U.S. patent application number 17/019233 was filed with the patent office on 2020-12-31 for extruder system for extruding cord reinforced extrudate.
The applicant listed for this patent is VMI HOLLAND B.V.. Invention is credited to Ronald Gerardus Maria De Bruijn, Emiel Hendricus De Jong, Pieter Cornelis Meijers.
Application Number | 20200406523 17/019233 |
Document ID | / |
Family ID | 1000005080260 |
Filed Date | 2020-12-31 |
United States Patent
Application |
20200406523 |
Kind Code |
A1 |
De Bruijn; Ronald Gerardus Maria ;
et al. |
December 31, 2020 |
EXTRUDER SYSTEM FOR EXTRUDING CORD REINFORCED EXTRUDATE
Abstract
The invention relates to an extruder system and a method for
extruding cord reinforced extrudate, wherein the extruder system
comprises an extruder head with a die for receiving extrusion
material and a cord guide for guiding cords in a common cord plane
in a cord direction into the die, wherein the extruder system
comprises a first extruder and a second extruder, wherein the
extruder head comprises a first flow channel and a second flow
channel, wherein the extruder system further comprises a first pump
and a second pump for receiving the extrusion material from the
first extruder and the second extruder and for directing said
extrusion material into the first flow channel and the second flow
channel.
Inventors: |
De Bruijn; Ronald Gerardus
Maria; (EPE, NL) ; De Jong; Emiel Hendricus;
(Epe, NL) ; Meijers; Pieter Cornelis; (Epe,
NL) |
|
Applicant: |
Name |
City |
State |
Country |
Type |
VMI HOLLAND B.V. |
Epe |
|
NL |
|
|
Family ID: |
1000005080260 |
Appl. No.: |
17/019233 |
Filed: |
September 12, 2020 |
Related U.S. Patent Documents
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Application
Number |
Filing Date |
Patent Number |
|
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15566149 |
Oct 12, 2017 |
10807294 |
|
|
PCT/NL2016/050235 |
Apr 5, 2016 |
|
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17019233 |
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Current U.S.
Class: |
1/1 |
Current CPC
Class: |
B29C 48/07 20190201;
B29K 2021/00 20130101; B29D 2030/381 20130101; B29D 30/38 20130101;
B29C 48/37 20190201; B29C 48/2883 20190201; B29C 48/156 20190201;
B33Y 30/00 20141201; B29L 2030/002 20130101; B29C 48/154 20190201;
B29C 48/49 20190201; B29C 48/21 20190201; B29C 48/34 20190201 |
International
Class: |
B29C 48/07 20060101
B29C048/07; B29C 48/49 20060101 B29C048/49; B29C 48/21 20060101
B29C048/21; B29C 48/34 20060101 B29C048/34; B29C 48/37 20060101
B29C048/37; B29C 48/154 20060101 B29C048/154; B29C 48/156 20060101
B29C048/156; B29C 48/285 20060101 B29C048/285; B29D 30/38 20060101
B29D030/38; B33Y 30/00 20060101 B33Y030/00 |
Foreign Application Data
Date |
Code |
Application Number |
Apr 14, 2015 |
NL |
2014634 |
Claims
1. An extruder system for extruding cord reinforced extrudate,
wherein the extruder system comprises: an extruder head with a die
for receiving extrusion material and a cord guide for guiding cords
side by side in a common cord plane in a cord direction into the
die so that, in use, the cords are embedded in the extrusion
material in the die; wherein the extruder system comprises a first
extruder and a second extruder external to the extruder head,
wherein the extruder head comprises a first flow channel that
debouches into the die from a first side of the cord plane and a
second flow channel that debouches into the die from a second side
of the cord plane opposite to the first side; wherein the extruder
system further comprises a first pump between the first extruder
and the first flow channel and a second pump between the second
extruder and the second flow channel, wherein the first pump and
the second pump are arranged for receiving the extrusion material
from the first extruder and the second extruder and for directing
said extrusion material into the first flow channel and the second
flow channel, respectively; wherein the extruder system is provided
with a first pressure sensor and a second pressure sensor at or
near the output side of the first pump and the second pump,
respectively, and upstream of or at the entrance of the first flow
channel and the second flow channel, respectively, for measuring
the pressures of the flows of extrusion material flowing from the
first pump and the second pump into the first flow channel and the
second flow channel, wherein the extruder system further comprises
a control unit that is operationally connected to the first pump
and the second pump and the first pressure sensor and the second
pressure sensor for controlling the speeds of the first pump and
the second pump based on the measurements from the first pressure
sensor and the second pressure sensor.
2. The extruder system according to claim 1, wherein the extruder
head has a feeding plane that extends orthogonal to the cord plane
and parallel to the cord direction, wherein the first extruder and
the second extruder are arranged for supplying the extrusion
material in a first supply direction and a second supply direction,
respectively, wherein the first supply direction and the second
supply direction are oblique with respect to the feeding plane,
wherein the first pump and the second pump are arranged for
receiving the extrusion material from the first extruder and the
second extruder in the first supply direction and the second supply
direction, respectively, and for directing said extrusion material
in or parallel to the feeding plane into the first flow channel and
the second flow channel, respectively.
3. The extruder system according to claim 2, wherein the first
supply direction and the second supply direction are each offset
with respect to the feeding plane over an angle of at least fifteen
degrees.
4. The extruder system according to claim 2, wherein the first
supply direction and the second supply direction are offset with
respect to the cord direction in the same direction.
5. The extruder system according to claim 1, wherein the extruder
head has a feeding plane that extends orthogonal to the cord plane
and parallel to the cord direction, wherein the first extruder and
the second extruder are arranged for supplying the extrusion
material in a first supply direction and a second supply direction,
respectively, wherein the first supply direction and the second
supply direction extend parallel to or in the feeding plane,
wherein the first pump and the second pump are arranged for
receiving the extrusion material from the first extruder and the
second extruder in the first supply direction and the second supply
direction, respectively, and for directing said extrusion material
in or parallel to the feeding plane into the first flow channel and
the second flow channel, respectively.
6. The extruder system according to claim 1, wherein the first
extruder is arranged for supplying a first compound of the
extrusion material into the die via the first flow channel and
wherein the second extruder is arranged for supplying a second
compound of the extrusion material into the die via the second flow
channel.
7. The extruder system according to claim 6, wherein the first
compound is chemically different from the second compound.
8. The extruder system according to claim 1, wherein the first pump
and the second pump are a first gear pump and a second gear pump,
respectively.
9. A method for extruding cord reinforced extrudate, with the use
of an extruder system, wherein the extruder system comprises an
extruder head and a first extruder and a second extruder external
to the extruder head, wherein the extruder head comprises a die for
receiving extrusion material, a cord guide for guiding cords side
by side in a common cord plane in a cord direction into the die, a
first flow channel that debouches into the die from a first side of
the cord plane and a second flow channel debouches into the die
from a second side of the cord plane opposite to the first side,
wherein the method comprises the steps of: guiding cords side by
side in the common cord plane in the cord direction into the
extruder head, supplying extrusion material from the first extruder
and the second extruder to the extruder head; providing a first
pump between the first extruder and the first flow channel and a
second pump between the second extruder and the second flow
channel, wherein the first pump and the second pump receive the
extrusion material from the first extruder and the second extruder
and direct said extrusion material into the first flow channel and
the second flow channel, respectively; measuring the pressure of
the first compound at or near the output side of the first pump and
upstream of or at the entrance to the first flow channel; measuring
the pressure of the second compound at or near the output side of
the second pump and upstream of or at the entrance to the second
flow channel; and controlling the speeds of the first pump and the
second pump based on the measurements of the pressures of the first
compound and the second compound.
10. The method according to claim 9, wherein the extruder head has
a feeding plane that extends orthogonal to the cord plane and
parallel to the cord direction, wherein the extrusion material is
supplied from the first extruder and the second extruder to the
extruder head in a first supply direction and a second supply
direction which are oblique to the feeding plane, wherein the first
pump and the second pump receive the extrusion material from the
first extruder and the second extruder in the first supply
direction and the second supply direction, respectively, and direct
said extrusion material in or parallel to the feeding plane into
the first flow channel and the second flow channel,
respectively.
11. The method according to claim 9, wherein the extruder head has
a feeding plane that extends orthogonal to the cord plane and
parallel to the cord direction, wherein the extrusion material is
supplied from the first extruder and the second extruder to the
extruder head in a first supply direction and a second supply
direction which extend parallel to or in the feeding plane, wherein
the first pump and the second pump receive the extrusion material
from the first extruder and the second extruder in the first supply
direction and the second supply direction, respectively, and direct
said extrusion material in or parallel to the feeding plane into
the first flow channel and the second flow channel,
respectively.
12. The method according to claim 9, wherein the first extruder
supplies a first compound of the extrusion material and wherein the
second extruder supplies a second compound of the extrusion
material.
13. The method according to claim 12, wherein the first compound is
chemically different from the second compound.
14. The method according to claim 9, wherein the compounds are
identical, wherein the speeds of the first pump and the second pump
are controlled to supply the first compound and the second compound
into the first flow channel and the second flow channel at
substantially the same pressure.
15. The method according to claim 9, wherein the first compound and
the second compound are different, wherein the speeds of the first
pump and the second pump are controlled based on data about the
ratios between the pressure and the flow rate for each of the first
compound and the second compound, such that the first compound and
the second compound at different pressures flow at the same flow
rate through or out of the die.
Description
CROSS REFERENCE TO RELATED APPLICATION
[0001] This application is a divisional of co-pending U.S. patent
application Ser. No. 15/566,149, filed Oct. 12, 2017, the contents
of which is incorporated herein.
BACKGROUND
[0002] The invention relates to an extruder system and a method for
extruding cord reinforced extrudate, in particular cord reinforced
tire components.
[0003] Known extruder systems for extruding cord reinforced tire
components comprise so-called `cross head` type extruder heads in
which the extrusion material is supplied laterally with respect to
the direction in which the cords are fed into the extruder head. EP
1 145 835 A2 discloses such an exemplary extruder system. The known
extruder heads are provided with flow channels that deflect the
flow of extrusion material from the lateral supply direction
towards the cord direction. The flow channels, although optimized
for uniform distribution of the extrusion material, are known to
cause non-uniformity in the extrudate that leaves the extruder
head. In particular, due to asymmetries in the flow channels, the
parts of the flow channels that are most distal in the supply
direction, will typically receive considerably less extrusion
material, resulting in uneven flow rates, non-uniform thickness
and/or density across the width of the extrudate.
[0004] It is an object of the present invention to provide an
extruder system and a method for extruding cord reinforced
extrudate, wherein uniformity of the extrudate can be improved.
SUMMARY OF THE INVENTION
[0005] According to a first aspect, the invention provides an
extruder system for extruding cord reinforced extrudate, in
particular cord reinforced tire components, wherein the extruder
system comprises an extruder head with a die for receiving
extrusion material and a cord guide for guiding cords side by side
in a common cord plane in a cord direction into the die so that, in
use, the cords are embedded in the extrusion material in the die,
wherein the extruder system comprises a first extruder and a second
extruder external to the extruder head, wherein the extruder head
comprises a first flow channel that debouches into the die from a
first side of the cord plane and a second flow channel that
debouches into the die from a second side of the cord plane
opposite to the first side, wherein the extruder system further
comprises a first pump between the first extruder and the first
flow channel and a second pump between the second extruder and the
second flow channel, wherein the first pump and the second pump are
arranged for receiving the extrusion material from the first
extruder and the second extruder and for directing said extrusion
material into the first flow channel and the second flow channel,
respectively.
[0006] The first pump and the second pump can uniformly distribute
the extrusion material into the flow channels, regardless of the
orientation of the extruders and/or irrespective of the direction
in which the extrusion material is supplied to the pumps by the
respective extruders. The extrusion material can thus be
distributed uniformly through the flow channels towards the die,
thereby improving the uniformity of the extrudate that ultimately
leaves the die.
[0007] The `cross head` type extruder of EP 1 145 835 A2 does not
disclose the aforementioned pumps. EP 0 492 425 A1 discloses a
compact precision extrusion system that is able to provide accurate
extrudate gauges during changes of stock viscosity of rubber feed
strips by use of a gear pump and a control system which
continuously measures the various temperatures and pressures at the
different positions of the system, which measurements are fed to a
computer control which induces changes in the pump and feed speed.
In EP 1 145 835 A2, the extruders are positioned laterally with
respect to the feeding plane. The pumps according to the invention
are used merely to uniformly distribute the flow of extrusion
material into the flow channels, irrespective of the direction in
which the extrusion material is supplied to the pumps by the
respective extruders. In EP 0 492 425 A1, the arrangement of the
extruder, the gear pump, the extruder head and the extruded strip
is completely coaxial. Therefore, there is no teaching nor a
suggestion in EP 0 492 425 A1 that the known gear pump arrangement
can be used in EP 1 145 835 A2 for the claimed purpose.
[0008] In one embodiment the extruder head has a feeding plane that
extends orthogonal to the cord plane and parallel to the cord
direction, wherein the first extruder and the second extruder are
arranged for supplying the extrusion material in a first supply
direction and a second supply direction, respectively, wherein the
first supply direction and the second supply direction are oblique
with respect to the feeding plane, wherein the first pump and the
second pump are arranged for receiving the extrusion material from
the first extruder and the second extruder in the first supply
direction and the second supply direction, respectively, and for
directing said extrusion material in or parallel to the feeding
plane into the first flow channel and the second flow channel,
respectively. The oblique positioned extruders can at least partly
be spaced apart from or placed out of line with respect to the cord
direction, thereby preventing that the extruders interfere with or
hinder the feeding of the cords from a creelroom to the extruder
head.
[0009] In a preferred embodiment thereof, the first supply
direction and the second supply direction are each offset with
respect to the feeding plane over an angle of at least fifteen
degrees, preferably at least twenty degrees and most preferably at
least thirty degrees. Such angles provide sufficient spacing of the
extruders with respect to the cords to allow the cords to be easily
fed in the cord direction into the extruder head.
[0010] In a practical embodiment thereof the first supply direction
and a second supply direction are offset with respect to the cord
direction in the same direction. As such, the extruder system can
be designed to be more compact and/or more practical, in particular
as both extruders can be fed from the same side of the feeding
plane.
[0011] In an alternative embodiment the extruder head has a feeding
plane that extends orthogonal to the cord plane and parallel to the
cord direction, wherein the first extruder and the second extruder
are arranged for supplying the extrusion material in a first supply
direction and a second supply direction, respectively, wherein the
first supply direction and the second supply direction extend
parallel to or in the feeding plane, wherein the first pump and the
second pump are arranged for receiving the extrusion material from
the first extruder and the second extruder in the first supply
direction and the second supply direction, respectively, and for
directing said extrusion material in or parallel to the feeding
plane into the first flow channel and the second flow channel,
respectively. The supply directions parallel to or in the feeding
plane can eliminate the drawback of the uneven distribution of
`cross-head` configurations. To allow access to the cord guide, the
cord guide may be arranged on a carriage that is displaceable along
a rail in or parallel to the cord plane, away from the die.
[0012] Optionally, the first supply direction and the second supply
direction extend obliquely with respect to the cord plane. The
oblique angle can provide access to the part of the cord plane that
extends between the extruders. Regardless of the angle of the
supply directions with respect to the cord plane, the gear pumps
can generate a uniform pressure in the extrudate that goes into the
flow channel.
[0013] In an embodiment the first pump and the second pump are
arranged for directing the extrusion material symmetrically and/or
uniformly distributed with respect to the feeding plane into the
first flow channel and the second flow channel, respectively. The
pumps can thus improve the distribution of the extrusion material
going into the extruder head.
[0014] In an embodiment the first flow channel and the second flow
channel are arranged for receiving the extrusion material from the
first pump and the second pump in, parallel or symmetrical to the
feeding plane. The flow channels can thus be adapted to optimally
receive the extrusion material from the pumps, to facilitate the
in-line, parallel or symmetrical supply of extrusion material.
[0015] In an embodiment the feeding plane extends in-line with the
cord direction. The extrusion material can thus be fed in-line with
the cord direction into the extruder head, contrary to the lateral
direction in which the extrusion material is fed into the known
extruder heads according to the prior art.
[0016] In an embodiment the first flow channel and the second flow
channel are symmetrical or substantially symmetrical to the feeding
plane. Preferably the first flow channel and the second flow
channel are symmetrical or substantially symmetrical to the feeding
plane within the entire extruder head. The symmetry of the flow
channels within the extruder head can improve the symmetry and/or
uniformity of the flow of extrusion material in the extruder
head.
[0017] In an embodiment the extruder head has a plurality of
externally facing surfaces, wherein the first flow channel and the
second flow channel are arranged in fluid communication with the
material source via an externally facing surface of the extruder
head that intersects with the feeding plane. The externally facing
surfaces that intersect with the feeding plane, not being the
laterally facing side surfaces of the extruder head, can be used to
symmetrically connect the flow channels to the material source in
accordance with the invention.
[0018] In an embodiment the die is provided with a die opening for
shaping the extrusion material, wherein the die opening has a width
parallel to the cord plane, wherein the feeding plane is at or near
the center of the width of the die opening. The extrusion material
can thus be fed into the extruder head in a centered position with
respect to the width of the die opening, thereby further improving
the uniformity of the extrudate when it leaves the die.
[0019] In an embodiment the first extruder is arranged for
supplying a first compound of the extrusion material into the die
via the first flow channel and wherein the second extruder is
arranged for supplying a second compound of the extrusion material
into the die via the second flow channel. By using two extruders,
the two compounds of the extrusion material can be supplied to the
two flow channels individually or in separate flows.
[0020] In an embodiment the first extruder is arranged for
receiving a first compound that is chemically different from the
second compound that is received in the second extruder. Thus, it
becomes possible to obtain an extrudate with different material
characteristics for the part of the extrudate above the cords and
the part of the extrudate below the cords.
[0021] In an embodiment the first extruder and the second extruder
are provided with a first heater for heating the first compound and
a second heater for heating the second compound, respectively,
wherein the first heater and the second heater are individually
controllable. Preferably, the extruder system comprises a first
control unit that is operationally connected to the first heater
and the second heater, wherein the first control unit is arranged
for controlling the first heater to a different temperature than
the second heater. The difference in temperature can influence the
viscosities and thus the flow rates of the respective compounds in
the extruder head. The difference in temperature can be used to
control swelling of the extrudate after it leaves the die, for
example for controlling the relative position of the cords with
respect to the extrudate.
[0022] In an embodiment the extruder system is provided with a
first pressure sensor and a second pressure sensor at or near the
output side of the first pump and the second pump, respectively,
and upstream of or at the entrance of the first flow channel and
the second flow channel, respectively, for measuring the pressures
of the flows of extrusion material flowing from the pumps into the
flow channels, wherein the extruder system further comprises a
second control unit that is operationally connected to the pumps
and the pressure sensors for controlling the speeds of the pumps
based on the measurements from the pressure sensors. The pressure
in the extrusion material can thus be controlled for each outflow
from the respective pumps, to further improve the uniformity of the
extrusion material in the extruder head. In particular, the
pressures can be set to the same level when the compounds are
identical, or to different pressures, based on given data about the
ratios between the pressure and the flow rates for different
compounds. Thus, one can control the speeds of the pumps to control
the pressures and/or flow rates of the extrusion material in the
extruder head.
[0023] In an embodiment the first pump and the second pump are a
first gear pump and a second gear pump, respectively. Gear pumps
can provide a flow of extrusion material with constant flow rate
and/or pressure.
[0024] In a practical embodiment the cord plane is horizontal or
substantially horizontal, wherein the first flow channel debouches
into the die from below the cord plane and wherein the second flow
channel debouches into the die from above the cord plane.
[0025] In an embodiment the plurality of externally facing surfaces
comprises at least one surface of the group comprising a rear
surface facing upstream in the cord direction, a top surface facing
upwards away from the cord plane and a bottom surface facing
downwards away from the cord plane, wherein the first flow channel
and the second flow channel are arranged in fluid communication
with the material source via a the rear surface, the top surface
and or the bottom surface. These externally facing surfaces, not
being the laterally facing side surfaces of the extruder head, can
be used to symmetrically connect the flow channels to the material
source in accordance with the invention.
[0026] According to a second aspect, the invention provides a
method for extruding cord reinforced extrudate, in particular cord
reinforced tire components, with the use of an extruder system,
wherein the extruder system comprises an extruder head and a first
extruder and a second extruder external to the extruder head,
wherein the extruder head comprises a die for receiving extrusion
material, a cord guide for guiding cords side by side in a common
cord plane in a cord direction into the die, a first flow channel
that debouches into the die from a first side of the cord plane and
a second flow channel debouches into the die from a second side of
the cord plane opposite to the first side, wherein the method
comprises the steps of guiding cords side by side in the common
cord plane in the cord direction into the extruder head, supplying
extrusion material from the first extruder and the second extruder
to the extruder head, wherein the method further comprises the step
of providing a first pump between the first extruder and the first
flow channel and a second pump between the second extruder and the
second flow channel, wherein the first pump and the second pump
receive the extrusion material from the first extruder and the
second extruder and direct said extrusion material into the first
flow channel and the second flow channel, respectively.
[0027] The first pump and the second pump can thus uniformly
distribute the extrusion material into the flow channels,
regardless of the orientation of the extruders and/or irrespective
of the direction in which the extrusion material is supplied to the
pumps by the respective extruders. The extrusion material can thus
be distributed uniformly through the flow channels towards the die,
thereby improving the uniformity of the extrudate that ultimately
leaves the die.
[0028] In an embodiment of the method, the extruder head has a
feeding plane that extends orthogonal to the cord plane and
parallel to the cord direction, wherein the extrusion material is
supplied from the first extruder and the second extruder to the
extruder head in a first supply direction and a second supply
direction which are oblique to the feeding plane, wherein the first
pump and the second pump receive the extrusion material from the
first extruder and the second extruder in the first supply
direction and the second supply direction, respectively, and direct
said extrusion material in or parallel to the feeding plane into
the first flow channel and the second flow channel, respectively.
The first pump and the second pump can thus uniformly distribute
the extrusion material into the flow channels in or parallel to the
feeding plane, regardless of the oblique orientation of the
extruders with respect to said feeding plane and/or irrespective of
the direction in which the extrusion material is supplied to the
pumps by the respective extruders.
[0029] In an alternative embodiment of the method, the extruder
head has a feeding plane that extends orthogonal to the cord plane
and parallel to the cord direction, wherein the extrusion material
is supplied from the first extruder and the second extruder to the
extruder head in a first supply direction and a second supply
direction which extend parallel to or in the feeding plane, wherein
the first pump and the second pump receive the extrusion material
from the first extruder and the second extruder in the first supply
direction and the second supply direction, respectively, and direct
said extrusion material in or parallel to the feeding plane into
the first flow channel and the second flow channel, respectively.
The supply directions parallel to or in the feeding plane can
eliminate the drawback of the uneven distribution of `cross-head`
configurations. To allow access to the cord guide, the cord guide
may be arranged on a carriage that is displaceable along a rail in
or parallel to the cord plane, away from the die.
[0030] Optionally, the first supply direction and the second supply
direction extend obliquely with respect to the cord plane. The
oblique angle can provide access to the part of the cord plane that
extends between the extruders. Regardless of the angle of the
supply directions with respect to the cord plane, the gear pumps
can generate a uniform pressure in the extrudate that goes into the
flow channel.
[0031] In an embodiment the extrusion material is made to flow
symmetrical or substantially symmetrical to the feeding plane
within the extruder head. Preferably, the entire flow of extrusion
material within the extruder head is symmetrical or substantially
symmetrical to the feeding plane. The symmetry of the flow channels
within the extruder head can improve the symmetry and/or uniformity
of the flow of extrusion material in the extruder head.
[0032] In an embodiment the first extruder supplies a first
compound of the extrusion material and wherein the second extruder
supplies a second compound of the extrusion material. By using two
extruders, the two compounds of the extrusion material can be
supplied to the two flow channels individually or in separate
flows.
[0033] In an embodiment the first compound is chemically different
from the second compound. Thus, it becomes possible to obtain an
extrudate with different material characteristics for the part of
the extrudate above the cords and the part of the extrudate below
the cords.
[0034] In an embodiment the first compound is heated to a different
temperature than the second compound. The difference in temperature
can influence the viscosities and thus the flow rates of the
respective compounds in the extruder head. The difference in
temperature can be used to control swelling of the extrudate after
it leaves the die, for example for controlling the relative
position of the cords with respect to the extrudate.
[0035] In an embodiment the method further comprises the steps of
measuring the pressure of the first compound at or near the output
side of the first pump and upstream of or at the entrance to the
first flow channel, measuring the pressure of the second compound
at or near the output side of the second pump and upstream of or at
the entrance to the second flow channel, controlling the speeds of
the pumps based on the measurements of the pressures of the
compounds. The pressure in the extrusion material can thus be
controlled for each outflow from the respective pumps, to further
improve the uniformity of the extrusion material in the extruder
head.
[0036] In an embodiment the compounds are identical or
substantially identical, wherein the speeds of the pumps are
controlled to supply the compounds into the flow channels at
substantially the same pressure. The pressures can be set to the
same level when the compounds are identical, so that the flow of
the compounds through the die has the same flow rate for each
compound, thereby improving the uniformity of the extrudate.
[0037] In an embodiment the compounds are different, wherein the
speeds of the pumps are controlled based on data about the ratios
between the pressure and the flow rate for each of the different
compounds, such that the different compounds at different pressures
flow at the same or substantially the same flow rate out through
and/or out of the die. Thus, one can correct for the different
viscosities of the compounds to ultimately arrive at the same flow
rate for each of the compounds in the die.
[0038] The various aspects and features described and shown in the
specification can be applied, individually, wherever possible.
These individual aspects, in particular the aspects and features
described in the attached dependent claims, can be made subject of
divisional patent applications.
BRIEF DESCRIPTION OF THE DRAWINGS
[0039] The invention will be elucidated on the basis of an
exemplary embodiment shown in the attached schematic drawings, in
which:
[0040] FIG. 1 shows a top view of an extruder system according to a
first embodiment of the invention;
[0041] FIG. 2 shows a side view of the extruder system according to
FIG. 1;
[0042] FIG. 3 shows a side view of an alternative extruder system
according to a second embodiment of the invention;
[0043] FIG. 4 shows a side view of a further alternative extruder
system according to a third embodiment of the invention; and
[0044] FIGS. 5 and 6 show a top view and a side view, respectively,
of a further alternative extruder system according to a fourth
embodiment of the invention.
DETAILED DESCRIPTION OF THE INVENTION
[0045] FIGS. 1 and 2 show an extruder system 1 according to a first
embodiment of the invention. The extruder system 1 is arranged for
extruding an extrudate 9, in particular a tire component, that has
been reinforced with cords 8, typically steel or textile cords.
Examples of cord reinforced tire components are breaker plies, body
plies, cap strips and chafers.
[0046] The extruder system 1 comprises an extruder head 2 with a
die 3 for extruding the extrudate 9 and a cord guide 4 for guiding
the cords 8 into the die 3 so that the cords 8 in use are embedded
into the extrudate 9. The extruder system 1 further comprises a
material supply or material source 5 for supplying liquefied
extrusion material 90, e.g. a viscous rubber compound 91, 92, to
the extruder head 2. The material source 5 is located external to
or outside of the extruder head 2. In this exemplary embodiment,
the extruder system 1 is further provided with a pump section 6
between the extruder head 2 and the material source 5 for evenly or
uniformly distributing the extrusion material 90 from the material
source 5 into the extruder head 2.
[0047] As shown in FIG. 2, the extruder head 2 is provided with a
first half 21 and a second half 22 which are mated together to form
the die 3 and the cord guide 4. The cord guide 4 is provided with a
plurality of guide channels (not shown and known per se) for
receiving the cords 8 in a cord direction A from a creelroom (not
shown and known per se) and for guiding the cords 8 in a side by
side orientation in a common cord plane B into the die 3. In this
exemplary embodiment, the cord plane B extends horizontally or
substantially horizontally. As best seen in FIG. 1, the cords 8 are
extending mutually parallel into, through and out of the extruder
head 2 in the cord direction A.
[0048] As shown in FIGS. 1 and 2, the die 3 is provided with a die
opening 31 through which the extrusion material 90 is forced into
the shape of the extrudate 9. The die opening 31 has a width W
parallel to the cord plane B that substantially corresponds to the
desired width W of the extrudate 9. In this exemplary embodiment,
the die 3 is a separate piece of tooling that is mounted directly
downstream of the cord guide 4 and that can be interchanged by
other tooling when extrudates with different cross sections are to
be produced.
[0049] As shown in FIGS. 1 and 2, the extruder head 2 has a
plurality of externally facing surfaces. In particular, in this
exemplary embodiment, the extruder head is shaped like a block,
comprising a rear surface 23 facing upstream or opposite to the
cord direction A, a top surface 24 facing upwards and away from the
cord plane B and a bottom surface 25 facing downwards and away from
the cord plane B, and two sides 26, 27 that are facing laterally
away from the cord direction A in a direction parallel to the cord
plane B. The extruder head 2 is provided with a first flow channel
71 extending in the first half 21 of the extruder head 2 for
connecting the material source 5 in fluid communication to the die
3. The first flow channel 71 connects to the externally located
material source 5 via one of the externally facing surfaces 23, 24
at the first half of the extruder head 2, not being one of the two
laterally facing sides 26, 27. In this example, the first flow
channel 71 connects to the externally located material source 5 via
the rear surface 23. The first flow channel 71 merges or debouches
into the die 3 from a first side of the cord plane B.
[0050] As best seen in FIG. 2, the extruder head 2 comprises a
second flow channel 72 similar or identical to the first flow
channel 71. In this example, the second flow channel 72 is mirror
symmetrical to the first flow channel 71 with respect to the cord
plane B. The second flow channel 72 extends in the second half 22
of the extruder head 2 for connecting the material source 5 in
fluid communication to the die 3. Like the first flow channel 71,
the second flow channel 72 connects to the externally located
material source 5 via one of the externally facing surfaces 23, 25
at the second half 22 of the extruder head 2, not being one of the
two laterally facing sides 26, 27. In this example, the second flow
channel 72 also connects to the externally located material source
5 via the rear surface 23, yet on the opposite side with respect to
the cord plane B of the connection of the first flow channel 71 to
the material source 5. The second flow channel 72 merges or
debouches into the die 3 from a second side of the cord plane B,
opposite to the first side.
[0051] Later in the description, two alternative embodiments of the
invention will be described in more detail, in which the first flow
channel 71 and the second flow channel 72 connect to the externally
located material source 5 via the top surface 24 and the bottom
surface 25, respectively.
[0052] As shown in FIG. 1, the first flow channel 71 is arranged
for receiving the extrusion material 90 from the material source 5
in a first inflow direction F1 extending in an in-line feeding
plane P with respect to the cord direction A. The same applies to
the second flow channel 72 which, although not shown in FIG. 1, is
arranged for receiving the extrusion material 90 from the material
source 5 in a second inflow direction F2 (see FIG. 2) extending in
the same in-line feeding plane P. The feeding plane P extends
perpendicular or orthogonal to the cord plane B and in-line or
parallel to the cord direction A. In the case where the cord plane
B extends horizontal or substantially horizontal, the feeding plane
P extends vertical or substantially vertical. In this example, the
feeding plane P is arranged at the center of the width W of the die
opening 31. The feeding plane P intersects with the rear surface
23, the top surface 24 and the bottom surface 25 of the extruder
head 2.
[0053] The first flow channel 71 and the second flow channel 72 are
shaped to be symmetrical or substantially symmetrical to the
feeding plane P, preferably within the entire extruder head 2.
Thus, after receiving the extrusion material 90 in the respective
inflow directions F1, F2, the flow channels 71, 72 are arranged for
guiding the flow of the extrusion material 90 within the extruder
head 2 in a symmetrical or substantially symmetrical fashion with
respect to the feeding plane P.
[0054] In particular, as shown in FIG. 1, the first flow channel 71
is provided with a diverging section 73 that symmetrically diverges
with respect to the feeding plane P in the cord direction A to
evenly or uniformly distribute the extrusion material 90 towards
the die opening 31 across the entire width W of the die opening 31.
The same symmetrical divergence is applied to the second flow
channel 72. To further improve the evenness or uniformity of the
distribution in the flow channels 71, 72, the flow channels 71, 72
may be provided with a distribution insert 74 in the diverging
section 73. The distribution insert 74 in a manner known per se
forces or splits the inflow of extrusion material 90 into two
separately diverging flows D1, D2 towards the die opening 31.
Different inserts 74 may be provided for each of the flow channels
71, 72. The resulting outflow U of extrusion material 90 is
substantially uniform or even in viscosity, flow rate and/or
density across the width W of the die opening 31.
[0055] As shown in FIG. 2, the material source 5 comprises a first
extruder 51 that is operationally connected to or arranged in fluid
communication with the first flow channel 71 and a second extruder
52 that is operationally connected to or arranged in fluid
communication with the second flow channel 72. The first extruder
51 comprises a barrel 53 that is arranged for receiving a first
compound 91 of the extrusion material 90 and for supplying said
first compound 91 to the first flow channel 71 in a first supply
direction S1, parallel to the direction of the barrel 53 of the
first extruder 51. The second extruder 52 also comprises a barrel
54 that is arranged for receiving a second compound 92 of the
extrusion material 90 and for supplying said second compound 92 to
the second flow channel 72 in a second supply direction S2,
parallel to the direction of the barrel 54 of the second extruder
52. In this exemplary embodiment, the first compound 91 is the same
as the second compound 92. Alternatively, the first compound 91 may
be materially or chemically different from the second compound 92
to arrive at different material characteristics for the part of the
extrudate 9 above the cords 8 and the part of the extrudate 9 below
the cords 8.
[0056] The material source 5 according to the invention further
comprises a first heater 55 that is thermally coupled to the first
extruder 51 for heating the first compound 91 and a second heater
56 that is thermally coupled to the second extruder 52 for heating
the second compound 92. Optionally, the extruder system 1 is
provided with a first control unit 57 that is operationally
connected to the first heater 55 and the second heater 56 for
individually controlling the heaters 55, 56. This feature can be
used to control the temperature of the first compound 91 to a
different temperature than the temperature of the second compound
92, which influences the viscosities and thus the flow rates of the
respective compounds 91, 92 in the extruder head 2. The difference
in temperature can be used to control swelling of the extrudate 9
after it leaves the die 3, for example for controlling the relative
position of the cords 8 with respect to the extrudate 9.
[0057] As shown in the side view of FIG. 2, the first extruder 51
and the second extruder 52 are positioned with their respective
supply directions S1, S2 extending parallel or substantially
parallel to the cord plane B. In the top view of FIG. 1, it is
shown that the first extruder 51 (and the second extruder 52 hidden
underneath the first extruder 51), are offset or placed at an
oblique angle with respect to the cord direction A and/or the
feeding plane P. In particular, the extruders 51, 52 are position
such that their respective supply directions S1, S2 are offset with
respect to the feeding plane P over an angle H of at least fifteen
degrees, preferably at least twenty degrees and most preferably at
least thirty degrees, with a maximum of ninety degrees. Thus, the
barrels 53, 54 of the extruders 51, 52 are laterally offset with
respect to the cord direction A in a direction parallel to the cord
plane B and do not interfere with or hinder the feeding of the
cords 8 from the creelroom (not shown) to the extruder head 2 in
the cord direction A.
[0058] In this example, the extruders 51, 52 are offset over the
same angle H and in the same direction with respect to the feeding
plane P. Alternatively, the extruders 51, 52 may be offset over
different angles and/or in opposite directions with respect to the
feeding plane P. In all of the aforementioned variants, the
compounds 91, 92, in their respective supply directions S1, S2, are
supplied asymmetrically with respect to the feeding plane P.
[0059] As shown in FIG. 2, the pump section 6 is provided with a
first gear pump 61 that is located in fluid communication between
the first extruder 51 and the first flow channel 71 and a second
gear pump 62 that is located in fluid communication between the
second extruder 52 and the second flow channel 72. The first gear
pump 61 and the second gear pump 62 are arranged in fluid
communication with the downstream ends of the first extruder 51 and
the second extruder 52, respectively, for receiving the first
compound 91 in the first supply direction S1 and the second
compound in the second supply direction S2, respectively. The first
gear pump 61 and the second gear pump 62 have a first output
direction G1 and a second output direction G2, respectively, which
are different from the first supply direction S1 and the second
supply direction S2. In particular, the gear pumps 61, 62 are
arranged for deflecting or directing the compounds 91, 92 from
their respective supply direction S1, S2 to the respective output
directions G1, G2, wherein the output directions G1, G2 are in line
with, parallel to or symmetrical with respect to feeding plane P.
As such, the compounds 91, 92 that are output from the first gear
pump 61 and the second gear pump in the respective output
directions G1, G2 can be symmetrically received with respect to the
feeding plane P into the first flow channel 71 and the second flow
channel 72, respectively, symmetrically to the feeding plane P.
[0060] The gear pumps 61, 62 are particularly useful for evenly or
uniformly metering, dosing, pressurizing and/or distributing the
flow of extrusion material 90 in or symmetrical to the feeding
plane P into the first flow channel 71 and the second flow channel
72, respectively, to improve the evenness or uniformity of the
extrudate 9.
[0061] As shown in FIG. 2, the extruder system 1 is provided with a
first pressure sensor 63 and a second pressure sensor 64 at or near
the output side of the first gear pump 61 and the second gear pump
62, respectively, upstream of or at the entrance of the first flow
channel 71 and the second flow channel 72, respectively, for
measuring the pressure of the compounds 91, 92 flowing out of the
gear pumps 61, 62 in their respective output direction G1, G2. The
extruder system 1 further comprises a second control unit 65 that
is operationally coupled to the gear pumps 61, 62 and the pressure
sensors 63, 64 for controlling the speed of the gear pumps 61, 62
based on the measurement signals from the pressure sensors 63, 64.
In particular when identical compounds 91, 92 are used, the gear
pumps 61, 62 are controlled via a feedback loop with the pressure
sensors 63, 64 and the second control unit 65 to match the
pressures of both compounds 91, 92 flowing in the respective output
directions G1, G2. When two different compounds 91, 92 are used,
test, known or given data about the ratios between the pressure and
flow rate for each of the compounds 91, 92 is stored in the second
control unit 65 and the gear pumps 61, 62 are controlled via a
feedback loop with the pressure sensors 63, 64 and the second
control unit 65 to different pressures which, according to the
data, should result in equal flow rates of the outflows U of the
compounds 91, 92 in the die 3.
[0062] FIGS. 3 and 4 show two alternative embodiments of the
invention to illustrate the scope of the invention.
[0063] FIG. 3 shows an alternative extruder system 101 according to
a second embodiment of the invention, comprising an alternative
extruder head 102. The alternative extruder head 102 differs from
the extruder head 2 as shown in FIG. 2 in that it is provided with
an alternative first flow channel 171 and an alternative second
flow channel 172 that connect to the material source 105 via the
top surface 124 and the bottom surface 125, respectively.
[0064] FIG. 4 shows a further alternative extruder system 201
according to a third embodiment of the invention, comprising a
further alternative extruder head 202 and an alternative
configuration of the material source 205 and the pump section 206.
The alternative extruder head 202 differs from the extruder head 2
as shown in FIG. 2 in that it is provided with an alternative first
flow channel 271 and an alternative second flow channel 272 that
connect to the material source 205 via a corner of the top surface
224 and the rear surface 223 and via a corner of the bottom surface
225 and the rear surface 223, respectively. The first extruder 251
and the second extruder 252, as well as the first gear pump 261 and
the second gear pump 262, respectively, are placed at an
inclination with respect to the cord plane B to improve the
alignment of the output directions G1, G2 of the respective gear
pumps 261, 262 with respect to the inflow directions F1, F2 of the
respective flow channels 271, 272.
[0065] FIGS. 5 and 6 show a further alternative extruder system 301
according to a fourth embodiment of the invention. The extruder
system 301 differs from the previously discussed extruders systems
1, 101, 201 in that its extruders 351, 352 are arranged parallel to
or in the feeding plane P so that their respective supply
directions S1, S2 are also parallel to or in the feeding plane P.
Hence, the gear pumps 361, 362 are arranged for receiving and
directing the extrudate 9 from the first extruder 351 and the
second extruder 352 in the first supply direction S1 and the second
supply direction S2, respectively, and for directing said extrusion
material 9 in or parallel to the feeding plane P into the first
flow channel 371 and the second flow channel 372, respectively, of
the extruder head 302. As shown in FIG. 6, the first supply
direction S1 and the second supply direction S2 may optionally
extend obliquely with respect to the cord plane.
[0066] To allow for easy access to the cord guide 304, the cord
guide 304 is placed on a carriage that is slidable in or parallel
to the cord plane B along a linear guide 340 to a position away
from the die 303.
[0067] It is to be understood that the above description is
included to illustrate the operation of the preferred embodiments
and is not meant to limit the scope of the invention. From the
above discussion, many further variations will be apparent to one
skilled in the art that would yet be encompassed by the scope of
the present invention.
[0068] In summary the invention relates to an extruder system and a
method for extruding cord reinforced extrudate, wherein the
extruder system comprises an extruder head with a die for receiving
extrusion material and a cord guide for guiding cords in a common
cord plane in a cord direction into the die, wherein the extruder
system comprises a first extruder and a second extruder, wherein
the extruder head comprises a first flow channel and a second flow
channel, wherein the extruder system further comprises a first pump
and a second pump for receiving the extrusion material from the
first extruder and the second extruder and for directing said
extrusion material into the first flow channel and the second flow
channel.
* * * * *