranged so that in each case a bottom section plate comes to lie over an opening.
- While such mixers provide better mixing of the materials, based on their length, and have a smaller pressure drop than conventional mix-wound mixers, they have relatively large dead spaces in which the material can cure and clog the mixer.
- FIG. 1 shows a section of a first exemplary embodiment of a mixer 1 according to the invention, which has a number of identical mixing elements 2, 2 'and 2 ", which are each arranged rotated through 180 ° with respect to the longitudinal axis, and at one end is the mixer housing 3 indicated.
- the single mixing element 2 has at one end, viewed in the direction of flow, ie in the drawing from below, a transverse edge 8 on a transverse guide wall 8 'extending perpendicularly thereto two end sections 6 and 7 with the complementary side openings 11 and 12 and a bottom section 9 and complementary bottom section opening 10, the latter being located between two guide walls 4 ', 5' which each open into a separating edge 4, 5 and are aligned here parallel to the longitudinal central axis.
- the termination sections extend over half of the separation edges.
- the openings, or their cross-section, determine with the lengths of the webs substantially the pressure drop from the beginning to the end of the mixer.
- the mixing element 2 'following on mixing element 2 has the same individual parts and structures, but is arranged rotated with respect to the longitudinal axis by 180 ° above the first mixing element 2.
- the following mixing elements are also identical to the mixing element 2 and, viewed in the longitudinal direction, are arranged rotated through 180 ° one behind the other.
- the flow direction is indicated by an arrow 13.
- FIG. 2 shows the distribution of the two components G and H at the mixer inlet, each component originating from a container of a double cartridge or a dispenser having separate outlets, see FIG. 13.
- the mixer inlet is shown below according to the flow direction .
- each component spreads along the transverse guide wall 8 'and are divided by the guide walls 4', 5 'into three strands, so that finally six strands AG, BG, CG and AH, BH and CH arise, these strands in the mixer per a chamber DG, EG, FG; DH, EH, FH can be assigned.
- the six strands reach the next mixing element 2 '.
- the mixed and spread strands AG, BG and CG are displaced through the side openings 11 and 12 on one side of the transverse edge and on the other side of the transverse edge are the spread out strands AH, BH, CH through the bottom opening 10, as indicated schematically in Fig. 3.
- This results in the mixed strands A1.G and C1.G with B1.G and A1.H and C1.H with B1.H A1.1 and C1.1 with B1.1 and A1.2 at the end of element 2 and C1.2 with B1.2 according to the scheme of Figure 3.
- the mixed strands propagate on both sides of the transverse edge.
- the next step is to displace in the other direction, i. Strands A3.1, B3.1 and C3.1 are displaced outwards and A3.2, B3.2 and C3.2 outwards, as is also apparent from FIG. Again, when entering the next element, the components spread out respectively on both halves of the transverse edge, to then be displaced again and move to the next mixing element.
- the arrangement and design of the mixing elements results in a three-part sequence of the mixing process, in which the mass is first divided, then spread out and then displaced, in order then to be divided, spread and displaced again in the next step.
- more than two dividing edges and baffles may be provided, e.g. three separating edges and baffles, which result in more than six strands, the bottoms or openings being mutually offset.
- a transverse edge is present, so that the strands are divided into two parts. The result is an analogous image for a mixing element with more than one transverse edge and more than two partitions.
- the mixer 1 is drawn by 180 ° in the same direction of flow.
- the single mixing element 2 has at one end, seen in the running direction from below, two separating edges 4 and 5, which in each case a guide wall 4 ', 5', which are aligned here parallel to the longitudinal center axis, and the perpendicular thereto, on both sides of the baffles , two end portions 6 and 7 and a bottom portion 9 located between the baffles and extending over half of the baffles.
- a transverse guide wall 8 ' Perpendicular to the end sections, in the middle of the guide walls, a transverse guide wall 8 'is arranged, which has a transverse edge 8 at the other end of the mixing element.
- the bottom section opening 10 between the guide walls and the two side openings 11 and 12 on both sides of the guide walls are complementary to the two end sections and the bottom section.
- the openings, or their cross-section, essentially determine the pressure drop from the beginning to the end of the mixer.
- the mixing element 2 'following on mixing element 2 has the same individual parts and structures and is arranged with respect to the longitudinal axis by 180 ° swept over the first mixing element 2.
- the following mixing elements are also arranged one behind the other with respect to the longitudinal axis by 180 ° in turn.
- the flow direction is indicated by arrow 13.
- FIG. 5 shows the distribution of the two components G and H at the mixer inlet, each component originating from a container of a double cartridge or a dispenser having separate outlets, see FIG. 13.
- the mixer inlet is shown below according to the flow direction .
- the six strands reach the next mixing element 2 '.
- the two strands A1.G with A1.H and B1.G with B1.H and C1.G with C1.H A1.1 with A1.2, B1.1 with B1.2 and C1.1 with C1.2 mixed according to Figure 7, wherein, due to the geometric structure of mixing element 2 strand A1.1 strand A1.2 displaced and passes through side opening 11 through the next mixing element, strand B1.2 strand B1.1 displaced and through the bottom section opening 10 passes through the next mixing element and strand C1.1 strand C1.2 displaced and passes through the side opening 12 through the next mixing element.
- the mixed strands B2.1 and B2.2 spread on one side of the transverse edge 8 on the whole half A2.1 - B2.1 - C2.1 and likewise the two mixed propagate Strands A2.1, A2.2 and C2.1, C2.2 on the other side of transverse edge 8 on the front half in the figure A2.2, B2.2 and C2.2, from.
- the arrangement and design of the mixing elements also results in a three-part flow of the mixing process, in which the mass is first divided and then displaced and finally spread, and then divided again in the next step, displaced and spread.
- the mixers described above not only give a good mixing of the materials, but above all a lower pressure drop and less dead space in comparison to other mixers mentioned above.
- mixers having a rectangular or square cross-section have been described and the two incident components have the same cross-section.
- the separation edges and baffles can be arranged at an angle to each other and likewise the end portions and the bottom portion and the transverse edge can each have an angle to each other, so that the openings need not be rectangular or square.
- edges, for example, the transverse edge have a kink.
- the mixing elements need not be arranged one behind the other with respect to the longitudinal axis in each case rotated by 180 ° to each other, any angle of 0 ° - 360 ° is possible.
- a mixer 14 is shown with a circular cylindrical housing as a special case of a mixer with mixing elements with curved walls, with the mixing elements 15, 15 'and 15' 'and the housing 16.
- the mixing element 15 at one End, seen in the direction of flow below, a transverse edge 21, from the two baffles 17 ', 18' go out, each in a separating edge 17, 18 open.
- the baffles each include a termination portion 19 and 20 with the side openings 24, 25, a bottom portion 22 and a complementary bottom opening 23.
- the individual sections are not defined as clearly as in the first embodiment.
- the two baffles 17 ', 18' are curved from the separating edges 17 and 18 located at one end and continuously into the transverse edge 21 as far as the other end. This curved design of the baffles, or their transition into the transverse edge is apparent from Figure 9, wherein the schematic transition in Figure 12 is shown.
- this second embodiment is the same as in the first example.
- FIG. 12 is to be interpreted analogously to the diagram of FIG. 4, with the difference that the vertical guide walls 4 ', 5' present in FIG. 4 are V-shaped here and transition into the transverse edge.
- the cross-sections or volume flow ratios of the materials G and H can be different from 1: 1, and above all the baffles can assume a multiplicity of geometric shapes from the separating edges to the transverse edge, and the mixing elements can also be reversed with respect to the direction of flow be shown arrangement.
- the mixing principle is maintained each time that mix the middle strands and spread on one side of the transverse edge and then spread the two outer strand pairs each on the other side of the transverse edge.
- FIG. 13 a new mixer arrangement is shown, which yields particularly good values when using the described mixing elements.
- the mixer housing 16 From Figure 13 from the mixer 36, the mixer housing 16, the mixer inlet with the inlets 32 and 33 and the outlet openings 34 and 35 can be seen.
- the leading edge 31 of the first mixing helix element 28 is arranged transversely over the two outlet openings 34, 35.
- the two separating edges of the first mixing element 15 of the first mixing group 27 are arranged transversely to the outlet edge 30 of the first mixing spiral element.
- the first mixing group 27 consists of the mixing elements 15, wherein for example four mixing elements are shown here. This is followed by the second mixing spiral element 28 ', which is followed by a second mixing group 27'.
- This second mixing group also consists of four mixing elements 15 'which, however, are turned 180 ° relative to the first mixing group with respect to the direction of flow, i. with the transverse wall directed against the inlet, with which this group acts in a similar way to that according to FIG. 9.
- the transverse edge 21 of the last mixing element of the mixing group is in each case perpendicular to the inlet edge 31 'of the mixing spiral element 28'.
- the purpose of periodically using a mixing helix element is to efficiently peel the material off the walls and redeploy it, thereby further improving mixing performance.
- the exemplary embodiment according to FIGS. 15-17 is based on the exemplary embodiment according to FIG. 1 with straight element walls, whereby, however, the mixing elements are arranged in a circular-cylindrical housing.
- the mixing elements are arranged in a circular-cylindrical housing.
- several features are given, which both improve the mixing and reduce the dead zones, or their losses and thus allow a much higher total efficiency. Not all of these features must be present simultaneously on all mixing elements or mixing groups.
- Figure 15 shows a mixing element arrangement 40, wherein the housing is not shown, with the inlet part 41 with the inlets 42, 43 and the outlets 42 ', 43' and the mixing part 44 with the mixing elements. Until the first transverse edge 45, the components are separated by a separating web 46.
- five mixing elements 47a-47e are combined in a first mixing group 47, while the second mixing group 48 comprises two mixing elements 48a and 48b and the further mixing group 49 again comprises five mixing elements 49a-49e.
- the flowed through the transverse wall guide walls 50, 51 have a greater height ZL than the height ZQ of the transverse guide walls, z. B. preferably with a factor between 1.1 to 2.0, in particular 1.5.
- This extension of the double baffles results in a better alignment of the material, which gives it more time to spread before it is split again.
- the extension of the double baffles also causes a reduction in the number of mixing elements required to achieve the same or better mixing quality.
- the height ZQ may be 1.1 to 2.0 times greater than the height ZL of the guide walls, in particular 1, 5 times.
- FIG. 17 shows different dead zone closures TZV.
- the bottom portion 9 has a first type of dead zone closures TZV1 directed toward the previous mixing element.
- the mixing elements which do not have bevels, i. the mixing elements 47a-47e and 49a-49e also have dead-zone closures TZV2 on the inwardly facing sides of the bottom sections.
- the baffles 50 and 51 have outwardly third and fourth types of dead zone closures TZV3 and TZV4, which are located where no slanting ridges are disposed.
- wall layers are formed which cause defective layers during strand formation.
- slanted webs are used, which are mounted on the inside and outside of the guide walls.
- these slanting ridges are attached to the middle mixing group 48, and inner slanting ridges 52 and outer slanting ridges 53 are visible, both of which are attached to the baffles 50 and 51 of the mixing elements 48a and 48b.
- Wall layers are formed not only on the baffles but also on the inner wall of the mixer housing.
- longitudinal webs are attached which connect the double guide walls on the outside. These longitudinal webs need not be present in all mixing groups.
- the longitudinal webs 54 are attached to the first and second mixing groups 47, 48, but they could also be attached to the third or any other mixing group, or alternatively as in mixing group 48.
- FIG. 16 shows the flowchart during mixing.
- the two components spread on the respective half of the transverse guide wall 55.
- the right part goes to the center and spreads over the entire length of the baffles 50, 51, while the left part divides into two halves and forms the outer two-thirds.
- these three streams are divided transversely.
- the left half is directed to the center and spreads over the entire length of the baffles, while the right half is split and each half reaches the one and the other side of the baffles, whereupon again follows a transverse edge, etc.
- transverse edges and baffles have no webs such as web 152, which do not change the general mixing principle of the mixing elements.
- a possible doubling of the transverse edge into two parallel transverse walls falls under the definition of a transverse wall, as this does not change the mixing principle either.
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- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Dispersion Chemistry (AREA)
- Transition And Organic Metals Composition Catalysts For Addition Polymerization (AREA)
- Processing And Handling Of Plastics And Other Materials For Molding In General (AREA)
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Claims (19)
- Mélangeur statique comprenant des éléments mélangeurs (2, 2', 2"; 15, 15', 15"; 47a-47e; 48a, 48b, 49a-49e) pour partager la matière à mélanger (G, H) en plusieurs boudins, ainsi que des moyens pour réunir ces derniers sous la forme de couches, avec une arête transversale (8, 21, 45) et des parois de guidage (4', 5', 50, 51) s'étendant à un angle par rapport à l'arête transversale, ainsi que des éléments de guidage agencés à un angle par rapport à l'axe longitudinal et munis d'ouvertures, l'élément mélangeur (2, 2', 2"; 15, 15', 15"; 47a-47e; 48a, 48b; 49a-49e) présentant une arête transversale (8, 21; 45) prolongée d'une paroi de guidage transversale (8', 21'; 55) et au moins deux parois de guidage (4', 5', 50, 51) se terminant par des arêtes de division (4, 5) respectives et munies de sections de clôture (6, 7; 19, 20) latérales et au moins une section de fond (9, 22) agencée entre les parois de guidage, lesquelles définissent au moins une ouverture (10, 23) d'un côté de l'arête transversale (8, 21; 45) et au moins deux ouvertures (11, 12; 24, 25) de l'autre côté de l'arête transversale, caractérisé en ce qu'au moins six boudins sont formés, les deux composants (G, H) qui sont à mélanger étant d'abord partagés en deux ou en au moins trois et ensuite en au moins trois ou en deux boudins, respectivement, selon l'orientation des éléments mélangeurs par rapport à la direction d'écoulement.
- Mélangeur statique selon la revendication 1, caractérisé en ce que les sections des parois de guidage sont planes et agencées à un angle réciproque.
- Mélangeur statique selon la revendication 1 ou 2, caractérisé en ce que le boîtier (3) du mélangeur présente une section transversale ronde.
- Mélangeur statique selon la revendication 1 ou 2, caractérisé en ce que le boîtier (3) du mélangeur présente une section transversale rectangulaire, que lesdites au moins deux arêtes de division (4, 5) prolongées des parois de guidage (4', 5') sont agencées perpendiculairement à au moins une arête transversale (8) de la paroi de guidage transversale (8'), et que les sections latérales de clôture (6, 7) et la section de fond (9) sont agencées perpendiculairement aux parois de guidage.
- Mélangeur statique selon la revendication 1 ou 2, caractérisé en ce que les parois de guidage sont incurvées, lesdites au moins deux parois de guidage (17', 18') avec les arêtes de division (17, 18) à l'une des extrémités de l'élément mélangeur aboutissant à une arête transversale (21) située à l'autre extrémité de l'élément mélangeur.
- Mélangeur statique selon la revendication 5, caractérisé en ce le boîtier (16) du mélangeur est rond et l'élément mélangeur (15, 15', 15") présente au moins deux arêtes de division (17, 18) et une arête transversale (21) avec des parois de guidage (17' 18') qui les relient et présentent deux sections latérales de clôture (19, 20) et au moins une section de fond (22), les parois de guidage de liaison s'incurvant à partir des arêtes de division de manière continue vers l'arête transversale.
- Mélangeur statique selon l'une des revendications 1 à 6, caractérisé en ce que les éléments mélangeurs successifs (2, 2', 2"; 15, 15', 15") sont chaque fois pivotés par rapport à l'axe longitudinal.
- Mélangeur statique selon la revendication 7, caractérisé en ce que les éléments mélangeurs successifs sont chaque fois pivotés de 180° par rapport à l'axe longitudinal.
- Mélangeur statique selon l'une des revendications 1 à 8, caractérisé en ce que des éléments mélangeurs (2, 2', 2"; 15, 15', 15"; 47a-47e; 48a, 48b, 49a-49e) sont regroupés en groupes de mélange (27, 29) et qu'au moins un élément de transposition (28, 28', 28'') est chaque fois interposé entre les groupes de mélange.
- Mélangeur statique selon la revendication 9, caractérisé en ce le mélangeur comprend consécutivement un premier groupe de mélange (27) composé d'éléments mélangeurs (15), lequel est suivi d'un élément de transposition (28) qui est à son tour suivi d'un deuxième groupe de mélange (29), et ainsi de suite, l'arête d'entrée (31) de l'élément de transposition étant essentiellement perpendiculaire à l'arête transversale (21) du dernier élément mélangeur du groupe de mélange, et le deuxième groupe de mélange étant renversé de 180° par rapport à la direction d'écoulement de telle manière que l'arête transversale (21) de l'élément mélangeur (15) est essentiellement perpendiculaire à l'arête de sortie (30) de l'élément de transposition.
- Mélangeur statique selon l'une des revendications 1 à 10, caractérisé en ce que la hauteur (ZL) des parois de guidage (50, 51) est supérieure à la hauteur (ZQ) de la paroi de guidage transversale (55).
- Mélangeur statique selon l'une des revendications 1 à 11, caractérisé en ce que la hauteur (ZQ) de la paroi de guidage transversale (55) est supérieure à la hauteur (ZL) des parois de guidage (50, 51).
- Mélangeur statique selon la revendication 11, caractérisé en ce (ZL) = 1,1 à 2,0 (ZQ), préférablement 1,5 (ZQ).
- Mélangeur statique selon la revendication 12, caractérisé en ce (ZQ) = 1,1 à 2,0 (ZL), préférablement 1,5 (ZL) .
- Mélangeur statique selon la revendication 11 ou 12, caractérisé en ce les parois de guidage (50, 51) comportent à l'intérieur ou à l'extérieur des nervures obliques (52, 53).
- Mélangeur statique selon l'une des revendications 11 à 15, caractérisé en ce que des traverses longitudinales (54) sont agencées entre les parois de guidage de deux éléments mélangeurs voisins.
- Mélangeur statique selon l'une des revendications 1 à 16, caractérisé en ce que les sections de fond (9) et les parois de guidage (50, 51) sont munies d'obturations de zones mortes (TZV1, TZV2, TZV3, TZV4).
- Procédé pour la mise en oeuvre du mélangeur selon l'une des revendications 1 à 17 pour le cas où la matière rencontre l'arête transversale (8, 21, 45) en premier, l'élément mélangeur (2, 2', 2"; 15, 15', 15") étant agencé de manière à partager d'abord le boudin de matière en deux boudins (G, H) pour partager à la sortie les deux boudins en au moins six boudins (AG, BG, CG, AH, BH, CH), deux boudins mélangés (BG avec AG et CG) étant dirigés vers un côté de la paroi transversale (8, 21; 45) et un boudin mélangé (AH et CH avec BH) étant dirigé vers l'autre côté de la paroi transversale pour être ensuite partagés en au moins trois boudins chacun par les parois de guidage.
- Procédé pour la mise en oeuvre du mélangeur selon l'une des revendications 1 à 17 pour le cas où la matière rencontre les arêtes de division (4, 5, 17, 18) des parois de guidage (4', 5'; 17', 18') en premier, l'élément mélangeur (2, 2', 2"; 15, 15', 15") étant agencé de manière à partager le boudin de matière en au moins six boudins (AG, BG, CG, AH, BH, CH) pour diriger une partie des boudins (BG, BH) vers un côté de l'arête transversale (8, 21) et l'autre partie des boudins (AG, AH, CG, CH) vers l'autre côté de l'arête transversale.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
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CH20722002 | 2002-12-06 | ||
CH20722002 | 2002-12-06 |
Publications (3)
Publication Number | Publication Date |
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EP1426099A1 EP1426099A1 (fr) | 2004-06-09 |
EP1426099B1 true EP1426099B1 (fr) | 2007-09-12 |
EP1426099B8 EP1426099B8 (fr) | 2007-10-17 |
Family
ID=32304051
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP03405865A Expired - Lifetime EP1426099B8 (fr) | 2002-12-06 | 2003-12-04 | Mélangeur statique et procédé |
Country Status (12)
Country | Link |
---|---|
US (3) | US20040141413A1 (fr) |
EP (1) | EP1426099B8 (fr) |
JP (1) | JP4704676B2 (fr) |
KR (1) | KR101010872B1 (fr) |
CN (1) | CN1720094B (fr) |
AT (1) | ATE372824T1 (fr) |
AU (1) | AU2003283170A1 (fr) |
DE (1) | DE50308164D1 (fr) |
DK (1) | DK1426099T3 (fr) |
ES (1) | ES2291609T3 (fr) |
PT (1) | PT1426099E (fr) |
WO (1) | WO2004052519A1 (fr) |
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- 2003-12-05 CN CN2003801052450A patent/CN1720094B/zh not_active Expired - Lifetime
- 2003-12-05 JP JP2003407685A patent/JP4704676B2/ja not_active Expired - Lifetime
- 2003-12-05 WO PCT/CH2003/000804 patent/WO2004052519A1/fr not_active Application Discontinuation
- 2003-12-05 AU AU2003283170A patent/AU2003283170A1/en not_active Abandoned
-
2006
- 2006-04-24 US US11/409,102 patent/US7325970B2/en not_active Expired - Lifetime
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2007
- 2007-10-31 US US11/979,261 patent/US7841765B2/en not_active Expired - Lifetime
Non-Patent Citations (1)
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Cited By (16)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP2181827A2 (fr) | 2008-10-17 | 2010-05-05 | Sulzer Mixpac AG | Mélangeur statique |
EP2848320A1 (fr) | 2009-02-11 | 2015-03-18 | Sulzer Mixpac AG | Pièce intercalaire destinée à la liaison d'un récipient de stockage et d'un mélangeur statique |
WO2010102955A1 (fr) | 2009-03-11 | 2010-09-16 | Sulzer Mixpac Ag | Dispositif pour décharger une composition de remplissage |
EP2230025A1 (fr) | 2009-03-11 | 2010-09-22 | Sulzer Mixpac AG | Dispositif pour distribuer une matière de remplissage |
EP2407249A1 (fr) | 2010-07-16 | 2012-01-18 | Sulzer Mixpac AG | Pièce intercalaire pour relier une cartouche et un mélangeur statique |
WO2012095178A1 (fr) | 2011-01-13 | 2012-07-19 | Sulzer Mixpac Ag | Dispositif de distribution d'une matière de remplissage |
EP2599540A1 (fr) | 2011-11-29 | 2013-06-05 | Sulzer Mixpac AG | Élément de mélange pour un mélangeur statique |
EP2614883A1 (fr) | 2012-01-11 | 2013-07-17 | Sulzer Mixpac AG | Mélangeur statique |
CN103933885A (zh) * | 2014-05-07 | 2014-07-23 | 冀中能源邯郸矿业集团有限公司 | 一种无动力三向入料液固介质混合装置 |
CN103933885B (zh) * | 2014-05-07 | 2015-11-18 | 冀中能源邯郸矿业集团有限公司 | 一种无动力三向入料液固介质混合装置 |
EP3162433A1 (fr) | 2015-10-30 | 2017-05-03 | Sulzer Mixpac AG | Melangeur statique |
WO2017072079A1 (fr) | 2015-10-30 | 2017-05-04 | Sulzer Mixpac Ag | Mélangeur statique |
DE102017117198A1 (de) | 2017-07-28 | 2019-01-31 | 3lmed GmbH | Mischer |
WO2019020764A1 (fr) | 2017-07-28 | 2019-01-31 | Kettenbach Gmbh & Co. Kg | Mélangeur |
WO2022101167A1 (fr) | 2020-11-11 | 2022-05-19 | Sulzer Mixpac Ag | Pointe de mélange statique améliorée |
EP4000749A1 (fr) | 2020-11-11 | 2022-05-25 | medmix Switzerland AG | Buse de mélange statique améliorée |
Also Published As
Publication number | Publication date |
---|---|
US20060187752A1 (en) | 2006-08-24 |
US20080232191A1 (en) | 2008-09-25 |
KR101010872B1 (ko) | 2011-01-26 |
ATE372824T1 (de) | 2007-09-15 |
ES2291609T3 (es) | 2008-03-01 |
KR20050086900A (ko) | 2005-08-30 |
CN1720094B (zh) | 2012-08-29 |
EP1426099A1 (fr) | 2004-06-09 |
EP1426099B8 (fr) | 2007-10-17 |
PT1426099E (pt) | 2007-12-04 |
US7841765B2 (en) | 2010-11-30 |
AU2003283170A1 (en) | 2004-06-30 |
JP2004188415A (ja) | 2004-07-08 |
DE50308164D1 (de) | 2007-10-25 |
CN1720094A (zh) | 2006-01-11 |
US7325970B2 (en) | 2008-02-05 |
WO2004052519A1 (fr) | 2004-06-24 |
DK1426099T3 (da) | 2008-01-07 |
JP4704676B2 (ja) | 2011-06-15 |
US20040141413A1 (en) | 2004-07-22 |
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