This application is a U.S. National Stage application of International Application No. PCT/EP2016/069187, filed Aug. 11, 2016, which claims priority to European Application No. 15182961.1, filed Aug. 28, 2015, the contents of each of which are hereby incorporated herein by reference.
The present invention relates to a static mixer for mixing together at least two components comprising: a mixer housing; a mixing element arranged at least partly within the mixer housing; and a mixer inlet section having at least two inlets disposed at an input side and at least two outlets disposed at an output surface. The invention further relates to a dispensing apparatus and to a method of assembling a static mixer.
A wide variety of ways of dispensing two-component masses from cartridges is known in the prior art. The materials to be dispensed are typically a matrix material and a hardener. Two-component materials are typically used as impression materials, e.g. on the formation of dental impressions, as a cement material for prosthetic restorations, as a temporary cement for trial cementing restorations or for cementing temporary crowns. Further applications of two-component materials are in the building industry where they are e.g. used as a replacement for mechanical joints that corrode over time. Adhesive bonding can be used to bond products such as windows and concrete elements. The use of multi-component protective coatings, for example moisture barriers, corrosion protection and anti-slip coatings, is also becoming increasingly common. Examples of flowable materials which can be used are, for example, distributed by the company Coltene using the tradename AFFINIS® or by the company DMG using the tradename PermaCem.
The following kinds of two-component materials are used in the building industry:
These materials are typically highly viscous and are almost solid and hence require large static mixers, having a diameter typically larger than 10 mm, in order to be discharged from a cartridge and subsequently mixed.
Filled cartridges can come in different ratios referred to as 1:1, 2:1, 4:1 and 10:1 etc., the numbers specifying the ratios of the amounts of each of the two materials that are to be dispensed. The reason for these different ratios is to allow a wide variety of different compositions to be mixed and dispensed. For example, some compositions require more hardener, and some require less hardener. Also, some compositions require more mixing.
Static mixers, also referred to as mixing tips, are known from the prior art. The static mixers are adapted to mix the compositions as they exit the cartridge. In this respect different length and different diameter mixing tips are provided to ensure a thorough through mixing of the various two-component mixtures. The mixing tips typically have an insert resembling e.g. an open spiral which forces the two-components into contact with one another and exerts forces on them causing them to mix.
The individual components of the multi-components to be mixed are frequently fairly expensive so there is a need to reduce the volume of material lost after a mixing process has taken place. This is in particular true for large static mixers, i.e. static mixers typically having diameters larger than 10 mm, that are used e.g. in the building industry. In order to reduce the volume remaining in a static mixer, specific designs have been implemented resulting in a reduced length static mixer. However, the reduction in length has led to very complicated designs of static mixers. Since the static mixers are frequently manufactured in an injection molding process, the production of static mixers has become very demanding in effort and cost, as highly complex molds are necessary. At times the manufacture may be impossible, as the provision of undercuts and recesses in the static mixer means that the previously used molds can no longer be used.
For this reason it is an object of the present invention to provide a static mixer in which the volume of the multi-component material left after use of the static mixer is reduced in comparison to the prior art. It is a further object of the invention to provide a static mixer in which the flow of multi-components through the static mixer is improved. It is yet a further object of the invention to provide a static mixer in which the through mixing of the multi-components is improved.
This object is satisfied by a static mixer having the features discussed herein.
In particular, such a static mixer is suitable for mixing together at least two components and comprises: a mixer housing; a mixing element arranged at least partly within the mixer housing; and a mixer inlet section having at least two inlets provided at an input side and at least two outlets provided at an output surface; wherein the at least two outlets are in fluid communication with the at least two inlets; and wherein the mixer housing, the mixing element and the mixer inlet section are formed as separate elements. The static mixer is characterized in that the mixing element comprises a plug element and the mixer inlet section comprises a counter plug element engaging the plug element. The static mixer is further characterized in that the mixing element and the mixer inlet section are plugged together in a rotationally fixed manner by a plugged connection.
Providing a three part static mixer enables the use of molds for injection molded processes to produce the static mixer. This leads to a reduction in the cost of manufacture and to reproducible production results.
Moreover, the handling and assembly of the static mixer is improved as the three parts can simply be plugged together after their respective production.
Furthermore, as the mixer inlet section and the mixing element are plugged together in a rotationally fixed manner, the mixing process is improved. This is because the orientation of the two parts relative to one another is improved, so that the components to be mixed are guided and fed into the mixing element such that the components arrive at the correct inlets of the mixing element improving the mixing result and more importantly also allowing a reduction in length of the static mixer. A reduction in length of the static mixer leads to a reduction in any residual volume that is left in the static mixer after its use.
In this connection it must be noted that the plug element and the counter plug element can be a plug and socket type connection. In one design the socket can be disposed at the mixing element, in a different design the socket can be provided at the mixer inlet section. The corresponding plug is then disposed at the other element.
Having regard to medium to high mixing ratios of 2:1, 4:1 or 10:1 etc, the flow of the low volume component can be controlled by maintaining a diameter of the flow path to the mixing element comparatively small and to introduce this component directly into the optimal spot of the mixing geometry and to thereby permit the other component to enter the mixing geometry at the position ideal for it and to thereby prevent undue forerunning of either of the components.
Similar guide mechanisms can also be employed for low to medium mixing ratios of 1:1 to 2:1 mixers using a static mixer in accordance with the invention, making the concept universally applicable to static mixers.
By providing a plug element and a counter plug element to connect the mixer inlet section and the mixing element, a distance between the mixing element and the mixer inlet section can be reduced. A reduction in the distance between the mixing element and the mixer inlet section leads to a reduction in the residual volume of components left behind in the static mixer.
In this connection it should be noted that the feature according to which the mixing element is at least partly provided within the housing means that at least mixer elements of the mixing element are arranged within the mixer housing and that, for example, components of the plug element may project out of the mixer housing in order to cooperate with the mixer inlet section. In this regard at least 70%, preferably 80 to 95% of the mixing element are typically arranged within the mixer housing.
Preferably the mixing element and the mixer inlet section are held together in an axial direction by the plugged connection that is formed by the plug element and the counter plug element and/or by at least one element of the mixer inlet section cooperating with at least one element of the mixer housing.
Forming the plugged connection between the mixer inlet section and the mixing element ensures that these components can remain connected outside of the housing. Alternatively or additionally forming the plugged connection between the housing and the mixer inlet section ensures that the three parts can be connected to one another in a preferably secure manner, such that any pressure arising within the static mixer does not result in the static mixer coming apart.
Advantageously the plugged connection, preferably between the plug element and the counter plug element, comprises a clamping connection and/or a frictional connection, such as at least one nose frictionally engages one of the mixer inlet section and the mixing element, and/or a latching connection of the plug element and the counter plug element. Such connections can easily be produced in a cost effective manner.
It is preferred if the mixing element and the mixer inlet section are aligned in a fixed predefined rotational angular relationship by the plug element and the counter plug element.
In this connection a predefined rotational angular relationship means that when the mixing element and the mixer inlet section are plugged together by the plugged connection that the outlets of the mixer inlet section are aligned relative to the mixing element.
Utilizing the plug and counter plug element to achieve the fixed predefined rotational angular relationship means that the two components mixing element and mixer inlet section can be tailored to one another to permit the desired flow of components from he mixer inlet section into the mixing element.
Optionally the plug element and the counter plug element comprise coding means or element, in particular a thickened end or a bulge cooperating with a corresponding recess or groove, allowing the mixing element and the mixer inlet section to be plugged together only in the predefined rotational angular relationship.
The provision of coding element advantageously permits the correct placement of the plug element relative to the counter plug element to ensure, on the one hand, the predefined rotational angular relationship, and, on the other hand, the correct alignment of the two components relative to one another.
In this connection it should be noted that the thickened end or bulge can be provided on either of the plug element and the counter plug element and that the corresponding recess or groove is then respectively provided on the other one of the plug element and the counter plug element.
The plug element preferably comprises a wall section provided at an input end of the mixing element and the counter plug element comprises a groove provided on the output surface. Providing the plug element at the mixing element and the corresponding socket at the mixer inlet section makes these parts particularly simple to manufacture.
In this connection it should be noted that the coding element can be provided at the wall section, so that the wall section advantageously carries out an alignment and coding function.
In a preferred design the wall section is arranged between the at least two outlets so as to separate the components leaving the at least two outlets before entering inlets of the mixing element. Providing the wall section such that the components are separate from one another before entering inlets of the mixing element ensures the optimum mixing results and hence permits a reduction in the length of the mixing element.
Preferably the wall section has a straight planar shape, and/or comprises a thickened end, and/or has at least partially a U-shaped cross section, and/or has at least partially a T-shaped cross section.
Such shapes have been found to be beneficial to ensure the connection between the mixing element and the mixer inlet section in a rotationally fixed manner and indeed even in a coded manner, so that the components can only be plugged together in one orientation.
Providing a wall section having a U-shaped cross-section, for example, enables the provision of a groove within the wall section of the plug element. This groove can then act as an extension of the flow path from the inlet of the mixer inlet section to the mixing element.
Advantageously the at least two inlets have respective inlet openings and the at least two outlets have outlet openings, with the outlet openings being formed in the output surface of the mixing inlet, wherein a surface area of at least one of the inlet openings is smaller than a surface area of the corresponding outlet opening.
Providing at least one outlet opening that is larger in area than an inlet opening means that one can manipulate the flow of at least one component in the direction towards the mixing element in a desired way.
It is preferred if the output surface of the mixer inlet section has an at least substantially slanted contour at an outlet side of the mixer inlet section with respect to a longitudinal axis of the static mixer, with the outlet side being disposed remote from the inlet side, with the at least substantially slanted contour of the output surface preferably being adapted to a shape of an inlet surface of the mixer housing.
Forming the output surface of the mixer inlet section in a convex manner and correspondingly adapting the inlet surface of the mixer housing means that a flow path extending through the mixer inlet section can be extended from the outlet of the mixer inlet section to the inlets of the mixing element in a desired way through cooperation with the housing. This means that there is no region between the outlets of the mixer inlet section and the inlets into the mixing element in which the flow path of the components experiences an unwanted deflection at the mixer housing. This leads to improved mixing results.
In this connection it must be noted that the slanted contour means that the correspondingly convexly shaped surface can be formed as part conical or cone shaped, part truncated cone like, as part chamfered surfaces or as part pyramid like surfaces etc. The specific shape chosen is ideally selected to ensure the optimum flow path to the inlets of the mixing element.
In this connection it should also be noted that the at least substantially convexly shaped surface, respectively the at least substantially slanted contour, refers to the general shape of that part of the surface of the mixer inlet section that is adjacent to the mixer housing and in which no openings, such as the outlet openings or the counter plug element are provided.
Preferably the static mixer has a longitudinal axis and at least two flow paths extend between the at least two inlet and outlet openings, wherein each inlet and outlet opening has a geometric center, with the geometric center of at least one, preferably of each, of the at least two outlet openings being spaced less far apart from the longitudinal axis than the geometric center of at least one, preferably of each, of the at least two inlet openings.
Guiding the flow paths of components to be mixed towards the longitudinal axis through the mixer inlet section means that the components can enter the mixing element at the optimum spot.
Advantageously, in a region of the at least two outlets, the at least two flow paths are configured to cooperate with the mixer housing, preferably with an inlet surface of the mixer housing, to provide a component flow guide region at inlets of the mixing element, wherein the at least two outlets of the mixer inlet section are preferably arranged to at least partly overlap with inlets of the mixing element, in particular with the inlets of the mixing element being formed by the mixing element and/or by spaces formed between the mixing element and an internal wall of the mixer housing.
Such a design leads to an improved flow path between the mixer inlet section and the mixing element in which the flow path of the components experiences less unwanted deflections at the mixer housing leading to improved mixing results.
It is preferred if at least one region of at least one of the at least two outlets adjacent to the corresponding outlet opening is configured such that its cross-section perpendicular to the respective one of the at least two flow paths is enlarged in comparison to the corresponding inlet, in particular such that the flow path extending between the inlet opening and the outlet opening is directed and enlarged in a direction towards at least one inlet of the mixer element.
Enlarging a volume of the outlet in the region of the outlet opening means that a flow path towards the inlets of the mixing element can be tailored to direct the components towards the mixing element.
Advantageously the mixing element comprises a plurality of mixer elements arranged one after another for a repeated separation and re-combination of streams of the components to be mixed.
It is preferred if at least one recess is provided at an outlet side of the mixer inlet section, wherein one of the at least two outlets opens into a base of the at least one recess. Such a recess advantageously forms a collecting region for a component to be directed into the inlets of the mixing element.
Advantageously a cross-sectional area of the at least one recess is preferably larger than the cross-sectional area of the one of the at least two outlets. Such a recess provides a comparatively large volume collecting region for guiding the component towards the inlets of the mixing element.
The depth of the recess in the axial direction can preferably amount to at least a third, in particular to at least half of the diameter of the outlet, alternatively the depth of the recess in the axial direction is preferably equal to or larger than the diameter of the outlet. Such a recess also provides a comparatively large volume collecting region for guiding the component towards the inlets of the mixing element.
Preferably the at least one recess has a cross-sectional shape that deviates from a circle. Advantageously such that the at least one recess has an elongate shape that is in particular extended towards the longitudinal axis. Thereby an as large as possible free space is generated in the mixer inlet section for the collection region. In this connection it should be noted that a recess can be disposed within each outlet, to provide an as large as possible free space for the collection region provided for each outlet.
In some designs it can be advantageous if the at least one recess is connected to the other one of the at least two outlets and/or to a further recess in a direction transverse to the longitudinal axis. Thereby at least one maximum volume collecting region can be generated in the mixer inlet section.
In this connection it should be noted that once the plug element engages the counter plug element the two outlets are separated, so that a maximum volume collecting region can be generated in the mixer inlet section for each outlet and hence for each flow path.
For an as good as possible mixing result the mixing element can comprise mixer elements for separating the material to be mixed into a plurality of streams, as well as means for the layered merging of the same, including a transverse edge and guide walls that extend at an angle to said transverse edge, as well as guide elements arranged at an angle to the longitudinal axis and provided with openings, wherein said mixing element comprises a transverse edge and a following transverse guide wall and at least two guide walls ending in a separating edge each with lateral end sections and with at least one bottom section disposed between said guide walls, thereby defining at least one opening on one side of said transverse edge and at least two openings on the other side of said transverse edge.
Alternatively the mixing element can comprise mixer elements for separating the material to be mixed into a plurality of streams, as well as a structure or means for the layered merging of the same, including separating edges and a transverse edge that extends at an angle to said separating edges, as well as deflecting elements arranged at an angle to the longitudinal axis and provided with openings, wherein said mixing element comprises at least two separating edges with following guide walls with lateral end sections and with at least one bottom section disposed between said guide walls, and a transverse edge arranged at one end of a transverse guide wall, thereby defining at least one opening on one side of the transverse edge and at least two openings on the other side of the transverse edge.
In a further aspect the present invention relates to a dispensing apparatus comprising a multi-component cartridge and a static mixer as described in the foregoing that is connected to the multi-component cartridge, with the multi-component cartridge preferably being filled with respective components.
Preferably the mixer elements of the mixing element are held together by struts, with the struts also acting as further guide and deflecting walls.
Such designs of mixing elements have been found particularly advantageous to improve the mixing results and at the same time to achieve the desired reduction in length of the static mixer.
In a further aspect the present invention relates to a method of assembling a static mixer, comprising a mixer housing, a mixing element and a mixer inlet section that are formed as separate elements, the method comprising the steps of:
Advantageously the static mixer used in such a method can be further developed in accordance with the static mixer described herein.
In a further aspect the present invention relates to a use of a static mixer of the kind described herein or of a dispensing apparatus of the kind described herein in order to dispense components from a multi-component cartridge via the static mixer.
In a further aspect the present invention relates to a mixer inlet section. The mixer inlet section comprises a counter plug element of the kind described herein.
In a further aspect the present invention relates to a mold for the mixer inlet section. The mold is then adapted such that it provides recesses and undercuts matching the negative shape of the mixer inlet section in a similar manner as the static mixer described in the foregoing.
In a further aspect the present invention relates to a mixing element. The mixing element comprises a plug element of the kind described herein.
In a further aspect the present invention relates to a mold for the mixing element. The mold is then adapted such that it provides recesses and undercuts matching the negative shape of the mixing element in a similar manner as the static mixer described in the foregoing.
Likewise, the method in accordance with the invention can be adapted in a similar manner as the static mixer and/or the dispensing apparatus described in the foregoing.
The invention will be explained in more detail hereinafter with reference to the drawings.
In the following the same reference numerals will be used for parts having the same or equivalent function. Any statements made having regard to the direction of a component are made relative to the position shown in the drawing and can naturally vary in the actual position of application.
The counter plug element of
The counter plug element 26 is configured such that the plug element 30 can only be inserted in one direction into the mixer inlet section 14. Thereby the shape of the counter plug element 26 acts as coding element for the insertion of the generally T-shaped end of the plug element 30.
The outlet openings 24a, 24b are respectively formed in an output surface 32 of the mixer inlet section 14. Adjacent to the outlet opening 24b a recess 34 is formed within the outlet 22b. The recess 34 expands a volume of the outlet 22b relative to the inlet 18b.
The recess 34 has an elongate shape and thereby enlarges and directs a flow path of a component 102b (see
The guide reservoir enables the component 102b to be directed into inlets 36 (see
In order to improve the introduction of the components 102a, 102b into the mixing element 16, the outlets 22a, 22b of the mixer inlet section 14 are spaced less far apart than the corresponding inlets 18a, 18b.
The outlet opening 24a is approximately a tenth of the size of the outlet opening 24b. This is because the mixer inlet section 14 is used for multi-components having a medium to high mixing ratio such as 4:1 and 10:1, this means that one of the components is introduced into the mixing element at a ratio of 4:1 or 10:1 with respect to the other component.
The inlets 18a, 18b are in fluid communication with the respective outlets 22a, 22b, so as to guide components from the cartridge 100 to the mixing element 16.
The alignment devices 20a, 20b are used in order to align the mixer inlet section 14 with the cartridge 100. In order to connect the mixer inlet section 14 of the static mixer 10 to the cartridge 100 in a coded and aligned manner the alignment devices 20a, 20b have a different size so that these can only be positioned in one way. Moreover, the alignment devices 20a, 20b have a generally T-shaped cross-section for this purpose. An attachment means or device (not shown) such as a retainer nut can additionally be used to, at least intermittently fixedly, connect the static mixer 10 to the cartridge 100.
Having regard to the high ratio mixer inlet section, the inlets 18a, 18b are also of different size so that these can only be placed on to the cartridge 100 in one way and thereby also act as a coded alignment devices.
Moreover, one can see a side view of the generally T-shaped alignment devices 20a, 20b in
The mixer inlet section 14 has a projection 40 arranged adjacent to the output surface 32. This projection is adapted to cooperate with a groove 42 (see
One can see how the flow path 44b between the inlet 18b and the outlet 22b is directed towards the longitudinal axis A. Through the provision of the recess 34, the diameter of the flow path 44b (the same is true in analogy for the flow path 44a) experiences no constrictions in the region of the outlet 22b. This is because a distance between the mixer housing 12 and the recess 34 is selected such that the diameter of the flow path 44b is kept at least substantially equal throughout the mixer inlet section 14 and up to the mixing element 16. For this reason the flow of the component 102b experiences significantly less flow resistance on its passage through the mixer inlet section 14 up to the mixing element 16 on being discharged from the cartridge 100 in comparison to prior art static mixers (not shown). Likewise the flow path 44a between the inlet 18a and the outlet 18b is shifted towards the longitudinal axis A.
The individual mixer elements 46 are connected to one another by struts 54, with the struts 54 also acting as further guide and deflecting walls. The number of mixer elements 46 and the corresponding length of the struts 54 is selected in dependence on the kind of material that is to be dispensed with a certain static mixer 10. For some applications five mixer elements 46 may be sufficient whereas for others ten or more mixer elements 46 may need to be connected to one another by struts 54.
Likewise the flow path 44b extends from the inlet 18b via the outlet 22b of the mixer inlet section towards inlets 36 of the mixing element 16. The flow path 44a is smaller in diameter than the flow path 44b, as the mixer inlet section 14 and the mixing element 16 currently employed are used for high mixing ratios of e.g. 4:1 and 10:1.
Moreover, the section shown in
Both
Moreover, the shift of the flow paths 44a, 44b takes place within the mixer inlet section 14, so that a spacing between the mixer inlet section 14 and the mixing element 16 can be reduced leading to a further reduction in the residual volume remaining in the static mixer 10. This is advantageously achieved in a mixer inlet section 14 having the same height as prior art mixer inlet sections (not shown).
As the outlets 22a, 22b have the same size, the side view of
Like with the outlet 22b of
As can be seen in the section of
The wall section 56 shown in the side view of
Using the molding devices Ma, Mb mixer inlet sections 14 and mixing elements 16 as described herein can be produced.
Number | Date | Country | Kind |
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15182961 | Aug 2015 | EP | regional |
Filing Document | Filing Date | Country | Kind |
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PCT/EP2016/069187 | 8/11/2016 | WO | 00 |
Publishing Document | Publishing Date | Country | Kind |
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WO2017/036759 | 3/9/2017 | WO | A |
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International Search Report dated Nov. 25, 2016 in corresponding International Application No. PCT/EP2016/069187, filed Aug. 11, 2016. |
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Number | Date | Country | |
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20190030499 A1 | Jan 2019 | US |