The present application is a U.S. National Phase Application pursuant to 35 U.S.C. § 371 of International Application No. PCT/EP2018/070344 filed Jul. 26, 2018, which claims priority to German Patent Application No. 102017117198.3 filed Jul. 28, 2017 and German Patent Application No. 102017117199.1 filed Jul. 28, 2017. The entire disclosure contents of these applications are herewith incorporated by reference into the present application.
The present disclosure relates to a mixer with a mixer housing, which encloses a mixing chamber, an inlet connectable with the mixer housing, which has at least two input openings for the components to be mixed, and a mixing element at least some sections of which extend into the mixing chamber, wherein each of the input openings is flow-connected with the mixing chamber by way of at least one input channel.
Generic static and dynamic mixers are used, for example, in the area of dentistry or for building materials and adhesives. The mixing element of the mixer serves for the homogenous mixing of several, usually two, viscous or pasty components, which are stored separately in a cartridge or a similar container in a dischargeable manner. Typical consistencies/viscosities for dental impression materials are described in the standard norm DIN EN ISO 4823. Through the mixing process, a reaction of the individual components to each other is frequently started, whereby the actual material to be processed, such as a dental material or a building material or adhesive, is formed. Depending on the composition of the components to one another and the areas of application, these are mixed in different ratios. Typical mixture ratios include 1:10, 1:5, 1:4, 1:2 and 1:1.
Since the compositions and concentrations of the viscous/pasty components (in the following also simply termed: components) and their mixture ratios are coordinated with one another, it is decisive that the ratio of the components to one another is not only preserved in the filling process in the cartridge, but also in the mixing process itself.
The filling of the components into the cartridges is technically connected with certain variations in filling level, typically in the range of 5% and, with higher technical expenditure, even 1% of the volume filled. In addition, the arrangement of the respective dispensing pistons is connected with certain tolerances. It thus happens that one of the pistons is positioned further forward in the direction of discharge. Both the technical variations in the filling level as well as the slightly different arrangement of the dispensing pistons leads to the fact that one of the components enters into the mixing chamber before the other component. Furthermore, the breakaway torque of the dispensing piston, i.e., the initial impulse of the dispensing piston, may also turn out differently upon the moving out of the bearing position in the direction of discharge, particularly for reason of fluctuations in manufacturing, so that, even upon a perfect filling, one of the components enters into the mixing chamber before the other component. Since the components to be mixed generally have a different composition, the components furthermore differ in their rheology and thus in their discharge behavior. Since a different composition inherently forms the basis for a multi-component system, it is not possible to rule out, even with the optimization of the known constructions and the filling process, that one of the components will enter into the mixing chamber before the other components, even with 1:1 cartridges.
In other words, it must necessarily be observed that the one component forms a so-called forerun that enters into the mixing chamber before the other component, so that at least the initial ratio of the components to one another differs from the ideal mixture ratio. Such a forerun frequently leads to the fact that this is discharged out of the mixer in unmixed form. The component forming the forerun in unmixed form must be discarded, because it does not have the properties of the material to be processed.
Although the filling-conditioned fluctuations and irregularities of the positioning of the piston appear upon all viscous or pasty components, these are often tolerated, particularly upon large-volume and economical components, such as sealing materials or adhesives, for example. For small-volume and high-priced components, such as dental materials for example, these fluctuations are not acceptable, however, because a greater portion of the expensive material must be discarded.
In addition, the discarding of the forerun is cumbersome for the user and is connected with a safety risk upon the application, since the forerun does not have the adhesion, impact strength and/or strength properties that are maintained for the mixture. An unintended use of the forerun can lead to undesirable results, even from optical viewpoints.
EP 2 599 540 B1 describes a mixing element for a static mixer that reduces the forerunning of a component, since this component is brought forward to the mixing element via an input channel separate from the other component. A forerun known in advance can be compensated through the separate guiding of the components.
EP 2 527 029 A2 discloses a mixer with a star-shaped baffle plate which has a central pin or mandrel extending upstream into the materials stream which, upon diverging in its direction of flow, passes into an axially perpendicular plate.
WO 2012 116 873 A1 likewise relates to the compensation of a forerun. For that purpose, two delay chambers and a deflection element are provided, whereby the deflection element redirects the flows of components radially inwardly.
Furthermore, documents EP 0 664 153 A1, EP 0 584 428 A1, DE 29 902 666 U1, and DE 3 606 001 A1 describe generic static mixers which relate to the above-described problems.
US 2012/0 199 607 A1 discloses a discharge device with a two-component cartridge and a mixer that can be placed on this. The mixer is intended to be easily attached to and removed from the cartridge.
DE 36 06 001 A1 describes a dosing and mixing gun for multi-component plastics. Each component is guided into the static mixing chamber through a supply channel provided with a throttling device.
In the documents WO 2013 0 26 722 A1, EP 1 943 012 B1, DE 10 112 904 A1, DE 10 2004 008 748 A1, DE 299 02 666 U1, EP 2 190 563 B1, EP 1 458 467 B1 and EP 1 892 033 A1 dynamic mixers are described which are intended to compensate for a forerun.
A mixer with a unification chamber accommodating a forerun, which is provided inside a mixer intake area, is known from EP 0 885 651 B1. The component intake openings are thereby divided by means of a separation rib and extend the path of travel of the component present in excess.
For the above-described solutions, the fact that a filling-conditioned variation of a component present in excess acts more strongly than upon a component present in insufficient quantity is essentially employed. A forerunning of the component present in excess therefore comes about only when a filling-conditioned variation present in the component in insufficient quantity forms no forerun. Particularly upon . . . high surpluses, a component, such as with common 1:10 mixing ratios, for example. A forerun of component present in excess therefore also comes about, because the container accommodating this component and the associated dispensing pistons are significantly larger than the respective components of the component present in insufficient quantity. In other words, it must absolutely be determined in the known solutions before the filling of the components which component is present in excess and whether a forerun has thus been formed. Therefore, the known solutions are usable only upon unequal mixing ratios.
Upon mixing ratios of 1:1 and, in part, already upon similar mixing ratios with slight differences in volume, such as 1:1, 2.5 or 1:2, for example, it is not possible to securely predict which of the components is present in too high portions, however, and that a forerun has therefore been formed. This problem appears in all known multi-component cartridges and, in particular, independently of whether a static or a dynamic mixer is used.
The object of the present disclosure is therefore to provide a mixer which, for all mixing ratios, particularly with slight differences in volume, such as 1:1 to 1:2, accommodates the forerun, which can in particular be formed both from the first component as well as from the second component.
This object is solved with a mixer in accordance with claim 1.
It is provided in accordance with the disclosure that the mixer has a mixer housing with a mixing chamber, an inlet connectable with the mixer housing, which has at least two input openings for the components to be mixed, and a mixing element, wherein the mixing element extends in at least some of its sections into the mixing chamber. Here, each of the input openings is flow-connected with the mixing chamber by way of at least one input channel. It is additionally provided that at least one compensation channel is formed in the inlet, which connects the input openings to each other. In addition or as an alternative to this, at least one reservoir chamber for the accommodation of the forerun is provided in the mixing element.
Through the connection of the input openings with a compensation channel, the forerun exiting at the input openings can enter into the compensation channel and be collected there as forerun. Since the input openings are connected to each other, the forerun is collected independently of the component that forms the forerun. In other words, the connection between the input openings ensures that the components enter into the compensation channel through these input openings without a preselection in regard to the component forming the forerun having to be made.
The compensation channel permits self-regulation in regard to the forerun since the compensation channel is first of all filled by the forerunning component until the additional component flows into the compensation channel and prevents an additional filling of the compensation channel by the forerunning component. Both may subsequently enter into the mixing chamber separately or together through the input channels.
In other words, the disclosure may be seen in the fact that a, particularly radial open, compensation channel is provided. The compensation channel can thereby be formed by an external closed ring and by an internal ring with symmetrically positioned openings.
During the discharge, the forerunning component expands far enough in the compensation channel until it meets the trailing component. A variable front of components thereby arises, depending on the forerun path. The components form a contact surface with this front. After the compensation channel is filled, the front of the components remains in its position in the compensation channel, which leads to the fact that the additional inflowing mass of components flows into the inlet to the mixing chamber and then axially in the direction of discharge in the shortest path from the input openings through the corresponding openings.
The arrangement of at least one reservoir chamber in the mixing element likewise permits the accommodation of the forerun independently of which of the components forms the forerun, since the reservoir chamber, or the reservoir space in which the mixing element is provided, is thus filled by the forerunning component. The reservoir chamber in accordance with the disclosure is thereby configured in such a way that the forerun is accommodated and remains in the reservoir chamber. The reservoir chamber is thereby preferably positioned in the first third of the mixing chamber in the direction of flow of the components.
The reservoir chamber is preferably configured in such a way that it has closed lateral walls and has only one opening, which is formed as an input opening in a transverse wall. Since the reservoir chamber has only one input opening, but is not otherwise flow-connected with the other chambers, the forerun entering into the reservoir chamber is held there, however, so that this essentially no longer participates in the additional mixing process.
The mixer in accordance with the disclosure may be a static or a dynamic mixer.
It is particularly advantageous in accordance with the disclosure that the compensation channel is provided in the inlet. Thus, the compensation channel can be made for any type of mixer and functions independently of the specific configuration of the mixer.
In one preferred variant, the internal volume of the compensation channel and/or the reservoir chamber is adjusted to the filling-conditioned variations in such a way that the variations in the volume of the components are smaller than the internal volume of the compensation channel and/or of the reservoir chamber. In other words, the internal volume of the compensation channel and/or of the reservoir chamber corresponds to 1% to 10%, particularly 1% to 8%, and particularly preferably to 1% to 5%, of the volume of a component if a mixture ratio of 1:1 is present. Upon a mixture ratio differing from 1:1, the volume of the component present in larger portions is decisive.
Alternately or as a supplement to that, the internal volume of the compensation channel and/or of the reservoir chamber corresponds to 1% to 10%, particularly to 1% to 8%, and particularly preferably to 1% to 5%, of the volume of the component present in excess in relation to the volume of the component present in insufficient quantity or of the volume of the component present in insufficient quantity in relation to the volume of the component present in excess.
In one preferred configuration, two compensation channels are formed in the inlet, which each connect the input openings to each other. This prevents any possible blocking of the flow connection from the input opening to the mixing chamber.
In one additional configuration, the input channels are designed in such a way that the components to be mixed are separately guided away from one another and into the mixing chamber. Through that fact, a premature reacting of the components and a possible blocking of the input channels is prevented. In addition, the separate feeding of the components into the mixing chamber allows a better mixing of the components with one another.
It is additionally preferred if the two input openings are positioned diametrically opposed to one another in the inlet, whereby the input channels extend along a diagonal connecting the input openings and are separated from one another by a partition wall extending transversely to the diagonal. The partition wall prevents a mixing of the components possibly occurring in the input openings, through which these could be blocked. The partition walls are preferably formed along a portion of the circumference of an input opening.
If the entire circumference of the input opening for the flowing of the components into the at least one compensation channel is available, then it is particularly preferable if the partition walls are positioned along less than 50%, preferably less than 40% and, most particularly preferably, to between 20% and 30% of the entire circumference of the corresponding input opening.
If the entire circumference of the input opening is not available for the inflowing of the components, such as because the flowing of the components through the input openings on the radial edge of the inlet is partially blocked, for example, then it is particularly preferable if the partition walls are positioned along less than 80%, preferably less than 70%, and are most particularly preferably positioned at between 40% and 60% of the circumference available for the inflowing of the corresponding input opening.
In accordance with one additional preferred configuration, the input channels are designed in such a way that the components to be mixed with one another are guided into the mixing chamber, at least in certain areas, in an enveloping manner. This supports the subsequent mixing process in the mixing chamber.
As an alternative to that, the input channels may be flow-connected with one other, so that the components to be mixed are jointly guided into the mixing chamber.
In one preferred variant, the at least one compensation channel extends in an essentially circular arc between the input openings. Such an arrangement ensures that the components can flow into the compensation channel from each of the input openings.
In one additional embodiment, the at least one compensation channel extends radially outside the input channels. Through that fact, the forerun is guided externally from the input openings or input channels, as the case may be, and into the compensation channel, which is particularly preferred if the inlet is positioned centrally in the mixing chamber, considered radially. This leads to the fact that the forerun first of all fills the external compensation channel and the components can subsequently enter into the mixing chamber together. An interruption of the input channels by the compensation channel is thus prevented and, furthermore, a relatively short path from the input openings into the mixing chamber is ensured, since this path leads along the input channels centrally into the mixing chamber. This additionally reduces the discharge pressure, since the components must be discharged over a short path of travel with less expenditure of energy.
Furthermore, it is preferable if the at least one compensation channel and the input channels are formed as depressions or grooves in the inlet and are sealed off, at least in certain areas, from the mixer housing or the mixing element. Since the inlet is produced separately from the mixer housing, additional material can be saved in this variant during the manufacture. It is thereby particularly preferred if the mixer housing or the mixing element of the compensation channel is covered by a disk-shaped or funnel-shaped collar in the intake area of the mixing chamber.
It is furthermore preferred if the compensation channel has a mirror plane extending through the middle points of the input openings. In addition or as an alternative to this, the compensation channel may have a multiple rotation-reflection axis. The numerical value of the rotation-reflection axis corresponds, in one preferred variant, to the number of the input openings. If, therefore, two input openings are present, then a two-fold rotation-reflection axis is preferred, if three input openings are present, then a three-fold rotation-reflection axis is preferred, and so forth. This symmetry ensures that a compensation of the forerun is ensured upon mixing ratios of 1:2 to 1:1 or 1:1:2 to 1:1:1 for more than two components independently of the respective forerunning component.
Finally, it is preferable that the inlet and the mixer housing are designed and adjusted to one another in such a way that the components exiting from the input openings and to be mixed are deflected from a direction of flow extending in parallel with the longitudinal axis of the mixer housing by 90° in a direction of flow transversely to the longitudinal axis of the mixer housing. The deflection prevents the components on the compensation channel from moving directly forward and into the mixing chamber.
In one preferred embodiment, a flow wall is provided along the circumference of at least one input opening, which [flow wall], considered from the corresponding input opening, is formed in a concave or convex manner.
Particularly for the case that the entire circumference of the input opening is available for the flowing of the components into the at least one compensation channel, it is preferable if the flow wall is positioned, particularly along less than 50%, preferably less than 40% and, most particularly preferably, to between 20% and 30%, of the entire circumference of the corresponding input opening.
If the entire circumference of the input opening is not available for the inflowing of the components, such as because the flowing of the components through the input openings on the radial edge of the inlet is partially blocked, for example, then it is preferable if the flow wall is positioned, in particular, along less than 80%, preferably less than 70% and, most particularly preferably, to between 40% and 60% of the circumference available for the inflowing of the corresponding input opening.
In continuation of this line of thought, it is preferable that the at least one flow wall is closed in a sealing manner with a disk-shaped or funnel-shaped collar of the mixer housing or of the mixing element. In other words, the axial length of the flow wall corresponds to the axial length of the compensation channel.
If several flow walls are provided, then it is preferable to arrange these at a distance from one another, so that the components can flow in through the recesses thereby formed between the flow walls centrally in the direction of the mixing element. The extent of the distance of two adjacent flow walls to one another thereby defines the drop in pressure in the center to the mixing element. The distance is preferably selected in such a way that the drop in pressure between the walls is greater than the drop in pressure in the compensation channel, so that forerunning material flows into the compensation channel before it enters centrally into the mixing chamber.
This is preferred if the inlet has a reservoir space that extends radially outwards of the compensation channel and/or the input channels. The reservoir space is closed off from the components in the direction of discharge of the material, so that the components from the reservoir space cannot flow into the mixing element. This delimits the reservoir space from the input channels. A reservoir space is particularly advantageous if a large-volume forerun is to be expected. A reservoir space with mixing ratios diverging from 1:1, particularly 1:10, is therefore particularly advantageous.
Furthermore, it is preferable, if at least one optional baffle plate and/or a flow clamp, which at least partially covers and/or laterally restricts the corresponding input opening, is assigned to one of the input openings. The baffle plate is preferably provided above the corresponding input opening and therefore lies directly in the direction of discharge of the material, so that the component that flows through the corresponding input opening, exits from the input opening at the exit and strikes the baffle plate and is deflected, particularly in the direction of the mixing chamber. The flow clamp preferably laterally restricts the corresponding input opening in such a way that the component that flows through the corresponding input opening is guided at the exit from the input opening in the direction of the mixing chamber. Both the baffle plate as well as the flow clamp thus make it possible to set a direction of flow for the component flowing out from the corresponding input opening. This is particularly advantageous if the portion of the corresponding component is small, so that this component can flow into the mixing chamber nearly completely and possible remnants in the inlet can be minimized. The above-described advantages of the baffle plate can thereby also be achieved on a collar provided on the mixing element if this, comparable to the baffle plate, covers at least one of the input openings, if the inlet and the mixing element are mounted in the mixer.
It is furthermore preferable if the mixing element has a flow chamber adjacent to the reservoir chamber, which stands in a flow-connected manner with the mixing chamber by way of a through-opening.
In continuation of this line of thought, it can be provided that that the flow chamber is restricted in the direction of discharge of the material by a transverse wall and that the transverse wall comprises a transverse wall opening, so that the components can at least partially flow in through the transverse wall opening. This reduces the discharge pressure upon the discharge of the components through the mixer, which leads to a greater user-friendliness when discharged.
It is additionally preferable if the cross-section of the mixing element positioned perpendicularly to the direction of discharge of the material amounts, in the section of the reservoir chamber and/or flow chamber, to 105% to 150%, preferably 105% to 120%, particularly preferably to 110%±5%, of the cross-section of the mixing element positioned perpendicularly to the direction of discharge of the material into the following section of the mixing element considered in the direction of discharge of the material. In other words, the mixing element is enlarged in an area of the reservoir chamber and/or flow chamber. This leads to the fact that a higher cross-section of flow can be achieved in this area with constant stability of the mixing element, which is advantageous for the reduction of the discharge pressures, particularly upon highly viscous components. Furthermore, the holding capacity of the reservoir chamber is improved, so that a large-volume forerun can be accommodated.
The reservoir chamber and/or flow chamber are preferably provided in the section that is covered with the inlet section of the mixing case, which has the advantage that an expansion of the mixing element can be accommodated in this section by means of a corresponding adjustment of the internal contour of the inlet section of the mixing case. Otherwise, the mixing case can, of course, even be adjusted corresponding to the expanded contour of the mixing element.
The disclosure will be explained in further detail in the following by means of exemplary embodiments and with reference to the diagrams. All the characteristics described and/or graphically represented thereby form the object of the disclosure, either by themselves or in any desired combination, independently of their summary in the claims or in their referrals back to the same.
The following are depicted schematically:
At least one compensation channel 4 is formed between the input openings 2 (
The operating principle of the compensation channel 4 is explained by means of
In
In the example depicted in
In the example depicted in
A third embodiment of the inlet 1 is depicted in
The flow walls 5 and the deflecting walls 9 are positioned at a distance from one another, so that openings form between each deflecting wall 9 and the adjacent flow walls 5, or each flow wall 5 and the adjacent deflecting walls 9, as the case may be. The components A and B can flow through the openings into the centrally positioned inlet of the mixing chamber (not depicted). On the basis of the arrangement of the flow walls 5 and the deflecting walls 9, the components A and B first of all fill the compensation channel 4 and subsequently flow centrally into the mixing chamber through at least one input channel 7a.
In
The fifth embodiment of an inlet 1 depicted in
The enveloping element 12 is configured in an essentially circular manner and has a central opening 12a, which opens in the direction of an input opening of a component and leads this centrally in the direction of the mixing chamber. An additional opening is positioned opposite the central opening 12a in the direction of the other component, which directs this into an essentially semi-circular channel 12b around the central opening 12a. This leads to the fact that the components A and B are introduced into the mixing chamber approximately coaxially into one another, which facilitates the subsequent mixing of both components in the mixing chamber.
The directions of flow 6A and 6B of the components A and B are depicted in
The mixing element 13 has a disk-shaped or funnel-shaped collar 15 on the inlet side. It is configured in such a way that it covers the inlet 1 and seals the compensation channel 4 in certain areas or as a whole.
For a better understanding of the effects in accordance with the disclosure, a helical mixer 16 with a connection 17 and with an inlet 18 known in accordance with the state of the art is depicted in
For the illustration of the problem forming the basis for the disclosure in accordance with the state of the art,
The transition from inlet 1 to the mixing element 13 is also clear from
A view from above of the third inlet, both with (top right) and without (top left) an input channel 7a is depicted in the mixing chamber (mixer entrance) at the top of
The inlets 1 in accordance with a seventh embodiment (
In this case, a forerun of component present in 10-fold excess is regularly to be expected, since this has a correspondingly higher volume in comparison with the component present in insufficient quantity, so that proportional variations, such as upon the filling process, for example, and thereby a compensating forerun, are relevant practically exclusively for the component that is present in excess.
The configuration of the compensation channels 4, of the flow walls 5, and the deflecting walls 9 of the seventh insert 1 is comparable to the third inlet 1 depicted in
Furthermore, the seventh inlet 1 comprises a baffle plate 20 lying in the direction of discharge of the material, which plate covers the input opening 2a in its radial external area at least partially in such a way that the component flowing through the input opening 2a is deflected in the direction of the centrally positioned opening to the mixing chamber 7 (not depicted) (
An eighth embodiment of the inlet 1 is depicted in
When the components flow in through the intake opening 13b, these are divided by a central wall 23 and flow partially into a reservoir chamber 14 and partially into a flow chamber 24. The components flow from the flow chamber 24 through a through-opening 25 and into the chambers of the mixing element 13, the length of which is defined in the direction of discharge of the material through the transverse wall 26.
In the third embodiment depicted here, the cross-section of the through-opening 25 is smaller than the cross-section of the flow chamber 24. The smaller cross-section, thus the cross-section of the through-opening 25 here, is thereby decisive for the drop in pressure upon the discharge of the components. Relatively high discharge pressures can hereby appear, whereby the discharge pressure is also influenced by the configuration of the mixing element 13 and the specific viscosity of the components.
A fourth mixing element 13 is depicted in
A sixth mixing element, which has been expanded in the area of the reservoir chamber 14 and of the flow chamber 24, is depicted in
A seventh mixing element 13 is depicted in
Number | Date | Country | Kind |
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102017117198.3 | Jul 2017 | DE | national |
102017117199.1 | Jul 2017 | DE | national |
Filing Document | Filing Date | Country | Kind |
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PCT/EP2018/070344 | 7/26/2018 | WO |
Publishing Document | Publishing Date | Country | Kind |
---|---|---|---|
WO2019/020768 | 1/31/2019 | WO | A |
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Number | Date | Country | |
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20200171448 A1 | Jun 2020 | US |