Helically thereaded mixing apparatus with transfermix goemetry

This invention relates to machinery for working or compounding one or more flowable media optionally in combination with powders, liquids or gases, where said, flowable media may be of any consistency including ל that of a stream of discrete particles such as lumps or powders or that of a visco-elastic solid. . It is particularly though not exclusively concerned with visco-elastic media such as rubber.

Continuously operating mixing machinery is known 10 comprising a rotor and a barrel, the rotor having an external helical thread and the barrel having an internal helical thread of opposite hand to but coaxial . with the helical thread on the .rotor, where one of said threads may form part of an entry zone., the said threads 1ל together forming a mixing zone in which, over a given axial length, the thread in one component (e.g. in the rotor). varies from a full cross-sectional area to ' :' substantially zero cross-sectional area while the thread in the other component (e.g. in the barrel) varies from 20 substantially .zero cross-sectional area to full crosssectional area and vice versa for a following mixing zone, if any. In operation a medium being transported or moved in the one component at the entry of said mixing zone will be transferred layer-by-layer from the one 2ל component (giver) to the other component (taker) into which substantially all the medium will have been transferred by the end of the mixing zone, the medium having been mixed and worked layer-by-layer during this transfer in accordance with' the conditions of relative motion between the two components.

.On account of this action, the geometry of such a mixing zone has become known in the art as a

Transfermix geometry and a device incorporating such a mixing zone or zones as a Transfermix.

A Transfermix geometry does, not depend upon a relative rotation between the two components for its essential mixing action but will operate also with the 10 two components having no rotation relative to one another and the medium being pumped through it. For example, a Transfermix geometry can be formed by a , system of vanes within an annular conduit where a medium is pumped or otherwise moved therethrough with the 15 purpose of heat exchange through or with said annular ׳ walls with said vanes extending from said annular walls in that case operating as secondary heat transferring walls. In such a Transfermix heat exchange device, a liquid or a gas may be the. medium with or without a 20 loading of a powder, and a change of state of the medium may also take place.

A Transfermix geometry may thus more generally be defined as:- a continuous mixing devicecomprising a component having an internal operating surface provided 25 with a helical thread and an interior component having an external operating surface provided with a helical thread of different direction from, but coaxial with, said helical thread on said internal operating surface, the-said threads facing one another and defining a passage for a medium to be mixed (mixing zone); the envelope of revolution defined by the crown or land of said interior thread being coincident with or a short radial distance within the envelope of revolution defined by the crown or land of said exterior thread, the cross-sectional areas of the grooves of said facing threads varying in opposite senses between a maximum ׳ and a minimum value for each said thread along substantially the same length of the said passage, whereby when in operation a medium moves along said (Jpassage, portions thereof are successively transferred between the grooves of said facing helical threads as giver and taker respectively and experience at least a and of their relative positions in the total flow, 15 change of flow-direction/on so being transferred.

A Transfermix geometry may most generally be regarded as a device for continuously applying a surface-effect and/or an edge-effect to a bulk flow of a medium for bringing about a step-wise change in a 20 property of said bulk flow to a certain degree of uniformity.

In this sense, heat-transfer is an example of a surface-effect. The application of shear-forces will be, depending on the consistency of the medium, an 25, edge-effect or a combined edge- and surface-effect.

For the initial plastification of a rubber compound from cold, we are considering a 'scissors-type' action between crossing thread-lands of the two components. Where shear-work is put into a viscous flow, there is a combined, edge- and surface-effect in that a thread-land of one component moves across a channel of the other component and the shear-stress is transferred through 5' the medium, In this case, the width-to-depth ratio of the said helical channel becomes a factor in the effectiveness of application of shear-stress and thus of the pumping action.

: Bulk flow is defined as the total flow in both 10 components at any cross-section, this being a multiple of that part of the flow which is being transferred from one component to the other at that cross-section and which is being moved most intensively on being .thus transferred. 'This among other features differentiates a Transfermix geometry from any.colloid-׳ mill ״type device in which the flow being worked is .substantially identical with the total flow being.

pumped. ..

By arranging Transfermix geometries in sequence, 20' required degrees of intensification of a surface- and/or . edge-effect may be obtained on a bulk flow or different effects may be applied to a bulk flow in sequence, each to a degree of uniformity determined by the geometry. As one of many possible examples may be quoted a rubber 25 or plastics compounding extruder, providing plastification or melting in one or more mixing zones, with shear-working and heat transfer, together with compounding and pressure build-up for extrusion in a

* '*־ following mixing zone or zones. An example of a simple edge-effect is 'chemical contacting', where a catalyst may be arranged along the edge of a thread-land.

Surface- and edge-effects are so called because . their intensity is a maximum at the surface or edge of application with the intensity dropping off with distance into the. bulk flow. The surface of revolution through which in a Transfermix geometry the. transfer of the medium takes place from the one into the other . 10 component, may be considered to be subdivided by the threads of the helical channels crossing one another. The more helical threads are provided on one or both of the components, the smaller will be subdivisions of said transfer surface and therefore the more uniform the application of the said edge- and/or surface-effects will -be.

There are, however, limits to the'multiplication of helical threads in each component because each thread must have a minimum land width for strength and the more 20 helical channels are provided to carry the bulk flow, the narrower each single channel will be until a stage is reached where the throughput will be materially . reduced. For a relative rotation of the components providing the pumping action, the transfer of shear25 stress and thus forward motion into the depths of such . channels may fail, leading to stoppages or back-flow there and in a stationary Transfermix geometry the resistance to pumping may become excessive.

For a Transfermix geometry, the extreme depths of channels will occur at opposite ends Of the mixing zone for each of the components which, however, makes the limitation no' less effective.

Such limiting effects will be easily understood with reference to Transfermix geometries of larger dimensions which are scaled up from smaller versions which may have been adequate for a required purpose.

For example, if the leading diameter and length as 10 well as the annular depth of a Transfermix geometry are. doubled, the area of the Transfer surface will be quadrupled. . Retaining the same number of helical ' channels in' each component as would happen in a true geometric, scale-up with width-to-depth ratio of the 15 channels ־the same, the number of subdivisions of the .Transfer-surface will be quartered, i.e., divided by four.

If, on the other hand, the number of helical . . channels in each component is doubled, the number of 20 subdivisions of the transfer zone will be raised to the same value as in the small Transfermix, but the widthto-depth ratio of the individual channels will have been halved, leading to the above-described loss of throughput and of general flow properties.

The above considerations explain scale-up difficulties which have been observed on Transfermix for example in application as cold-feed rubber extruders, . as well aS limitations on the performance of smaller ’ . - , units ׳in this and other applications. Such effects are not limited to the more heavily viscous materials, though in more easily flowable materials the shortcomings may not have been recognised as such, but rather can be shown as improvements not hitherto capable of realisation.

It is an object of this invention to provide a Transfermix geometry in which the uniformity (quality) of application of edge- and/or surface-effects as indicated by the number of subdivisions of the transfer zone, can be increased without reducing the rate of bulk flow by the occurrence of unfavourable width-to-depth ratios in individual helical channels.

It is a further object of this invention to provide a Transfermix geometry which can be scaled up on its leading dimensions while maintaining a required uniformity (quality) of application of edge- and/or surface-effects as indicated by the number of subdivisions of the transfer-surface without a disproportionate reduction in the rate of bulk flow by the occurrence of unfavourable width-to-depth ratios of individual helical channels.

• In relation to Transfermix geometries as applied to rubber and plasticsextruders particularly. of the cold-fed types,Jit is an object of this invention to achieve plasticisation and/or melting with low length-to-diameter ratios also for compounds which have hitherto proved difficult to plasticise in other than high length-to-diameter screw devices which incur the danger of a generalised or. localised overheating.

In these applications, it is a further object of the .invention to achieve scale-up on the same leading dimensions without loss of quality and/or output. In order to achieve the above objects, the present invention provides a continuous mixer comprising at least one mixing zone formed by a Transfermix geometry (as hereinbefore defined) in which the number of starts 10 of the helical thread changes for each of the components .along the length of said Transfermix zone in the opposite sense to the change of the cross-sectional area of helical grooves on said component, whereby when in operation a medium moves along said Transfermix zone,

15. portions thereof are successively transferred between' • the grooves of facing helical threads as giver and taker and whereby grooves of larger cross-sectional area are of greater widths than grooves of small cross-sectional area.

20. In preferred embodiments of this invention, the minimum values of groove cross-sections for each of ־' ; said threads is substantially zero, the said threads are of opposite hand and the product of- the number of starts in one said thread and the number of starts in the other said thread at any cross-section along substantially the whole length of said passage is constant.

At least one of said components may be rotatably mounted and driven to effect forward motion of said medium through said passage, the said rotatable component having maximum groove cross-sectional area at the beginning of said passage and correspondingly a minimum 10 number of thread-starts, and in advance of said passage, a transporting helical thread, having at least one start.

For embodiments adapted to media entering a mixing zone in the form of a visco-elastic solid in a transport 15 helical thread, an increase in the number of starts of said ״thread in excess of doubling will, in a preferred embodiment, commence with one’additional thread arising gradually near the leading surface of said transport thread followed by a second such additional thread at 20 a farther distance along said length and away from said leading thread surface until the full number of starts is reached, whereby in operation a blockage of the flow of said solid is avoided in -the said component and a transfer into the maximum number of grooves of 25 the other component with effective subdivision and ׳ plasticisation is achieved.

The invention will now be described by way of example and in some detail with reference to the

-ף־ accompanying drawing in which:FIGURE 1 is a sectional view of an embodiment of the invention as a cold feed rubber extruder with two Transfermix sections;

FIGURE 2 shows an alternative version of the Transfermix geometries of the rotor of Figure 1;

FIGURE 3 is a sectional view of a barrel sleeve forming the Transfermix part.of the embodiment of Figure 1;

FIGURE 4 is a developed view of a׳rotor.with two Transfermix sections with a multiple of the number of starts of the embodiment of . Figures 1-3;

FIGURE 5 is a developed view of.the barrel sleeve forming the Transfermix part with a multiple . - of the number of starts of the embodiment of

Figures 1 & 3 for use with the geometry of Figure 4;

FIGURE 6 is a view of the developed rotor of Figure 4 and of the developed barrel sleeve of

Figure 5 superimposed to illustrate the

Transfermix geometry with many starts for improved uniformity without loss of throughput and which could also represent a scale-up of the embodiment of Figures 1 - 3;

FIGURE 7 is a developed view of part of a barrel sleeve similar to Figure 5 but formed of an assembly of separately manufactured rings each having a different number of helical threads at different helix angles.

In the cold feed rubber extruder of Figure 1, the rotor 2T is rotatably mounted in the known manner in . 5 the barrel housing 22, . This has an inlet opening 23 and an outlet flange24 and both barrel and rotor have heating and cooling provisions as known in the art. Fixed to the outlet flange there could be known exit devices such as an extrusion head, a.screen pack, a 10 pelletising head, fixed cutter knives or the like,.

The rotor comprises a feed- and compressionsection 25 with a single-start helical thread 27 which leads up to the first Transfermix zone A and an exit section 26 with a two-start helical thread 28 following 15 the second Transfermix zone B. Both rotor sections 2ל and 26 run in cylindrical parts of the barrel-housing. The feed section 27 may be provided with known aids to forward transport of unplasticised rubber, such as fluting.

. In the first Transfermix zone A the barrel sleeve has a first section with a 20-start. thread 30 and a . second section with a 10-start thread 31 while in the second Transfermix zone B there is a sleeve section with a 10-start thread 32 followed by a sleeve section 2ל with a 20-start thread 33, the starts of the threads and the extent of these sections being shown below the barrel.

The rotor continues with a single-start thread 34 . in a first section and builds up. to & 4-star.t-thread 35. in this section to continue as such up to. the position of zero cross-sectional area at the- end of. Trans.fermix. zone A. In Transfermix zone B the'rotor׳starts with a־ sectional 4-start thread 36 and ends.with a sectional

2-start thread 37» this carrying on-beyond the׳ end. of Transfermix zone B as the outlet section: 26״with its׳

2-start thread 28.

, Regarding now the numbers of thread, starts shown for the barrel below and for the rotor above'the Figure, it will be seen that these vary in complementaryfashion according to the invention along the length of'each Transfermix zone.

The first section from single-start thread.34.of the rotor to 4-start thread 35 shows the . gradual build-up. from,״ single- to 4-start threads which according, to this invention, commences near the leading edge of: the single thread and new starts 38 are stepped gradually or. staggered along the section and across the width of'the single׳ groove originally formed by the 1-start thread* This avoids a: hold-up of the as yet hardly plasticised rubber which would occur if the three additional thread starts were to.arise abruptly at the same׳cross-section.

Figure 2 shows an alternative embodiment of a rotor 21, 2ל like numerals denoting like parts, in which.in Transfermixzone A eight starts 38' build up in gradual steps along and/ across the channel formed bythe original single-start thread 27 and continue as the 8-start thread 39 up to . the end of Transfermix zone A.

In contrast to the embodiment of Figure 1, the groove cross-sections formed by θ-start thread 39 do not reduce to zero, but to a minimum value and in Transfermix zone B increase again through the continuation of 8-start thread 41 into Transfermix zone B. This reduces to the 4-start thread 42 leading up to the end of Transfermix zone B. Thereafter the exit section 26 of the rotor continues with a 2-start thread 43.

< The numbers' of starts in the different sections is indicated below the rotor of Figure 2.

Figure 3 shows the barrel sleeve of Figure 1 taken out of the housing and without the rotor, to clarify its structure, like. numerals denoting like parts and 1ל the numbers of starts as well as their extent being indicated above Figure 3.

In operation, a feed of unvulcanised rubber in the form of strip, particles (pellets) or powder is introduced into the opening 23 and transported by the 20 rotor 21 towards the first Transfermix zone -A, while being compressed to eliminate air.

On entering the Transfermix zone A, the outermost layers of the flow in the rotor are transferred into the twenty starts of the stator thread 30 which commence from zero depth up to the depth-to-width ratio in the plane of the drawing of about unity. During this transfer those layers are thus subdivided and sheared for plasticisation by the relative rotation, while in the shallow barrel grooves effective forward transport takes place as a result of the same relative rotation. There are 1 x 2ό= 20 points of intersection of thread-lands or cut points'for scissors action at each cross-section here.

In the helical channel of the rotor, the new threadstart 34 emerging near the leading edge of the original single-start thread 27 penetrates into the flow of rubber, subdividing the as yet hardly plasticised material and spreading it across the helical channel as. do the other two emergent starts 34 stepped both across and along the helical channel. Thereby the forward flow in this helical channel .is not obstructed but is spread across towards the trailing edge of the original' helical channel where there is a reduced pressure and, depending on conditions, there is free space.for the

- .feed rubber to spread into.

After the gradual emergence of the three starts 34, the flow in the rotor will thereafter be־in four <

parallel helical'grooves 35 which will be full and which at their deepest points will have started from a ^:; width-to-depth ratio of about unity for good forward transport.

During development work for this invention,, the .25 additional three starts 34 were first made to emerge at the beginning of mixing zone A and this resulted in much reduced throughput. Also making one thread-start emerge at the beginning of .Transfermix zone A to halve the

׳£ ׳ י י original groove, and a little further along making the other two thread-starts emerge to halve each of the two helical channels, resulted in considerably reduced.

throughput. . This led to the stepwise emergence of ל additional threads for this case of plasticising rubber which may similarly apply to the melting of plastics but which may be less necessary for a medium which enters the mixing zone A already in a flowable state.

Opposite the 4-start rotor thread 35 there is the 10 10-start barrel thread 31 having a groove width wider than the maximum groove depth which is a good condition • for forward pumping effect. It will be seen that at each circumference here there are 4 x 10 = 40 inter-, sections of thread-lands or cut points for scissors.

action in each cross-section for bringing about a required uniformity of application of shear working as well as good forward transport. At the end of Transfermix zone A all layers of the rubber originally moving in the rotor will have been transferred into the ten helical barrel grooves, having been worked to a degree of'uniformity determined mainly by the number of cut points.

Analogously, there will be seen to be in Transfermix zone B, owing to the changes of numbers of starts, also ׳ 25 4 X 10 = 2 x 20 = 40 cut points at each cross-section, . determining the uniformity of shear application to a certain level.

With the rotor of Figure 2 in place of the 4-start

52506/2 .

rotor of Figure 1, the number of cut points at each cross-section will correspondingly be:

x 20 = 8 x 10 = 10 x 8 = 20 x 4 80 ־ for all parts of the Transfermix zones A and B, where we treat the emergent 8-start thread on the rotor as an average 4-start thread.

It has been found that in a small size Transfermix such as 3,25 inch or 82 mm diameter in which it is possible also to realize an 60 cut point per cross-section geometry without changing the numbers of starts ן according to this invention, that is to say by having j I a barrel sleeve with twenty starts all along its length ׳ and a rotor with four starts, making 4 x 20 = 20 x .4. = .80 cut point per cross-section, the results obtained on cold feed extrusion of a high performance t/uck tread compound containing a substantial proportion of natural rubber (over 50 per cent) were .,markedly. .. . ־ ._v ._ץ.^ .:..

inferior. In fact, applying the provisions of this invention provided an over 50 per cent increase in output of very smoothly extruded tread from 400 kg per i hour to 630 kg per hour and at about 5°C lower extrudate temperature, although the rotor speed could be increased from 86 to 108 revolutions per minute.

The number of cut points per circumference will serve, within limits, to differentiate Transfermix geometries of the same diameter, but for comparing

Transfermix geometries of different sizes it is advisable to use subdivision of circumference as a characterising length. For .example, for the 80 cut points on a . 3.25 inch diameter this would be the circumference of 10.21 inches ״ . .,’ .

= 0.128 inches = 3.24 mm. This would be the length of subdivision of circumference one would use as a guide towards obtaining a similar performance on scaling up a cold feed Transfermix extruder, at least in the first or plasticising Transfermix zone A.

Figure 4 shows, as a developed view, a rotor 50 with feed section.1 having a single-start thread 51 which at entry into the Transfermix zone A becomes an 8-start thread 52 with a stepwise transition 53 commencing at the ,leading edge of the single start thread, similarly as described with reference to Figures 1 and 2.

Proceeding further into the Transfermix zone, the 8-start thread subdivides by regularly distributed doubling into a 16-start thread 54 and farther along this subdivides similarly into a 32-start thread 55, corresponding to reducing groove depths towards the end of Transfermix zone A with substantially zero groove cross-section. In Transfermix zone B there is first the 32-start .

thread 56, going by regularly distributed halving to 16-start thread 57 and similarly to 8-start thread 58 towards the end of Transfermix zone B, to continue as

2-start thread 59 in the exit zone.

In Figure 5 is shown in developed view a corresponding barrel sleeve 60 commencing at the beginning of Transfermix zone A with a 40-start thread 61 at minimum depth, followed by a 20-start thread 62 and a 10-start thread 63 by the end of Transfermix zone A. In Transfermix zone B we׳ have conversely the 10-start thread 64 of maximum groove depth, followed by the

20-start thread 65 and 40-start thread 66 of reducing groove depths.

Figure 6 is the superimposition of Figures 4 and 5 which shows that except for the emergent 8-start thread 52 at the very beginning of Transfermix zone A, 10 . where the cut points increase from 40 to 320, the rest of the Transfermix zones A and B have 320 cut points per circumference, using helical grooves'which get wider with increasing depth and'vice versa for/keeping up the conditions for good forward transport.

. Using the subdivision length determined for the

3.25 ״inch Transfermix of 0.128.inch, we can calculate the circumference of the larger Transfermix having 320 cut points for equivalent plastification conditions, as 320 x 0.128 inch = 40.96 inches or the diameter as 20 . 320 ' .

--- x 3.25 inch = 13 inches. 80

Taking into account that rubber extruders are operated mostly on constant circumferential speed so that residence time increases with the leading dimension, the influence of this factor will permit a bigger

Transfermix to be made with this geometry for equivalent performance,׳

Figure 7 shows diagrammatically five separate rings

71, 72, 73» 74 and 75 which are made to be joined together to form a barrel sleeve 70. This assembly of rings, similarly to barrel sleeve 60 will be inserted into the barrel of the Transfermix where the rings can 5 be keyed with, the barrel or with each other or both to take up the torque transmitted by.the medium during, operation and thus to prevent rotation.

. Ring 71 has.a 40-start thread 76 with a helix-angle of.68°, ring 72 a 20-start thread 77 with a helix angle 10 of 59°, ring 73 a 10-start thread 78 with a helix angle of 59°, and rings 74 and 75 have 10-start threads 79 and 80 with helix angles of 59° and 68° respectively.

This indicates that, depending on the nature of the surface-effect, it. is intended to apply, for example shear with a material which reduces in viscosity fairly quickly with plasticisation, one can use a change of helix angle towards 45°, the angle of maximiim. forward transport (sin 4ל° x cos 45° is a maximum) to keep the helical grooves shallower, and thereby the width-to-depth 20. ratio of the grooves higher, in addition to reducing the number of threads with increasing groove depth.

In the barrel sleeve 70, the second mixing zone will be seen to have a 10-start thread only, though with stepwise changing helix angles from ring to ring. Together 25\ with this barrel could be used a rotor having, for example, . an 8-start thread for a Transfermix in which the first or plasticising mixing zone has a 320 cut point geometry and a second mixing zone has an 80 cut point geometry for less ־ 9/ . work input into an already.- plasticised material.

Similarly as with barrel sleeves, rotors can be made up of rings having., in. that case, their sections of helical threads on their outsides and which are then -ל fitted together, for instance on an internal spindle . while also being keyed together for transmission of .

. torque. .

Making up rotors׳or.barrel.sleeves from ring . sections will be advantageous׳ for bigger sized unCT׳״» 10 as such rings can be manufactured more easily and this might well compensate for-the:additional work of making the rings fit together properly and making certain that heating, and .cooling can be accomplished without leakages.

1ל ' Moreover Transfermix parts of rotors and barrel inserts can then be made..from 'ring-section's kept in stock, to build up different Transfermix geometries needed.

When making. Transfermix geometries out of rings 20 . these can be designed for assembly in different relative . angular positions so that potentially continuous threadstarts may or may not register with, each other.

If the thread-starts are arranged out of register with each other, additional stream-splitting features 2ל can be introduced. These could׳ also be realised in Transfermix not made up of rings.