Method and apparatus for forming tire components using a coextruded strip
12583166 ยท 2026-03-24
Assignee
Inventors
Cpc classification
B29C48/49
PERFORMING OPERATIONS; TRANSPORTING
B29K2021/00
PERFORMING OPERATIONS; TRANSPORTING
B29D30/52
PERFORMING OPERATIONS; TRANSPORTING
B29C48/387
PERFORMING OPERATIONS; TRANSPORTING
International classification
B29C48/49
PERFORMING OPERATIONS; TRANSPORTING
B29C48/305
PERFORMING OPERATIONS; TRANSPORTING
B29C48/375
PERFORMING OPERATIONS; TRANSPORTING
B29D30/52
PERFORMING OPERATIONS; TRANSPORTING
Abstract
One or more embodiments of the present invention provide an apparatus for applying a mixture of a first compound and a second compound, the apparatus comprising a first extruder for processing a first compound and a second extruder for processing a second compound, wherein the outlet from the first extruder is in fluid communication with a first channel of a housing, and the outlet from the second extruder is in fluid communication with a second channel of the housing, wherein a gear pump is positioned in each channel, wherein a nozzle is in fluid communication with an outlet of the first channel and an outlet of the second channel, and a coextruded continuous strip is produced. The ratio of the first compound to the second compound may be adjusted instantaneously.
Claims
1. A method for forming a coextruded strip of a first compound A and a second compound B for a tire component, the method comprising the steps of: extruding a first rubber compound A through a first extruder and a first gear pump and into a first passageway of a co-extrusion nozzle, extruding a second rubber compound B through a second extruder and a second gear pump and into a second passageway of the co-extrusion nozzle, wherein the co-extrusion nozzle includes an outlet, and the first and second passageways are joined together immediately upstream of the outlet of the co-extrusion nozzle, and wherein the first and second gear pumps are housed in a single housing.
2. The method of claim 1 wherein the co-extrusion nozzle has an insert which divides the nozzle into a separate first and second passageway.
3. The method of claim 2 wherein the insert has a distal end for positioning adjacent the outlet of the co-extrusion nozzle, wherein the distal end has an elongated flat portion.
4. The method of claim 1 wherein the ratio of the volume of rubber compound A to the volume of rubber compound B is varied by changing the ratio of the speed of the first gear pump to the second gear pump.
5. The method of claim 4 wherein the ratio of the first gear pump to the second gear pump may be varied during operation of the system.
6. The method of claim 2 wherein the insert is removable.
7. The method of claim 2 wherein the insert has a rectangular cross-sectional shape.
8. The method of claim 1 wherein the strip is formed in a continuous manner.
9. The method of claim 1 wherein the strip is applied in a continuous manner to a tire building machine to build a tire component.
Description
BRIEF DESCRIPTION OF THE DRAWINGS
(1) The invention will be described by way of example and with reference to the accompanying drawings in which:
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DETAILED DESCRIPTION OF THE INVENTION
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(16) The compound switching apparatus 10 is mounted upon a support frame 15. A translatable support bar 16 is mounted to the upper end of the support frame. Preferably, the compound switching apparatus 10 is mounted upon a translatable support bar 16, that can translate fore and aft in relation to a tire building machine 18.
(17) As shown in
(18) The first extruder inlet 32 receives a first compound A, examples of which are described in more detail, below. The first extruder 30 functions to warm up a first compound A to the temperature in the range of about 80 C. to about 150 C., preferably about 90 C. to about 120 C., and to masticate the rubber composition as needed. The output end 34 of the first extruder 30 is connected to an inlet end 43 of a first gear pump 42. Compound A is thus first extruded by the first extruder 30 and then pumped by the first gear pump 42 into a nozzle 80. The first gear pump 42 functions as a metering device and a pump and may have gears such as planetary gears, bevel gears or other gears.
(19) The second extruder inlet 62 receives a second compound B, examples of which are described in more detail, below. The second extruder 60 functions to warm up the second compound B to the temperature in the range of about 80 C. to about 150 C., preferably about 90 C. to about 120 C., and to masticate the rubber composition as needed. The output end 64 of the second extruder 60 is connected to an inlet end 45 of a second gear pump 44. Compound B is thus extruded by the second extruder 60 and then pumped by the second gear pump 44, which functions as a metering device and a pump and may have gears such as planetary gears, bevel gears or other gears.
(20) The first and second gear pumps 42,44 are preferably housed in a single housing 40 and are placed in close proximity to each other so that the outlet channels 46,48 of the first and second gear pumps are also in close proximity, as shown in
(21) A rotatable stitcher roller 90 is mounted adjacent the nozzle outlet 85 of the nozzle assembly 80. The stitcher roller 90 is pivotally mounted upon a support stand 92. An actuator 94 connected to the stitcher roller 90 pivots or rotates the support stand 92 about its end 93 when actuated.
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(23) New Material
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(25) The dual compound switching apparatus 10 with the coextrusion nozzle 100 produces a co-extruded strip 110 having a first layer 112 of a first compound A, and a second layer 114 of a second compound B. The first layer 112 and the second layer 114 are not mixed together, and are joined together at an interface in a coextrusion zone of the nozzle. The co-extrusion zone is located upstream of the nozzle die, where the compound A flow stream joins with the compound B flow stream.
(26) The dual compound switching apparatus 10 can be used to vary the volume ratio of compound A to compound B by varying the ratio of the speed of gear pump of compound A to the speed of gear pump of compound B. The dual compound switching apparatus 10 can adjust the speed ratios on the fly, and due to the small residence time of the coextrusion nozzle, the apparatus has a fast response to a change in the compound ratios. This is due to the low volume of the coextrusion zone. The dual compound switching apparatus 10 with the coextrusion nozzle may be used to coextrude a dual compound strip in a continuous manner onto a tire building drum. The ratio of compound A to compound B may be varied by changing the speed ratio of the gear pumps.
(27) Variations in the present inventions are possible in light of the description of it provided herein. While certain representative embodiments and details have been shown for the purpose of illustrating the subject invention, it will be apparent to those skilled in this art that various changes and modifications can be made therein without departing from the scope of the subject invention. It is, therefore, to be understood that changes can be made in the particular embodiments described which will be within the full intended scope of the invention as defined by the following appended claims.