A FILLING FLOW DIVIDER

Abstract

The present disclosure relates to a method and a filling machine for portioning pasty masses for the purpose of food production, wherein a pasty mass is fed by the filling machine into the filling flow divider, where it is separated into a plurality of mass flows and discharged in portions in the discharge direction. At the end of each portion the mass flow is sucked back in a direction opposite to the discharge direction.

Claims

1. A filling machine for carrying out a method of portioning pasty masses for food production, wherein the filling machine comprises a feed mechanism for feeding pasty mass to a filling flow divider, wherein the filling flow divider is configured such that the filling flow divider is able to divide the pasty mass into a plurality of mass flows and discharge the pasty mass in portions in a discharge direction, wherein the filling flow divider comprises a plurality of dosing elements for adjusting a volume flow of the plurality of mass flows, and wherein the filling machine comprises a control unit, which is configured such that and which controls the filling machine such that, at an end of each portion, a mass flow of the plurality of mass flows is sucked back in a direction opposite to the discharge direction.

2. The filling machine according to claim 1, wherein the dosing elements are driven via a joint motor and are coupled such that there is an equal volume flow in each line downstream of the respective dosing element or are driven by the pasty mass and configured as vane wheels that rotate freely about an axle, and wherein the dosing elements are coupled to one another.

3. The filling machine according to claim 1, wherein, downstream of the dosing elements, lines are arranged, wherein the lines are tubes and/or hoses and/or nozzles, wherein via the lines the mass flows are fed and discharged, said lines being arranged so as to be movable relative to one another such that a distance at which the discharge ends of neighboring lines are spaced apart is variable.

4. The filling machine according to claim 3, wherein the lines are curved and wherein the discharge ends thereof are directed downwards in a direction of a surface onto which the portions are discharged, the respective free discharge opening being located in a plane that is inclined by 0? to 60? relative to a plane in which the surface lies.

5. The filling machine according to claim 3, wherein at least a part of the lines is rotatably fastened.

6. The filling machine according to claim 1, wherein lines having no controllable discharge or shut-off valves are arranged between dosing elements and discharge ends of the filling flow divider.

7. The filling machine according to claim 1, wherein a discharge end of the filling flow divider has arranged thereon a self-closing membrane which is able to close when the pasty mass is sucked back and to automatically open when the pasty mass moves in the discharge direction.

8. The filling machine according to claim 1, wherein the dosing elements are driven by the pasty mass and configured as vane wheels that rotate freely about an axle, and wherein the dosing elements are coupled to one another.

9. A filling machine for portioning pasty masses for food production, the filling machine comprising: a filling flow divider; and dosing elements in the filling flow divider for adjusting a volume flow, wherein the dosing elements are either driven via a joint motor and are coupled such that there will be an equal volume flow in each line downstream of the respective dosing element, or the dosing elements are configured as vane wheels which rotate freely about an axle and the dosing elements are coupled to one another; wherein a feed mechanism is configured to feed a pasty mass into the filling flow divider, wherein the filling flow divider is configured to separate the pasty mass into a plurality of mass flows and to discharge portions in a discharge direction, wherein an end of each portion is a tear-off point between the portion and a subsequent portion, wherein the filling flow divider is configured to suck back the portion being discharged in a direction opposite to the discharge direction when the portion is being discharged but is not yet separated from the subsequent portion via separation at the tear-off point between the portion being discharged from the filling flow divider in the discharge direction and the subsequent portion upstream in the filling flow divider, thereby causing separation of the portion being discharged from the subsequent portion upstream in the filling flow divider and resulting in a discharged portion that is separated from the subsequent portion upstream in the filling divider, wherein the separated plurality of mass flows pass through respective dosing elements, wherein the dosing elements are configured to run backwards at the end of the portion as each of the plurality of mass flows is sucked back in the direction opposite to the discharge direction, wherein the portions being discharged are configured to be separated from subsequent portions by singulating, which is separating portions via only tearing off achieved by a relative movement of the portion being discharged relative to the subsequent portion by: carrying along the portion being discharged with a conveying unit, and/or a lifting movement of the filling flow divider or of discharge ends of the filling flow divider, and/or a gravitational forcing due to a weight force of the portion being discharged.

Description

BRIEF DESCRIPTION OF THE FIGURES

[0027] In the following, the present disclosure will be explained in more detail making reference to the following figures:

[0028] FIG. 1 shows, in a highly schematic representation, an embodiment according to the present disclosure.

[0029] FIG. 2 shows, in a perspective view, a preferred embodiment according to the present disclosure.

[0030] FIG. 3 shows, in a perspective view, a detail of a filling flow divider comprising rotatably fastened tubes.

[0031] FIG. 4 shows schematically, in a perspective representation, tubes with hose connection according to a further embodiment of the present disclosure.

[0032] FIG. 5a and FIG. 5b show diagrams illustrating the feed volume of the feed mechanism of the filling machine and the feed volume of a dosing element as a function of time.

[0033] FIG. 6 shows, in a highly schematic representation, an embodiment according to the present disclosure with a conveyor belt downstream of the filling flow divider.

[0034] FIG. 7a, FIG. 7b, FIGS. 7c, and 7d show schematically embodiments comprising a self-closing membrane.

[0035] FIG. 8a, FIG. 8b, FIG. 8c, FIGS. 8d, and 8e show the chronological sequence of an embodiment of a method according to the present disclosure.

[0036] FIG. 9a, FIG. 9b, FIGS. 9c, and 9d show the chronological sequence of a further embodiment of a method according to the present disclosure.

DETAILED DESCRIPTION

[0037] FIG. 6 shows a device according to the present disclosure. The filling machine 1 comprises a hopper 14 for receiving therein the pasty mass. The term pasty mass is here used e.g. for: sausage meat, dough, jam, creams, nut mass, etc. The filling machine 1 is e.g. a vacuum filler. The filling machine comprises a feed mechanism 10, which feeds the pasty mass to an outlet 15, e.g. an outlet tube. The feed mechanism may e.g. be a vane pump or a worm pump, etc. A filling flow divider 2 of the type shown e.g. also in FIGS. 1 and 2 is arranged downstream of the outlet 15 in the discharge direction. The filling flow divider divides the mass flow fed by the feed mechanism 10 into a plurality of n mass flows, e.g. four flows in FIG. 1, and e.g. eight flows in FIG. 2. To this end, the joint line 16 branches into a plurality of lines 7a, 7b, 7c, 7d.

[0038] To ensure a constant volume flow in the individual lines with the pressure drop, dosing elements 3a, b, c, d are arranged in the respective lines. In FIG. 1, the dosing elements are arranged schematically in the branching lines, but they may also be arranged at the beginning of the lines 7. The dosing units allow the volume flow to be adjusted in the respective lines. The dosing elements may be driven via a motor 5, preferably via a joint motor 5, and may e.g. be coupled such that there will be an equal volume flow in each line downstream of the respective dosing element.

[0039] The dosing elements 3a, b, c, d may also be driven by the product, i.e. the pasty mass, and may be configured e.g. as vane wheels, which rotate freely about an axle and are preferably coupled to one another, i.e. they rotate about a joint axle.

[0040] The dosing elements 3a, b, c, d are followed by the respective lines, e.g. tubes 7a, b, c, d and/or hoses 8a, b, c, d and/or nozzles 9a, b, c, d. As can be seen e.g. in FIG. 4, a respective line may be defined by a combination of a tube 71, a hose 8, a tube 72 and a nozzle 9. FIG. 4 shows e.g. two lines with hoses 8 that may be attached to a separate bar. The use of a hose allows, due to the flexibility, the lines to be bent and adjusted in a suitable manner. The lines can thus easily be positioned accurately. Moreover, the use of hoses is also cost-effective. Furthermore, hoses are also easy to manufacture and offer advantages as regards the lower weight.

[0041] FIG. 3 shows a further variant, in which the dosing elements 3 are arranged in a housing, with tubular connection pieces 26 projecting from the housing, which have attached thereto curved tubes 8a, 8b, here in combination with nozzles 9a, 9b. The curved tubes 8a, 8b are fastened in a rotatable manner. This means that the distance between the discharge ends 12 can be varied. The rotatably arranged curved tubes can then be fixed at the desired position.

[0042] The fact that the curved tubes 8a, 8b are curved allows the discharge end 12 and the free discharge area, respectively, to be directed downwards in the direction of a surface onto which the portions are discharged, the free discharge opening being located in a plane that is inclined by 0? to 60?, preferably by 0? to 45?, relative to a plane in which the surface onto which the portions are discharged lies. An arrangement of this kind proved to be advantageous, since the discharged product will then drop due to the force of gravity. The device according to the present disclosure does not necessitate the use of a specific separating unit for separating the individual portions. The separation can take place through tearing off caused by a relative movement of the discharged portion relative to the subsequent portion, in particular by carrying along the discharged portion with a conveying unit 6, here the conveyor belt 6. However, also a lifting movement of the filling flow divider allows tearing off. To this end, a lifting unit is provided, which is not shown here and via which the filling flow divider can move in a vertical direction relative to a surface and a conveying unit, respectively.

[0043] The filling machine according to the present disclosure also comprises a control unit 11, through which the filling machine 1 and its filling flow divider 2 are controllable. The control unit 11 may be integrated in the filling machine. The control unit in its entirety may, however, also be divided, so that one part of the control unit is arranged on the filling flow divider and the other part in the filling machine. Also the conveying unit 6 may be controlled via the control unit 11 or via a separate controller.

[0044] At the discharge end 12 of the filling flow divider, i.e. preferably at the discharge end of the lines 7, a self-closing membrane 13 may be arranged, which is shown in FIG. 7a, b, c, d. A membrane 13 of the type in question, here in particular a slotted membrane, opens when the pasty mass moves in a discharge direction A. In the course of this process, the membrane parts separated by slots move outwards, as shown by the arrows. Such a squeeze membrane is also used e.g. for plastic food containers, such as ketchup bottles.

[0045] In the embodiment shown in FIG. 7a, the membrane comprises a hollow, outwardly directed protrusion 31, with slots 30 being located in the area of the protrusion and converging towards a point P. When pressure is applied to the membrane by the mass flow, the area between the slots 30 will open, as indicated by the arrows, and the passage opens. When the pressure decreases and the pasty mass is sucked back, the membrane parts will automatically close again (FIG. 7a, 7b). FIG. 7c and d show a further embodiment, in which the membrane 13 is located e.g. substantially in one plane and has, as described above, a plurality of slots 30 that converge towards a point P. As indicated by the arrows, the membrane parts open outwards in response to pressure in the line 8 and close when, for example, the pressure decreases or the pasty mass is sucked back.

[0046] In order to discharge portions of exact weight without any pasty mass overrunning, the method following hereinafter is preferably executed.

[0047] Pasty material is filled into the hopper 14 and fed in the manner known via the feed mechanism in the direction of the filling flow divider 2. As explained in connection with FIG. 1, the mass flow is divided into a plurality of n mass flows in the filling flow divider 2, the volume flow being adjusted via dosing elements 3a, b, c, d, preferably such that the volume flow of all subflows is equal. To this end, the dosing elements can be driven in a suitable manner via a motor 5. The sum of the volume subflows corresponds here to the volume flow generated by the feed mechanism 10.

[0048] The pasty mass is then discharged from the lines 7 of the filling flow divider 2. At the end of each portion, the mass flow is sucked back in a direction opposite to the discharge direction.

[0049] At the end of a portion thus means at the tear-off point of the mass flow, i.e. the boundary to the following portion. This means that a portion volume V.sub.p corresponding to one portion can be discharged at the discharge end of the filling flow divider after a predetermined volume V.sub.1 has been fed through the respective dosing elements in the discharge direction. This means that at the end of the portion V.sub.p, the mass flow is briefly sucked back in a direction opposite to the discharge direction A, whereupon the predetermined volume V.sub.1, which corresponds to the volume of a portion V.sub.p plus the sucked-back volume V.sub.r, is again conveyed in the discharge direction A.

[0050] It will be particularly advantageous, when, at the end of a discharged portion V.sub.p, also the feed mechanism 10 runs backwards in a suitable manner. Hence, also the feed mechanism of the filling machine can run backwards after having fed a certain volume V.sub.f in the discharge direction. The volume V.sub.f fed by the feed mechanism of the filling machine in the discharge direction A will then correspond to the volume of n discharged portions (when the flow is divided into n subflows by the filling flow divider) plus the volume V.sub.R sucked back by the feed mechanism 10. The volume V.sub.R sucked back by the feed mechanism can thus substantially correspond to the sum of the volumes V.sub.r sucked back by the dosing elements, i.e. n V.sub.r. If, for example, dosing elements are used, which are driven by the product, it can be accomplished that, due to the vacuum generated by the backward-running feed mechanism, also these dosing elements will move backwards, e.g. that the vane wheels rotate about the axis in a backward direction or that the vane wheels are moved backwards by a separate unit.

[0051] This means that the feed mechanism 10 and the dosing elements 3a, b, c, d feed, as can in particular also be seen from FIG. 5, a feed volume V.sub.f, i.e. in FIG. 5 the area below the individual graphs. When a predetermined volume has been fed by the pump 10, the pump 10 starts to run backwards, as can be seen in FIG. 5a, thus sucking the pasty mass in a direction opposite to the discharge direction A. The volume V.sub.R sucked back by the pump 10 corresponds approximately to n * V.sub.r, i.e. the volume sucked back by the dosing elements 3.sub.n multiplied by the number n of dosing elements. The duration of the backward movement of the feed mechanism 10 is in a range of up to 1 second. FIG. 5b shows the feed volume as a function of time of a single dosing element 3a, b, c, d. As can be seen from FIG. 5, e.g. the feed volume V.sub.1, which corresponds to the hatched area below the graphs, is e.g. 1/n, here a quarter of the total feed volume, n corresponding to the number of divided volume flows. When a respective volume Vi has been conveyed by the dosing element 3a, the dosing element will also here run backwards, as can be seen in FIG. 5b. The volume V.sub.r sucked back corresponds here to 0.5% to 1000% of the volume in the line. This means that, in this embodiment, e.g. the volume sucked back by the feed mechanism substantially corresponds to the sum of the volumes V.sub.r, sucked back by the dosing elements.

[0052] The embodiment shown in FIGS. 5a and 5b is only one example. The aspect of essential importance is that the feed volume, as shown in FIG. 5b, is sucked back at the end of a portion in a direction opposite to the discharge direction A so as to prevent the mass from overrunning. The operation of the feed pump 10 can be adapted such that the dosing units will always have fed thereto a sufficient amount of pasty mass.

[0053] FIG. 8a to e show, in a highly simplified representation, the chronological sequence of an embodiment according to the present disclosure.

[0054] In FIG. 8a, a pasty mass is fed, as indicated by the arrow, in the discharge direction A via the respective dosing element 3 (and the pump 10, which is here not shown) through the line 7. The individual portions having a respective portion volume V.sub.p are conveyed via the conveyor belt 6. When the dosing element 3 in question has fed a certain volume V.sub.1, the pasty mass will be sucked back, as indicated by the arrow in FIG. 8b. Due to the backward movement of the pasty mass and the conveying movement of the belt 6, the pasty mass will tear at the marked tear-off point at the end of the line 7.

[0055] As shown in FIG. 8c, the portion then drops and the pasty mass has been sucked back into the line 7, i.e. a volume V.sub.r has been sucked back in a direction opposite to the discharge direction A.

[0056] As shown in FIG. 8d, the pasty mass is then again moved via the dosing units 3 in the discharge direction A, and this is continued until, as shown in FIG. 8, a volume V.sub.1 has been discharged again, where V.sub.1=V.sub.p+V.sub.r. The operation of the feed mechanism is adapted accordingly, as has been explained hereinbefore.

[0057] If the tear-off point is arranged at the end of the line 7, sucking back will take place when a portion having the volume V.sub.p has been discharged from the line 7.

[0058] This, however, is not necessarily the case. FIGS. 9a to 9d show a further embodiment, where a less viscous mass is portioned, e.g. jam into a container 25.

[0059] As can be seen from FIG. 9a, the pasty mass is moved in the discharge direction A via a dosing element 3. When a volume Vi has been discharged, sucking back will take place in a direction opposite to the discharge direction A, as shown in FIG. 9b. The tear-off point may here be located in an area between the dosing element and the discharge end of the line 7. In this case, separation is caused by sucking back and by the force of gravity. When a sufficient quantity has been sucked back, i.e. V.sub.r as shown in FIG. 9c, the pasty mass can again be fed in the discharge direction A, as shown in FIG. 9d, and fed into the next container 25.

[0060] The quantity V.sub.r to be sucked back and the moment in time of sucking back can be determined empirically for a given product and depend in particular also on the desired portion size, feed rate, internal volume of the line as well as the arrangement.

[0061] In principle, it is also possible that, if the dosing units 3a, b, c, d are driven by the filling flow, the backward movement is generated exclusively via the vacuum of the feed mechanism 10 or a vacuum is generated in the discharge direction via respective vacuum lines upstream of the individual dosing elements. An essential aspect of the present disclosure is that at the end of a portion, i.e. when a respective volume V.sub.1 has been fed by the filling flow divider, so that a portion volume V.sub.p can be discharged from the respective discharge end of the filling flow divider 2, the mass flow is sucked back in a direction opposite to the discharge direction so as to prevent overrunning.

[0062] The discharged portion is then automatically separated from the mass flow, since the adjoining pasty mass is sucked back, and tears. In particular, the separation is also caused by a relative movement between the portion and the subsequent portion, so that no movable parts will be necessary for separating the product. This allows a high cyclic output in comparison with valve technology. In the embodiment shown in FIG. 2, the portions are separated from one another by the force of gravity and/or by the movement of the conveyor belt 6.

[0063] The present disclosure is also particularly suitable for a co-extrusion unit, i.e. for a unit in which the individual portions produced in the lines have additionally applied thereto a co-extruded outer mass that is cured, if necessary. Due to the very small structural design, the product range can be considerably extended. In particular, the inner mass can be portioned precisely by means of the filling flow divider 2, i.e. very small quantities can be filled and separated in precise portions and small calibers can thus be realized.

[0064] Cleaning the system is very easy due to the simple structural design, in which no discharge or shut-off valves are arranged between the dosing units and the discharge ends 12, but only smooth, tubular inner walls come into contact with the pasty mass.

[0065] According to a further embodiment, in which the dosing elements run freely and are driven via the filling flow, the joint feed line 16 leading to the dosing elements is connected to a vacuum generating unit, so as to drive the respective dosing elements backwards. This unit may e.g. be configured as a variable-volume cylinder.

[0066] According to an additional embodiment with a non-driven filling flow divider, i.e. a filling flow divider in the case of which the dosing elements are driven via the filling flow, the axle of the filling flow divider connecting the dosing elements, e.g. the vane wheels, is connected via a freewheel to a unit, which allows to rotate the axle of the filling flow divider in a direction opposite to the discharge direction for the purpose of sucking back. Such a unit may comprise e.g. a pneumatic cylinder acting on the axle via a lever.