GB1568888A - Creación de Inventos y Patentes con Inteligencia Artificial

GB1568888A – Extrusion and mixing apparatus
– Google Patents

GB1568888A – Extrusion and mixing apparatus
– Google Patents
Extrusion and mixing apparatus

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Publication number
GB1568888A

GB1568888A
GB21149/77A
GB2114977A
GB1568888A
GB 1568888 A
GB1568888 A
GB 1568888A
GB 21149/77 A
GB21149/77 A
GB 21149/77A
GB 2114977 A
GB2114977 A
GB 2114977A
GB 1568888 A
GB1568888 A
GB 1568888A
Authority
GB
United Kingdom
Prior art keywords
barrel
rotor
groove
zone
stock
Prior art date
1977-05-19
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)

Expired

Application number
GB21149/77A
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)

Individual

Original Assignee
Individual
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
1977-05-19
Filing date
1977-05-19
Publication date
1980-06-11

1977-05-19
Application filed by Individual
filed
Critical
Individual

1977-05-19
Priority to GB21149/77A
priority
Critical
patent/GB1568888A/en

1980-06-11
Publication of GB1568888A
publication
Critical
patent/GB1568888A/en

Status
Expired
legal-status
Critical
Current

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Classifications

B—PERFORMING OPERATIONS; TRANSPORTING

B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL

B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS

B29B7/00—Mixing; Kneading

B29B7/30—Mixing; Kneading continuous, with mechanical mixing or kneading devices

B29B7/34—Mixing; Kneading continuous, with mechanical mixing or kneading devices with movable mixing or kneading devices

B29B7/38—Mixing; Kneading continuous, with mechanical mixing or kneading devices with movable mixing or kneading devices rotary

B29B7/40—Mixing; Kneading continuous, with mechanical mixing or kneading devices with movable mixing or kneading devices rotary with single shaft

B29B7/42—Mixing; Kneading continuous, with mechanical mixing or kneading devices with movable mixing or kneading devices rotary with single shaft with screw or helix

B29B7/425—Mixing; Kneading continuous, with mechanical mixing or kneading devices with movable mixing or kneading devices rotary with single shaft with screw or helix with screw surrounded by a casing provided with grooves or cavities

B—PERFORMING OPERATIONS; TRANSPORTING

B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL

B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS

B29B7/00—Mixing; Kneading

B29B7/30—Mixing; Kneading continuous, with mechanical mixing or kneading devices

B29B7/34—Mixing; Kneading continuous, with mechanical mixing or kneading devices with movable mixing or kneading devices

B29B7/38—Mixing; Kneading continuous, with mechanical mixing or kneading devices with movable mixing or kneading devices rotary

B29B7/40—Mixing; Kneading continuous, with mechanical mixing or kneading devices with movable mixing or kneading devices rotary with single shaft

B29B7/42—Mixing; Kneading continuous, with mechanical mixing or kneading devices with movable mixing or kneading devices rotary with single shaft with screw or helix

B29B7/428—Parts or accessories, e.g. casings, feeding or discharging means

B—PERFORMING OPERATIONS; TRANSPORTING

B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL

B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS

B29B7/00—Mixing; Kneading

B29B7/74—Mixing; Kneading using other mixers or combinations of mixers, e.g. of dissimilar mixers ; Plant

B29B7/7476—Systems, i.e. flow charts or diagrams; Plants

B29B7/7495—Systems, i.e. flow charts or diagrams; Plants for mixing rubber

B—PERFORMING OPERATIONS; TRANSPORTING

B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL

B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING

B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor

B29C48/25—Component parts, details or accessories; Auxiliary operations

B29C48/36—Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die

B29C48/395—Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die using screws surrounded by a cooperating barrel, e.g. single screw extruders

B—PERFORMING OPERATIONS; TRANSPORTING

B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL

B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING

B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor

B29C48/25—Component parts, details or accessories; Auxiliary operations

B29C48/36—Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die

B29C48/50—Details of extruders

B29C48/505—Screws

B29C48/56—Screws having grooves or cavities other than the thread or the channel

B—PERFORMING OPERATIONS; TRANSPORTING

B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL

B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING

B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor

B29C48/25—Component parts, details or accessories; Auxiliary operations

B29C48/36—Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die

B29C48/50—Details of extruders

B29C48/68—Barrels or cylinders

B29C48/685—Barrels or cylinders characterised by their inner surfaces, e.g. having grooves, projections or threads

B29C48/686—Barrels or cylinders characterised by their inner surfaces, e.g. having grooves, projections or threads having grooves or cavities

B—PERFORMING OPERATIONS; TRANSPORTING

B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL

B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING

B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor

B29C48/03—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor characterised by the shape of the extruded material at extrusion

Description

(54) EXTRUSION AND MIXING APPARATUS
(71) 1, PAUL GEYER, a Citizen of the
United States of America, residing at 15660
Tacoma, Detroit, Michigan 48205, United
States of America, do hereby declare the invention for which I pray that a patent may be granted to me, and the method by which it is to be performed to be particularly described in and by the following statement:
This invention relates to an apparatus for the mixing and extrusion of thermo-plastic and thermo-setting materials.
Preferably the apparatus is a screw or worm type for the mixing and extrusion of varied viscosity, natural and synthetic rubber and elastomeric material. Unless otherwise indicated, the term «extruder» as used herein, refers to and includes screw or worm type apparatus used to obtain an extrudate of desired cross-sectional configuration and/or for the mixing, blending, milling of thermo-plastic or thermo-setting compounds.
Conventional extruders include a barrel, a screw type rotor mounted within the barrel and adapted for rotational movement relative to the barrel and a means of introducing the material to be processed into the extruder, such as a hopper and its associated apparatus, if any. e rotor is provided with various threaded configurations, and rotational movement of the rotor relative to the barrel forces the material being processed through the barrel and out of the downstream end of the extruder. While the processed material is being discharged from one end of the extruder, hot or cold unprocessed material is fed into the feed hop per at the opposite end of the extruder to thereby make the extrusion process continuous.
Examples of the prior art are shown in
U.S. Patent 3,632,255, U.S. Patent 3,375,549, and U.S. Patent Re. 26,147.
Although many problems relative to the extrusion of plastic materials have been solved, dispersion, blending and temperature control are continuing problems, by which the quality of extrusion is measured.
In mill mixing, where the stock is banded on one roll and rotated through the mill bank and nip, a sample of the band will show that the stock adjacent to the mill roll has not been sheared or moved. This is an example of unequally sheared or poorly mixed stock. A mill man to achieve, «best mill mixing» will cut the mill band, roll the stock into a long roll or «pig», which he then feeds into the mill nip. What happens is an elongation of the stock particles as they are drawn through the mill nip.
Rolling and feeding at an angle, the particles, which are now short lines, are elongated into areas. Thus, dispersion of particles is obtained with minimum stock shearing and minimum power usage.
The design of an extruder limits the stock flow to a fixed labyrinth formed by the rotor groove and barrel groove configuration.
This invention provides a combination of interacting rotor and barrel grooves that shear and elongate the stock particles in a similar manner as that of «best mill mixing».
Extruder mixing is improved directly as the member of grooves or leads, but for the purpose of clarity the following discussion will deal with a single lead design.
The stock from the hopper enters the mixing stage of the apparatus via the rotor groove. The mixing stage is comprised of two zones, first a rotor to barrel stock transfer zone, then a shorter barrel to rotor stock transfer zone. The barrel to rotor zone may be one half to one twentieth as long as the rotor to barrel zone.
It is preferably about one fourth as long.
In the rotor to barrel zone stock is trans ferred from a rotor groove to a barrel groove and in the barrel to rotor zone stock is transferred from a barrel groove to a rotor groove.
In the rotor to barrel zone, the rotor is fitted with a rotor groove which is proportioned with decreasing extrusion capacity, so that, all or substantially all or part of the stock, as an example, three quarters of the stock is caused to flow outward uniformly along the length of the zone. This stock is received by a spiral barrel groove or «mixing pocket». Extrusion capacity of a rotor groove is related to the groove dimensions, where the rotor groove is reacted by a smooth barrel. However, where the reacting surface is discontinuous, as in a grooved barrel, groove dimensions do not necessarily correlate with extrusion capacity. Extrusion capacity therefore is the volume of stock caused to flow through the extruder by combined action of the rotor and barrel grooves.
Stock in the rotor groove, receives shearing and elongation of the stock particles as it is conveyed along the rotor groove by extruder action. As stock is transferred to the barrel it is sheared from the rotor groove, elongating stock particles, as the first step in obtaining dispersion. The sheared stock is accumulated in the barrel mixing pocket or groove in the form of a spiral wound cone, with the large part of the cone downstream.
While the transfer of less than all of substantially all of the stock of the barrel may represent less mixing action than that received by the transfer of all of the stock or material, the ratio of rotor to barrel and barrel to rotor stock can be tailored to suit stock mixing and blending requirements.
The barrel to rotor zone is relatively short and is designed to combine the barrel and rotor stock flows into the rotor groove.
To obtain «best mill mixing» the stock flow from the barrel groove is turned by the abrupt transfer design of the down stream end of the barrel groove so that stock elongation flow lines enter the «shear area», that is the circumference of rotor or barrel bore at an acute angle, that is, the stock is reoriented as it is presented to the shearing action of the rotor.
One form of barrel groove discharge end recognizes that the stock flow tends to be faster at the outer portion of the barrel groove. Therefore, a baffle is provided so that pressure flow at the inner portion of the groove causes the stock to turn and flow out of the groove. This flow is assisted by diminishing the groove depth. The barrel groove end may also be fitted with a stock flow divider, which divides the cone of stock into two columns, tending to stabilize the orientation of the stock and provide additional barrel reaction to the rotor for developing extrusion capacity.
The change of lead can be positive or or negative. The two maximum conditions being, first circumferential or zero lead, and second axial or infinite lead, if a negative is undesirable for stock clean-out reasons.
It is recognized that the orientation of stock in an extruder groove tends to be circumferential at the surface and across the groove sub-surface. Therefore it is the object of the groove design to obtain maximum stock orientation. A device to accomplish this is a plow at the trailing edge of the groove, which twins under the circumferential flow ing stock, forcing it to flow axially into the barrel to rotor zone.
Change in groove depth can be circumferential, axial, or along the groove, again it is the object of the design, to obtain right angle orientation of the stock flow lines.
The aforesaid stock flow patterns are ideal and not fully obtainable, but even partial orientation is a significant improvement. Also, it must be recognized that a combination of designs is possible to obtain the desired orientation. Where less than substantially all of the stock is transferred to the barrel groove in the rotor to barrel zone the stock not transferred, for example, the aforementioned one quarter of the stock not transferred to the barrel groove, is conveyed by the rotor from the rotor to barrel zone directly into the barrel to rotor zone of the rotor. The rotor being continuous, but enlarged in cross-section permits the rotor groove to be offset so that the rotor stock enters the enlarged portion of the rotor groove only after some stock or material from the barrel groove has transferred to the rotor. The object of this design is to place the rotor stock in a preferred position to be transferred upon reaching a second mixing stage.
Also, as the aforementioned one quarter of the stock in the rotor groove nears the end of the rotor to barrel zone, the rotor groove can be fitted with dividers, so that numerous columns of stock enter the enlarged portion of rotor at the barrel to rotor zone.
The barrel to rotor zone is followed by simple extruder zone, that is a spiral groove rotating relative to a smooth cylindrical barrel. This section acts as a bearing area to guide the rotor and develops pressure for extrusion flow.
The preferred design of the mixing stage, i.e., rotor to barrel zone, is such that the extrusion capacity of rotor and barrel grooves is such that the rotor to barrel zone develops stock flow pressure when operated at its designated capacity.
The frugal use of power permits multigroove and multi-stage designs. The preferred design uses a rotor to barrel zone with four start similar screw grooves communicating with four to six start barrel grooves or mixing pockets. The said four and six start grooves although similar can have different extrusion rates to effect extrusion blending. For the ultimate in mixing three mixing stages in series can be used to process thermo-setting stocks at a safe temperature.
The basic form of extruder is essentially a long channel, so that sequence of entering material is the same as that of leaving.
Some blending is obtained as the stock is formed into a long helix, the center of which tends to lag the extremes. High die pressures accent this lagging called pressure flow. Actually, it is back pressure flow.
This means that blending has been achieved by back pressure flow only, a wasteful expenditure of power.
The present invention provides means for obtaining a designed amount of blending.
A mixing stage with both rotor and barrel grooves has two rates of extrusion. The stock transmitted by the rotor arrives at the receiving barrel to rotor zone ahead of that transmitted by the barrel groove. This displacement takes place with no expenditure of power as such. The degree of blending can be designed. By altering the relative capacities of the rotor and barrel extrusions, a wide range of blending is possible. This range of blending makes continuous mixing possible with less accurate continuous weighing equipment.
The temperature rise in an extruder results from the work required to shear the stock. As the extruder rotor design is fixed each turn of the rotor produces the same shearing action on the stock and requires the same work input. Thus, the work input is proportional to the rotor speed. Heat transfer from the extruder tends to be a constant, determined by stock temperature and cooling system constants. The result is that stock discharge temperatures rise with rotor speed. Therefore, when stock temperatures are critical the rotor speed is limited.
As stocks of various viscosities (and heat generating abilities) are processed by a mixing line including an internal mixer, the extruder has to be sized to process the mixing capacity of the internal mixer, when the mixer is processing the most viscous stock.
This results in either a large, low revolution per minute extruder mixer, or one with minimal mixing ability. The large, low revolution per minute mixer extruder results in high capital expenditure in hardware and torque, which cannot be effectively used on low viscosity stocks.
The minimal mixing ability extruder at higher revolution per minute can economi
cally process the high viscosity stocks, but is even more ineffective in processing the low viscosity stocks. An ideal extrusion mixer for use with an internal mixer would be a
small, high revolution per minute mixer that imparts its full power capability to the mix regardless of stock viscosity and at capacity determined by the internal mixer. In the case of an extrusion mixer, used independently of an internal mixer on re-mills of final mix or curative incorporation, temperature of discharge can be even more important. In cases where curatives are added, discharge temperature must be high enough to melt sulphur and low enough not to initiate cure. This temperature spread can be as low as twenty degrees F. Again, with stocks of varying viscosity rotor speed alone is not a satisfactory means of temperature control.
As extrusion equipment has to be competitive with other milling equipment, lack of temperature control has reduced the number of installations where extrusion mixing can be used.
In view of the foregoing, it can be seen that temperature control is of the utmost importance, if a variety of stocks are to be processed. An extruder mixer compares to an internal mixer with a fixed cycle time.
A feature of the invention is to provide a variable cycle time for an extruder mixer.
It is accomplished by means of throughput or capacity per turn control. As the capacity per turn is reduced and the same work work per turn supplied to the rotor, more work per pound is expended on the stock.
The capacity per turn control is accomplished by altering the extrusion capacity of the barrel to rotor zone. This previously described zone is of short length, as measured on the rotor axis, and is designed to transfer stock, from the barrel groove to the full area rotor groove of this zone. The extrusion capacity of this zone can be reduced by moving the rotor forward so that the barrel groove discharge is aligned with a smaller area rotor groove at the downstream end of the rotor to barrel zone. This restriction reduces extrusion capacity, so that the work per pound is increased and, thereby, the extrusion temperature. This method does not waste power because, with lower throughput, sheared stock sections become thinner, thereby increasing the shearing or mixing per stock unit. The rotor position can be set at any point between minimum and maximum restriction. This allows a setting to be found, to satisfy capacity and discharge temperature for a wide range of stock viscosities. The minimum restriction setting established the required milling for the hardest or most viscous stock. Rotor design is established to process the hard
stock at the desired capacity, discharge tem
perature, rotor speed near full power of the
drive motor.
Softer or less viscous stocks require less
torque to drive the rotor. Power input is
now restored by restricting the extrusion capacity and increasing rotor speed to compensate for lower torque. Thus, near full power can also be usefully used to mix the softer stocks.
The unit now approaches the ideal extrusion mixer as it can impart full power mixing to hard and soft stocks alike and hold desired capacity and discharge temperature.
One advantage of the invention is capability of dispersing particles of a mix with minimum shearing and, therefore, least degradation to the stock polymer. Further, stock is blended as it traverses the rotor and barrel of the apparatus. Temperature of the extrudate at discharge can be controlled by means of altered extrusion characteristics of rotor and barrel configurations.
In addition the apparatus can be set to perform varied amounts of mastication of the stock as it traverses the apparatus, can be operated at a range of rotor speeds and discharge extrudate at the same set temperature, and can be operated at higher rotor speeds so as to minimize capital expenditures.
Moreover, the apparatus is capable of
combining cold fed ingredients into a homogeneous mix and at the desired extrusion temperature. When operated in conjunction
with an internal mixer the apparatus can be
set to contribute most of its power to the mix regardless of stock viscosity.
In the drawings:
Figure 1 is a sectional view of a preferred embodiment of the present invention
as applied to process rubberlike compounds,
discharged from an internal mixer;
Figure 2 is a fragmentary elevational view
of the grooves of the rotor member in a typical mixing stage;
Figure 3 is a surface development of a
typical groove of the rotor member, show
ing lead and width;
Figures 4 through 8 inclusive are sec
tional views of a typical rotor groove,
taken progressively along the groove of the rotor member as shown in Figure 3;
Figure 9 is a sectional view of the mix
ing pocket or groove of the barrel member,
using change of lead for stock reorienta- tion;
Figure 10 is a surface development of
a typical mixing pocket or groove of the barrel member, using change of lead for
stock reorientation;
Figures 11 through 15 inclusive are sectional views of the barrel mixing pocket or groove, taken progressively along the pocket or groove as shown in Figure 10;
Figure 16 is a sectional view of the barrel mixing pockets or grooves, using a ring type baffle for stock reorientation and representing a modification of the present invention;
Figure 17 is a surface development of a typical mixing pocket or groove using ring type baffle for stock reorientation as shown in Figure 16;
Figures 18 through 22 inclusive are sectional views of barrel mixing pockets or grooves, taken progressively along the pocket or groove as shown in Figure 17;
Figure 23 is a sectional view of the stock mixing stage, which incorporates means of longitudinally displacing the rotor member relative to the barrel member, with the bottom cut-away representing stock flow with the rotor in a minimum restrictive position;
Figure 24 is a sectional view of the stock mixing stage with the rotor member shifted forward to a restrictive position and with the bottom cut-away representing stock flow and depicting high flow rate location to decrease extrusion capacity;
Figure 25 is a fragmentary elevational view of the grooves of a rotor member of modified design in a typical mixing state;
Figure 26 is a surface development of a typical groove of the rotor member shown in Figure 25, showing lead and width;
Figures 27 through 33 inclusive are sectional views of a typical rotor groove, taken progressively along the groove of the rotor member as shown in Figure 26; Figure 34 is a sectional view of the mixing pocket or groove of a barrel member of modified design, using change of lead for stock reorientation;
Figure 35 is a surface development of a typical mixing pocket or groove of the barrel member shown in Figure 34, using change of lead for stock reorientation;
Figures 36 through 40 inclusive are sectional views of the barrel mixing pocket or groove, taken progressively along the pocket or groove as shown in Figure 35;
Figure 41 is a sectional view of the barrel mixing pockets or grooves of a barrel member of modified design, using change of lead for stock reorientation;
Figure 42 is a surface development of a typical mixing pocket or groove of the barrel member shown in Figure 41; and
Figures 42 through 49 inclusive are sectional views of barrel mixing pockets or grooves, taken progressively along the pocket or groove as shown in Figure 42.
Referring to the drawings, Figure 1 is a sectional elevation view of the extrusion apparatus A in accordance with the invention and is the preferred embodiment of the invention as applied to a natural and synthetic rubber stock and materials and particularly as fed thereto hot from an internal batch mixer. The extrusion apparatus A has a barrel or barrel member 10, provided with a uniform diameter bore 11, extending therethrough which acts in com bination with rotor, screw or screw member 12, rotatably mounted therein. The rotor member 12 is adapted to be rotated by a variable speed drive means 13 as is conventional in the art.
The barrel member 10 is provided at the feed end thereof with a hopper opening 14 in the top thereof, or on the side thereof, and remote from the discharge end 15 of the barrel member 10, through which stock to be processed is introduced into the apparatus A.
The rotor member 12 is provided with a single start helical groove 16 which when filled with stock from hopper opening 14 and rotated relative to barrel 10 by the variable speed drive means 13, causes the stock or material to be moved forward along the rotor groove 16 to point 17. The rotor member 12 from point 17 to point
18 is provided with four start helical grooves 19 which connect with single start helical groove 16 and also cause the stock or material to be moved forward. The grooves 19 of the rotor member 12 which may have a helix angle of about 45″ to 780 with the centerline of the rotor are
similar and are spaced equally around the rotor member 12. These grooves 19, diminish uniformly in extrusion capacity from point 17 to point 18 or from full extrusion capacity, as an example, to one quarter extrusion capacity, as energized by relative rotation of the grooves 20 and land areas 22 of the surrounding barrel member 10 as shown in Figure 1.
It should be noted that extrusion capacity as referred to previously is not directly related to depth, area or volume of the grooves, but is the amount of stock caused to flow in the barrel grooves 20 by the relative rotating action of the barrel grooves 20 and land areas 22. Groove ratio of depth to width, slope of groove sides or bottom, location in barrel or rotor, easement of sharp groove corners are also significant and included in the term extrusion capacity.
The effect of this diminishing extrusion capacity is to transfer, as an example, three quarters of the stock flow of the rotor grooves 19 to the barrel grooves 20 at the rotor-to-barrel zone of each mixing stage.
Because of the groove design this stock approaches a uniform thin slab equal in width to the distance of point 17 to point
18. Each barrel groove 20 will receive stock or material from each rotor groove 19 in succession thereby effecting considerable blending.
There are six barrel grooves 20 shown in the preferred embodiment of Figures 1 and 9. In the length from point 17 to point 18, the grooves 20 communicate with the rotor grooves 19 and the helix of grooves 20 which preferably are from about 45″ to 60 with the centerline of the bore 11 is such to cause stock flow from point 17 to point 18 at the rotor-to-barrel zone. The relative extrusion capacity of barrel grooves 20, relative to the extrusion capacity of rotor grooves 19, of the exemplary apparatus is such that a difference of stock flow rate exists between the stock in barrel grooves 20 and that of the rotor grooves 19. The object of this is to allow some stock to pass through the mixing zone at an accelerated rate thereby creating a stock blending condition.
At point 18, the barrel grooves 20 now transporting as an example three quarters of the extruder throughput are designed to reorient that stock at the barrel-to-rotor zone. Orientation of stock is the direction of strain caused by shearing stress imposed by the apparatus A. The method of reorienting, shown in the preferred embodiment (Figure 9-15 inclusive) is to reduce or diminish the depth of the barrel grooves 20 and employ in the barrel-torotor zone a change in the helix angles of the barrel grooves 20. That is barrel grooves 20 between points 17 and 18 of the rotorto-barrel zone are at a maximum lead, say they advance a circumference distance per turn or have a helix angle of 45″ with the center line of the rotor. At point 18 through 23 of the barrel-to-rotor zone which in the depicted apparatus is about one fourth as long as the rotor-to-barrel zone, a minimum lead is provided. That is, barrel grooves 20, between points 18 and 23 of the barrel-to-rotor zone, are circumferential as possible without over restricting stock flow. Also between points 18 and 23 of the barrel-to-rotor zone the cross-sectional area of the barrel grooves 20 is reduced from maximum to zero, thus assisting in inducing stock flow from barrel grooves 20 back to rotor grooves 19 of the rotor member 12 in the barrel-to-rotor zone of the apparatus A.
The rotor grooves 19 at point 18 are enlarged from one quarter extrusion capacity to full extrusion capacity, providing an adequate channel for the reoriented stock flow which is being sheared from barrel grooves 20 in the barrel-to-rotor zone. Also at point 18, as an example, the one quarter of the stock not transferred to barrel grooves 20 in the rotor-to-barrel zone is received by the enlarged rotor groove 19 to be mixed with the re-oriented barrel stock in the barrel-to-rotor zone. The discharge of groove 19 (one quarter extrusion capacity groove) at point 18 can be provided with numerous groove dividers to promote flow control and facilitate mixing.
It is shown in Figure 1 as aligning with the center line of enlarged extrusion cap acity groove 19 in Figure 1 but can be offset, so that the rotor stock or material is placed in a preferred position to be transferred at the next mixing stage.
The bore 11 of barrel member 10 between points 23 and 17′ (next mixing stage), is smooth and without any groove configuration to act as a bearing guide for the rotor 12. The rotor grooves 19 are maintained at full extrusion capacity from point 18 forward to point 17′ of the next mixing stage.
Figure 1 shows an apparatus with two mixing stages as per above description although additional mixing stages may be provided or a single stage may be used.
The two mixing stages are followed by four start helical rotor grooves 24 which are continuous with grooves 19, but have a reduced extrusion capacity. The rotor grooves 24 contained in a smooth bore 11 of barrel 10, combine to act as a bearing for rotor 11. Also, it should be noted that the decreased lead and, therefore, reduced extrusion capacity is such that at full capacity operation, the stock flow is restrained generating pressure in the apparatus A. This pressure keeps the mixing stages full of stock and assures intensive shearing action.
Figure 2 is an enlarged view of the quadruple start rotor grooves 19 of the rotor member 12 for a complete mixing stage from point 23 of the first stage, to point 23′ of the second stage. Figure 3 is a surface development of one quadrant of the helical groove 19 of the rotor 12 showing the relation of the groove 19 and land areas 21 of rotor member 12.
Figures 4-8 inclusive illustrate progressive transverse sections of quadrant of the rotor member 12 showing approximate shape of the groove 19 to achieve extrusion capacity. Figure 9 is a sectional view of the preferred barrel member 10 showing six start helical barrel grooves 20 and land areas 22 from point 23 of the first mixing stage to point 23′ of the second mixing stage.
Figure 10 is a surface development of one helical sextent of the bore 11 of barrel member 10 showing the relation of groove 20 to land areas 22. More important,
Figure 10 displays the change of lead between 17 and 18, compared with lead between points 18 and 23′.
Figures 11-15 inclusive illustrate progressive transverse sections of sextant of the barrel member showing approximate shape of barrel grooves 20 for stock retention and transmission.
Figure 16 is a sectional view of another or alternative form of barrel groove 25 of barrel member 10. There are four start helical grooves 25 with land areas 26 in this alternative barrel member 10′. Grooves 25 accumulate the three quarters of the stock flow expelled from rotor between points 17 and 18 of the rotor-to-barrel zone, in a similar manner to grooves 20. The main difference between this and the the preferred embodiment of Figures 9-15 is that accumulated groove stock is induced radially outward from the groove 25 by means of a ring baffle 27. Baffle 27 retards the stock flow at the outer portion of the groove 25 allowing the lower portion and now faster portion, to turn the stock or material in a radial direction. The alternative structure does not employ a change of lead, but conceivably could be combined with the preferred embodiment of Figures 9-15 inclusive by having more or less lead. The grooves 25, as shown in Figures 16 and 17, are provided with a stock divider 28 at the center line of the groove 25 and between points 18 and 23′ of the barrel-to-rotor zone. This divider 28 assists in increasing rotor extrusion capacity and also establishes additional cleavage for an increase in stock shear. The grooves 25 in the barrelto-rotor zone shown in Figure 16, each have a lead as a continuation of the groove in the screw-to-barrel zone. Such groove has a positive lead.
It should be appreciated however that the grooves 25 in the barrel-to-rotor zone may have a «negative lead», or points in between a positive lead and negative lead.
Figure 23 is a partial sectional view of the assembled mixing stage, showing the normal relation between rotor member 12 and barrel member 10 with the bottom cut-away section indicating normal stock flow which is shown by six dashed lines 29.
It can be observed that the combined grooves of rotor member 12 and barrel member 10 provide an adequate channel through the extruder apparatus A. Points 17 and 18 of the rotor member 12 align with points 17 and 18 of the groove of the barrel member 10.
Figure 24 is a similar sectional view of the assembled mixing stage, but with the normal relation between rotor member 12 and barrel member 10 displaced longitudinally. Point 18 of the rotor member 12 now aligns with point 23 of the barrel member
10 threaded into nut 30 and brought to bear on the rotor extension 33, when rotor 12 is to be moved forward. For retracting the rotor member 12, the adjusting screw 32 is brought to bear against rotor 12, the adjusting screw 32 is brought to bear against rotor extension stop unit 34. Adjusting screw 32 is driven by spur gear 35, which is in turn driven by spur gear 36, and associated drive motor. Worm gear is engaged and disengaged via hinge 37 and air cylinder 38. This drive method allows longitudinal drive of the rotor 12, when drive means is at rest. A more elaborate adjustment means would utilise a differential drive, not shown, which would allow adjustments to be made during extruder operation.
The entire extruder apparatus A is mounted, by suitable bolts or machine screws, not shown, on the base 42 which, in turn, may be affixed by suitable studs, not shown, to the floor 44.
Figure 25 is a fragmentary elevational view of a rotor member 12′ like rotor member 12 but of modified groove design wherein the rotor grooves 19′ are reduced to zero extrusion capacity so that the maximum of stock being processed is transferred to the barrel grooves in the rotor to barrel zone.
In the rotor depicted in Figure 25 the grooves 19′ are at at a helix angle of about 600 to the axis of the rotor. Other suitable helix angles may be employed. The rotor grooves are also double in number at the barrel-to-rotor zone 18 to 23. This is accomplished by means of a stock divider 40 in each groove 19′ at the start thereof.
Blending considerations could be served by dividing only half of the grooves.
Figure 26 is a surface development of one quadrant of the helical groove 19′ of the rotor 12′ showing the relation of the groove 19′ and land areas 21′ of rotor member 12′.
Figures 27-32 inclusive illustrate progressive transverse sections of quadrant of the rotor member 12′ showing approximate shape of the groove 19′ to achieve extrusion capacity.
Figure 33 is a fragmentary sectional view on the lines 33-33 of Figure 26.
Figure 34 is a sectional view of a barrel member 10′ similar to the barrel member 10 showing six start helical barrel grooves 20′ of modified design and land areas 22′ from point 23 of the first mixing stage to point 23′ of the second mixing stage.
Figure 35 is a surface development of one helical sextant of the bore 11′ or barrel member 10′ showing the relation of groove 20′ to land areas 22′. Figure 35 displays the change of lead between points 17 and 18, compared with lead between points 18 and 23′.
Figures 36-40 inclusive illustrate progressive transverse sections of sextant of the barrel member showing approximate shape of barrel grooves 20′ for stock retention and transmission. The design depicted in
Figures 34-40 directs the flow pattern circumferentially so as to obtain longitudinal groove shearing of the stock as it passes from barrel to rotor. The helix angle of the groove 20′ is preferably from about 45″ to 60 with the center line of the bore 11′.
Stock flow at trailing edge of groove assists in slowing down the circumferential flow of stock and changing its direction to cross its direction to cross groove flow. The cam shaped circumferential groove propels the stock from the barrel toward the rotor, with adequate volume to develop extrusion pressure. Stock flow is circumferential and has predominance of shear lines axially with the rotor or at an acute angle to the direction of the groove. The circumferential shear, as the stock passes from barrel-to-rotor, now tends to elongate the shear lines into areas. This type of shearing is desirable to obtain microscopic dispersion, but is less effective for stock blending than the cross groove shearing.
Entrance to the circumferential groove can be fitted with a stock divider.
Figure 41 is a sectional view of another or alternate form of barrel groove 20″ of barrel member 10″. There are four start helical grooves 20″ with land areas 22′ in this alternative barrel member 10″.
Figure 42 is a surface development of one helical quadrant of the bore 11″ of barrel member 10″ showing the relation of groove 20″ to land areas 22″.
Figures 43-47 inclusive illustrate progressive sections of the barrel member 10″ showing approximate shape of barrel grooves 20″ for stock retention and transmission.
Figures 48 and 49 illustrate sections of th barrel grooves 20″ on the lines 48-48 and 49-49, respectively.
Figures 41, 42 display a change of lead between points 17 and 18, to zero lead between points 18 and 23′. The helix angle of the groove 20″ in the rotor-to-barrel zone is preferably from 45″ to 60 with the centerline of the bore 11″ and changes to zero in the barrel to rotor zone 18 to 23′, that, is, parallel with the centerline of the bore 11′.
Stock in an extruder groove tends to flow in the following pattern. The exposed portion of the stock in the groove is subjected to circumferential actuation or shear so that the resulting flow, toward the trailing edge of the groove, is essentially circumferential. The stock, displayed by this circumferential flow; then follows the path of least resistance, back to the leading edge of the extruder groove. This return path tends to be at right angles to the groove, but pressure flow, can result in a path that is nearly parallel to the axis of the rotor.
The design of Figures 41, 42 directs this flow pattern radially, so as to obtin cross groove shearing of the stock as it passes from barrel to rotor.
Stock flow at trailing edge of groove assists in slowing down the circumferential flow and changing its direction to cross groove flow. Restricted flow area increases flow velocity so that the resulting flow direction is nearly axial. The barrel to rotor groove is axial in direction and circular in profile so that the stock is turned at right angles and leaves the barrel in a radial direction. The stock divider 42, located at the center of the axial discharge groove.
stabilizes the radial flow of stock from the
barrel groove. Large land areas of this
design are effective in actuating flow in the
corresponding rotor grooves. This design
(cross shearing) is effective because the
stock in the barrel groove, due to the design
of the rotor to barrel stock flow, is in the
form of a long spiral, of wound sheet
stock, the width of which is the length of
the rotor to barrel zone and the pitch or
lead is a function of capacity.
While the foregoing apparatus has been
described primarily in connection with the
refining of materials such as curved or
rubber stocks, it is particularly to be under
stood that this apparatus, with or without
minor changes and adjustments may readily
be employed in processing other thermo
plastic and thermo-setting materials both
hot and cold feed.
WHAT I CLAIM IS:
1. An apparatus for the extruding and mixing of thermo-plastic and thermo-setting materials for both hot and cold feed, comprising an elongated generally cylindrical barrel member and an elongated rotor member disposed coaxially within said barrel member, means providing relative rotational movement between said rotor and barrel members for treating and axially advan- ing material to be processed along said members, said rotor and barrel members having a feed end, a discharge end, and a mixing stage including a rotor-to-barrel zone and a barrel-to-rotor zone interposed between said feed and discharge ends, the portions of said rotor and barrel members in said zones each being provided with at least one longitudinal helical groove, the grooves of said rotor and barrel members in said rotor-to-barrel zone being sized, with the extrusion capacity of the helical groove in said rotor member decreasing along the length of said rotor-to-barrel zone and with the extrusion capacity of the helical groove in said barrel member increasing along the length of said rotor-to-barrel zone, whereby said relative rotational movement between said rotor and barrel members causes material to flow outwardly from the rotor groove in said rotor-to-barrel zone into the barrel groove in said rotor-to-barrel zone, said barrel groove in said barrelto-rotor zone having a reduced depth to turn the received material away from the barrel groove and to direct the reoriented material towards the rotor groove for changing the axis of material shear as said material is advanced from said barrel member to said rotor member in said barrel-torotor zone from where the material flows toward said discharge end upon relative
rotational movement between said members.
2. An apparatus as claimed in claim 1, in which at least the down stream end of said barrel groove in said barrel-to-rotor zone has a flow divider therein.
3. An apparatus as claimed in claim 1, in which said barrel groove has a baffle therein in said barrel-to-rotor zone.
4. An apparatus as claimed in claim 3, in which said baffle is at the exterior of
said barrel.
5. An apparatus as claimed in claim 1,
in which the helix angle of the down stream end of said barrel groove in said barrel-to-rotor zones is different from the helix angle of said barrel groove in said rotor-to-barrel zone.
6. An apparatus as claimed in claim 1, including means for longitudinally displacing one of said members relative to said other member to vary the extrusion capacity of said rotor and barrel members.
7. An apparatus as claimed in claim 1, wherein said barrel-to-rotor zone has a length less than the length of said rotor-tobarrel zone.
8. An apparatus as claimed in claim 1, in which the flow of the material along the barrel groove in the barrel-to-rotor zone is turned at the down stream end of the groove at substantially right angles.
9. An apparatus as claimed in claim 1, wherein the barrel in said zones has multiple grooves.
10. An apparatus as claimed in claim 1, wherein the barrel groove in said rotorto-barrel zone has a lead sufficient for full capacity extrusion, and wherein the down stream end of said barrel groove in said barrel-to-rotor zone has a lead approximating zero.
11. An apparatus as claimed in claim 1, wherein there are a plurality of mixing stages in said rotor and barrel members, each of said stages including said rotor-tobarrel zone and said barrel-to-rotor zone.
**WARNING** end of DESC field may overlap start of CLMS **.

Claims (14)

**WARNING** start of CLMS field may overlap end of DESC **. of the extruder groove. This return path tends to be at right angles to the groove, but pressure flow, can result in a path that is nearly parallel to the axis of the rotor. The design of Figures 41, 42 directs this flow pattern radially, so as to obtin cross groove shearing of the stock as it passes from barrel to rotor. Stock flow at trailing edge of groove assists in slowing down the circumferential flow and changing its direction to cross groove flow. Restricted flow area increases flow velocity so that the resulting flow direction is nearly axial. The barrel to rotor groove is axial in direction and circular in profile so that the stock is turned at right angles and leaves the barrel in a radial direction. The stock divider 42, located at the center of the axial discharge groove. stabilizes the radial flow of stock from the barrel groove. Large land areas of this design are effective in actuating flow in the corresponding rotor grooves. This design (cross shearing) is effective because the stock in the barrel groove, due to the design of the rotor to barrel stock flow, is in the form of a long spiral, of wound sheet stock, the width of which is the length of the rotor to barrel zone and the pitch or lead is a function of capacity. While the foregoing apparatus has been described primarily in connection with the refining of materials such as curved or rubber stocks, it is particularly to be under stood that this apparatus, with or without minor changes and adjustments may readily be employed in processing other thermo plastic and thermo-setting materials both hot and cold feed. WHAT I CLAIM IS:

1. An apparatus for the extruding and mixing of thermo-plastic and thermo-setting materials for both hot and cold feed, comprising an elongated generally cylindrical barrel member and an elongated rotor member disposed coaxially within said barrel member, means providing relative rotational movement between said rotor and barrel members for treating and axially advan- ing material to be processed along said members, said rotor and barrel members having a feed end, a discharge end, and a mixing stage including a rotor-to-barrel zone and a barrel-to-rotor zone interposed between said feed and discharge ends, the portions of said rotor and barrel members in said zones each being provided with at least one longitudinal helical groove, the grooves of said rotor and barrel members in said rotor-to-barrel zone being sized, with the extrusion capacity of the helical groove in said rotor member decreasing along the length of said rotor-to-barrel zone and with the extrusion capacity of the helical groove in said barrel member increasing along the length of said rotor-to-barrel zone, whereby said relative rotational movement between said rotor and barrel members causes material to flow outwardly from the rotor groove in said rotor-to-barrel zone into the barrel groove in said rotor-to-barrel zone, said barrel groove in said barrelto-rotor zone having a reduced depth to turn the received material away from the barrel groove and to direct the reoriented material towards the rotor groove for changing the axis of material shear as said material is advanced from said barrel member to said rotor member in said barrel-torotor zone from where the material flows toward said discharge end upon relative
rotational movement between said members.

2. An apparatus as claimed in claim 1, in which at least the down stream end of said barrel groove in said barrel-to-rotor zone has a flow divider therein.

3. An apparatus as claimed in claim 1, in which said barrel groove has a baffle therein in said barrel-to-rotor zone.

4. An apparatus as claimed in claim 3, in which said baffle is at the exterior of
said barrel.

5. An apparatus as claimed in claim 1,
in which the helix angle of the down stream end of said barrel groove in said barrel-to-rotor zones is different from the helix angle of said barrel groove in said rotor-to-barrel zone.

6. An apparatus as claimed in claim 1, including means for longitudinally displacing one of said members relative to said other member to vary the extrusion capacity of said rotor and barrel members.

7. An apparatus as claimed in claim 1, wherein said barrel-to-rotor zone has a length less than the length of said rotor-tobarrel zone.

8. An apparatus as claimed in claim 1, in which the flow of the material along the barrel groove in the barrel-to-rotor zone is turned at the down stream end of the groove at substantially right angles.

9. An apparatus as claimed in claim 1, wherein the barrel in said zones has multiple grooves.

10. An apparatus as claimed in claim 1, wherein the barrel groove in said rotorto-barrel zone has a lead sufficient for full capacity extrusion, and wherein the down stream end of said barrel groove in said barrel-to-rotor zone has a lead approximating zero.

11. An apparatus as claimed in claim 1, wherein there are a plurality of mixing stages in said rotor and barrel members, each of said stages including said rotor-tobarrel zone and said barrel-to-rotor zone.

12. An apparatus as claimed in claim
1, in which the helix angles of said grooves in said rotor and barrel members are from 45″ to 780 with the centerline of the rotor member.

13. An apparatus as claimed in claim 1, wherein the barrel groove in said rotorto-barrel zone has a center line arranged at a maximum lead adequate for full capacity extrusion, and wherein the barrel groove in said barrel-to-rotor zone has a center line arranged at a minimum lead approximating zero.

14. An apparatus for the extruding and mixing of thermo-plastic and thermo-setting materials substantially as herein described with reference to the embodiments illustrated in the accompanying drawings.

GB21149/77A
1977-05-19
1977-05-19
Extrusion and mixing apparatus

Expired

GB1568888A
(en)

Priority Applications (1)

Application Number
Priority Date
Filing Date
Title

GB21149/77A

GB1568888A
(en)

1977-05-19
1977-05-19
Extrusion and mixing apparatus

Applications Claiming Priority (1)

Application Number
Priority Date
Filing Date
Title

GB21149/77A

GB1568888A
(en)

1977-05-19
1977-05-19
Extrusion and mixing apparatus

Publications (1)

Publication Number
Publication Date

GB1568888A
true

GB1568888A
(en)

1980-06-11

Family
ID=10158027
Family Applications (1)

Application Number
Title
Priority Date
Filing Date

GB21149/77A
Expired

GB1568888A
(en)

1977-05-19
1977-05-19
Extrusion and mixing apparatus

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Country
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(1)

GB1568888A
(en)

Cited By (7)

* Cited by examiner, † Cited by third party

Publication number
Priority date
Publication date
Assignee
Title

EP0219334A2
(en)

1985-10-14
1987-04-22
Kabushiki Kaisha Kobe Seiko Sho
Cavity transfer mixing extruder

GB2206838A
(en)

1987-07-16
1989-01-18
Werner & Pfleiderer
Extruder

GB2214126A
(en)

1987-12-30
1989-08-31
Toshiba Machine Co Ltd
Injection mould screws

EP0574172A1
(en)

1992-06-09
1993-12-15
Frenkel C-D Aktiengesellschaft
Mixing machinery of the transfermix type

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(en)

2009-11-04
2015-09-15
Koninklijke Philips N.V.
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2021-02-12
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US11031149B1
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1977

1977-05-19
GB
GB21149/77A
patent/GB1568888A/en
not_active
Expired

Cited By (11)

* Cited by examiner, † Cited by third party

Publication number
Priority date
Publication date
Assignee
Title

EP0219334A2
(en)

1985-10-14
1987-04-22
Kabushiki Kaisha Kobe Seiko Sho
Cavity transfer mixing extruder

EP0219334A3
(en)

1985-10-14
1988-03-16
Kobe Steel Ltd
Cavity transfer mixing extruder

GB2206838A
(en)

1987-07-16
1989-01-18
Werner & Pfleiderer
Extruder

GB2206838B
(en)

1987-07-16
1990-08-22
Werner & Pfleiderer
Extruder

GB2214126A
(en)

1987-12-30
1989-08-31
Toshiba Machine Co Ltd
Injection mould screws

GB2214126B
(en)

1987-12-30
1991-10-23
Toshiba Machine Co Ltd
Screws for use in vent type injection molding machines

EP0574172A1
(en)

1992-06-09
1993-12-15
Frenkel C-D Aktiengesellschaft
Mixing machinery of the transfermix type

US9132244B2
(en)

2009-11-04
2015-09-15
Koninklijke Philips N.V.
Medication delivery apparatus including a medication metering system

US11031149B1
(en)

2018-02-13
2021-06-08
AGI Engineering, Inc.
Nuclear abrasive slurry waste pump with backstop and macerator

CN112354387A
(en)

2020-09-17
2021-02-12
宁波领智机械科技有限公司
Slurry mixing machine

CN112354387B
(en)

2020-09-17
2023-04-07
宁波领智机械科技有限公司
Slurry mixing machine

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