U.S. patent number 3,578,066 [Application Number 04/795,569] was granted by the patent office on 1971-05-11 for apparatus for the heating and cooling of moulds for the production of plastic bodies.
This patent grant is currently assigned to Thermovox G.m.b.H. Kunststoffmaschinen. Invention is credited to Anton J. Vox.
United States Patent |
3,578,066 |
Vox |
May 11, 1971 |
APPARATUS FOR THE HEATING AND COOLING OF MOULDS FOR THE PRODUCTION
OF PLASTIC BODIES
Abstract
In combination with a mould having an outer and an inner wall
defining a space therebetween for the flow of cooling or heating
fluid therethrough, fluid circuit means including a pressure pump
for circulating fluid under pressure through the space and bypass
means connected to the circuit means for bypassing part of the
fluid pumped by the pump past the mould to avoid overpressure in
the space and possible deformation of the mould walls.
Inventors: |
Vox; Anton J. (Ruit,
DT) |
Assignee: |
Thermovox G.m.b.H.
Kunststoffmaschinen (Ruit, DT)
|
Family
ID: |
26002081 |
Appl.
No.: |
04/795,569 |
Filed: |
January 31, 1969 |
Foreign Application Priority Data
|
|
|
|
|
Feb 2, 1968 [DT] |
|
|
P-1704375-3 |
|
Current U.S.
Class: |
165/61; 165/297;
165/254 |
Current CPC
Class: |
B29C
35/007 (20130101) |
Current International
Class: |
B29C
35/00 (20060101); F25b 029/00 () |
Field of
Search: |
;165/48,61,66,22,52,107,31,36,26,27 |
References Cited
[Referenced By]
U.S. Patent Documents
Primary Examiner: Sakalo; Charles
Claims
I claim:
1. In a moulding apparatus, a combination comprising at least one
mould having an outer and an inner wall spaced from each other and
defining between said walls a space for the passage of a heat
transfer fluid therethrough, at least said inner wall being a thin
wall to assure quick heat transfer from said fluid to moulding
material in a cavity defined by said inner wall and vice versa;
fluid circuit means for circulating the fluid through said space
and including a feed conduit communicating with said space for
feeding fluid thereinto, a return conduit for discharging the fluid
from said space and a pressure pump for pumping the fluid under
pressure through said circuit means and said space; means in said
fluid circuit means for changing the temperature of the fluid
passing therethrough; a bypass conduit between said feed conduit
and said return conduit; and regulating means cooperating with said
bypass conduit for regulating the amount of fluid flowing
therethrough so that only part of the fluid pumped by said pump
will flow through said space to thereby avoid excessive pressure in
said space which could lead to a deformation of at least said inner
wall.
2. A combination as defined in claim 1, wherein said regulating
means comprise an overflow valve in said bypass conduit.
3. A combination as defined in claim 1, wherein said regulating
means comprise a flow regulator at the junction of said feed
conduit and said bypass conduit.
4. A combination as defined in claim 1, and including a storage
container in said return conduit, said bypass conduit communicating
at one end with said storage container.
5. A combination as defined in claim 1, wherein said means for
changing the temperature of said fluid comprise heating means in
said circuit means upstream of said pressure pump for heating the
fluid.
6. A combination as defined in claim 1, wherein said means for
changing the temperature of said fluid comprise cooling means in
said circuit means upstream of said pressure pump for cooling the
fluid.
7. A combination as defined in claim 1, and including pressure
sensing means communicating with said space for sensing the fluid
pressure in said space.
8. A combination as defined in claim 7, and including means
cooperating with said pressure sensing means and said regulating
means for automatically adjusting the latter in accordance with the
fluid pressure in said space to maintain the fluid pressure below a
critical value which would cause deformation of at least said inner
wall.
9. A combination as defined in claim 1, and including a suction
pump in said fluid circuit means downstream of the junction of said
bypass conduit with said return conduit.
10. A combination as defined in claim 9, wherein the delivery of
said suction pump is greater than that of said pressure pump.
11. A combination as defined in claim 1, wherein two of said fluid
circuit means are provided, each provided with a bypass conduit and
regulating means cooperating with said bypass conduit, and wherein
said means for changing the temperature of said fluid comprises
heating means in one of said circuit means upstream of the pressure
pump thereof for heating the fluid and cooling means in the other
circuit means upstream of the pressure pump thereof for cooling the
fluid.
12. A combination as defined in claim 11, and including a one-way
valve in the feed conduit of each circuit means downstream of the
junction of the bypass conduit and the feed conduit of the
respective circuit means.
13. A combination as defined in claim 11, and including a suction
pump in each fluid circuit downstream of the junction of the bypass
conduit and the return conduit of the respective circuit means.
14. A combination as defined in claim 11, wherein at least a
portion of said bypass conduit is mounted on said mould.
15. A combination as defined in claim 1, wherein at least a portion
of said bypass conduit is mounted in said mould.
Description
The invention relates to an apparatus for the heating and cooling
of moulds used for the production of plastic bodies, particularly
by the rotary process, and having walls constructed for the
conduction of a heating or cooling liquid, provided with at least
one forward conduit, leading to the mould and having a pressure
pump, and with at least one reverse conduit which leads from the
mould and from which the liquid is conveyed back to the pressure
pump via a heating or cooling device.
The walls of such moulds have to be as thin as possible, so that
they can be rapidly heated and rapidly recooled. On the other hand,
they have to be able to stand up to the pressure of the heating or
cooling liquid pumped through the apparatus. This leads to
difficulties, particularly in the case of large-size moulds.
Furthermore, the moulds used in the rotary process have to be as
light in weight and occupy as little space as possible.
Attempts have already been made to overcome these difficulties by a
system in which, in accordance with Pat. application Ser. No.
761,222 filed Sept. 20, 1968 and now Pat. Ser. No. 3,525,098
granted Aug. 18, 1970, by the same applicant, a suction pump of
which the delivery is somewhat greater than the pressure pump is
built into the reverse conduit. This makes it possible, when it is
designed for a certain mould, i.e. for a certain flow resistance of
the mould, and for liquid of a certain viscosity, to avoid the
creation of an excess pressure, so that even very large moulds can
be constructed with comparatively thin walls and thus
satisfactorily heated or cooled. This system also renders it
possible, owing to the fact that the liquid is pumped in and
withdrawn by suction simultaneously, to circulate the said liquid
at a high speed, so that the temperature gradient from the entry to
the emergence of the heating or cooling liquid remains very
limited, as a result of which even very large moulds can be kept to
a certain constant temperature. This is of importance, since it is
particularly with these large moulds that an even heating is often
a decisive factor for the quality of the plastic bodies produced
with them.
To provide a further improvement, the aforementioned apparatus
comprises a heating liquid circuit and a cooling liquid circuit
separate therefrom, each of these circuits having its own pressure
pump and its own suction pump of the type described.
The effectiveness of the above measures in accordance with the
older Patent Application Ser. No. 761,222 filed Sept. 20, 1968 and
now Pat. No. 3,525,098 granted Aug. 18, 1970 nevertheless depends,
as already mentioned, on the flow resistance of the mould and on
the viscosity of the liquid pumped through it. In an apparatus of
this kind, e.g. a rotation machine, however, a great variety of
moulds have to be used, often of widely differing capacity and area
and thus presenting different degrees of resistance to the
through-flow. Furthermore, the viscosity of the heating or cooling
liquid used depends to a great extent on the temperature, so that
when the heating is carried out, at 220.degree. C., for instance,
it is far lower than when the cooling is effected, at 40.degree. C.
The heating and cooling temperature selected also depends on the
conditions prevailing in the mould and the plastic body to be
produced and above all on the nature of the plastics to be
processed. It has been found that a mould through which heating
liquid flows satisfactorily undergoes deformation when cooling
liquid is passing through it, owing to the higher viscosity and the
resulting lower rate of through-flow and higher pressure, and that
it may burst open in consequence. The same thing can occur if the
apparatus is designed for a particular mould with a particular
resistance to flow and a different moulds with a greater internal
resistance to flow is then employed. It is true that these dangers
can be counteracted by designing stronger moulds, but this is at
variance with the requirement that the moulds are to be as
thin-walled as possible, so that they can be heated rapidly and
also recooled rapidly.
In an apparatus with a supplementary suction pump in the return
conduit, it has been found to be a still more serious drawback that
with the use of a mould in which a higher pressure is built up,
either owing to the mould itself or owing to the higher viscosity
of the liquid, the suction pump no longer receives enough liquid,
so that the heating or cooling apparatus following it in the
circuit is no longer subjected to a correct flow of liquid. The
pressure pump then no longer receives heating or cooling liquid at
the exact temperature required, so that the exact control or
regulation of the heating or cooling of the mould breaks down.
The purpose of the invention is to provide an apparatus of the type
described at the beginning which will ensure that the mould is kept
free of undesirable excess pressures and also, if necessary, that
the suction pump will always be fed sufficiently and that a
sufficient quantity of liquid will at all times flow through the
heating or cooling apparatus following it in the circuit, whatever
the mould used, whatever its internal resistance to flow, whatever
the heating or cooling liquid used and whatever the viscosity
adopted, a further aim being comparative simplicity in the
apparatus. The invention enables this object to be achieved by a
system in which, between the pressure pump and the mould, a branch
conduit is connected up to the forward conduit, leads into the
reverse conduit and contains an overflow valve, or is connected up
to a flow regulator of the forward conduit. When the pressure in
the mould, either as a result of the internal flow resistance of
the mould or in consequence of a higher viscosity of the liquid,
e.g. as a result of the temperature of 40.degree. C. in the cooling
liquid, as compared with 220.degree. C., which is that of the
heating liquid, rises above a certain level, the overflow valve in
the branch conduit opens to a greater or smaller extent, enabling a
greater or a smaller quantity of liquid to flow direct into the
return conduit. The mould is thus kept free of excess internal
pressures. For this reason it is desirable for a pressure gauge for
the liquid conveyed through the apparatus to be provided shortly
before the mould is reached, or preferably on the mould itself.
Furthermore, the overflow valve can with advantage consist of a
pressure-controlled valve. The aforementioned pressure gauge can be
operatively connected with this latter valve, thus ensuring
automatic regulation. It may also be sufficient, however, for the
overflow valve to be set by hand, when it is in particular the
internal flow resistance of a mould that has to be considered, and
not so much the change of the viscosity as between the heating and
the cooling liquid. This is particularly the case when, as already
suggested in the aforementioned older patent application, the
operation is being carried out with a heating liquid circuit and
with a cooling liquid circuit separate therefrom, in which case
each of these circuits has its own pressure pump and its own return
pump of the type mentioned. In accordance with the invention it is
then desirable for a branch conduit of this kind to be provided in
each circuit. By comparison with the object of the aforementioned
older patent application, this provides the advantage that on the
average a more satisfactory and reliable through-flow is obtained
for a large number of different moulds with simpler means, i.e.
dispensing with a suction pump mounted in the return conduit, so
that these moulds can be made with very thin walls without any
danger of bursting.
In an apparatus in which the return conduit contains a suction
pump, in accordance with the proposal made in the aforementioned
older patent application, the delivery of the said suction pump
being preferably somewhat greater than that of the pressure pump,
the liquid being conveyed back to the pressure pump from the
suction pump via the heating or cooling device, the invention
provides that the branch conduit, as an additional supply conduit
for the suction pump, is to lead into the return conduit before
reaching the said suction pump. By this additional branch-flow
supply conduit for the suction pump, this latter is at all times
fed with sufficient heating or cooling liquid. The flow of liquid
is not interrupted in the pump, and a correct flow continues
through the subsequent heating and cooling devices. If the pressure
in the mould, either owing to the internal flow resistance of the
latter or as a result of a higher viscosity in the liquid, e.g. in
consequence of the temperature of 40.degree. C. in the cooling
liquid, as against the temperature of 220.degree. C. in the heating
liquid, rises above a certain level, the overflow valve in the
branch-flow supply conduit opens to a greater or smaller extent and
feeds a greater or smaller additional quantity to the suction pump.
If the process is carried out with a heating liquid circuit and
with a cooling liquid circuit separate therefrom, each such circuit
having its own pressure pump and its own suction pump of this kind,
then it is desirable, in accordance with the invention, for a
branch-flow supply conduit of this kind, for the particular suction
pump concerned, to be provided in each such circuit.
In another embodiment of the invention the branch-flow conduit is
in each case connected up to a flow regulator of the particular
forward conduit concerned. This suffices particularly in those
cases in which it is especially the internal flow resistance of the
mould that has to be taken into consideration and the change in the
viscosity of the particular liquid flowing through the mould, owing
to the provision of a cooling circuit separate from the heating
circuit, can be taken into account in some other manner, e.g., by
an appropriate preliminary setting of the flow regulator in each
forward conduit. The capacity and internal area of each mould used,
and thus its internal resistance to the flow, are known. Each mould
can thus be allocated a certain characteristic number, in
accordance with the internal resistance to flow, by which code
number the flow regulator can be set, in addition to adjusting it
in accordance with the viscosity of the liquid in question. It then
diverts a certain quantity of the flowing liquid into the branch
conduit, or into the supply conduit of the branch flow, for the
suction pump concerned. No pressure is then required on the mould.
Preferably, however, a pressure gauge, or at least a means of
connecting up a pressure gauge, should nevertheless be provided,
for control purposes.
The branch conduit concerned can also be provided on or in the
mould itself. To this extent, a mould of this kind is then to be
regarded as an integral part of the apparatus to which the
invention relates.
Further details and advantages of the invention will emerge from
the following description of examples illustrated schematically in
the drawing. The diagrams are as follows:
FIG. 1 is a schematic diagram of a first version, with pressure
pump and suction pump;
FIG. 2 is a schematic diagram of a second version, with pressure
and suction pumps;
FIG. 3 is a schematic diagram of a third version, with pressure
pump only.
The mould 1 shown in the drawing is of the double-walled type, with
an internal chamber 2, for the through-flow of heating or cooling
liquid. In the version shown in FIG. 1, a forward conduit 3 leads
into this internal chamber 2, and a return conduit 4 leads out of
it. The forward conduit 3 contains a pressure pump Pd and the
return conduit 4 a suction pump Ps. The latter preferably has a
higher rate of delivery than the pressure pump Pd. From the suction
pump Ps the liquid is conveyed back to the pressure pump Pd via a
heating or cooling device not shown in the drawing, appropriate
control mechanisms being provided.
In the example of the invention shown in FIG. 1, a branch supply
conduit 5 for the suction pump Ps is connected to the forward
conduit 3, between the pressure pump Pd and the mould 1, and leads
into the return conduit 4, before reaching the suction pump, and
contains an overflow valve 6. A pressure gauge 7 for the liquid
conveyed through the apparatus is provided on the mould 1. The
overflow valve 6 is adjusted by hand, according to the said
pressure gauge. As shown at 8, the pressure gauge 7 can also be
connected up shortly before the mould 1. A control connection 9 is
also shown, in dot-and-dash lines, between the pressure gauge 7 and
the overflow valve 6, the overflow valve 6 being automatically
controlled via the said control line.
In the version shown in FIG. 2, a heating liquid circuit is
provided, with a forward conduit 10, a pressure pump Pdh, a return
conduit 11 and a suction pump Psh. From the latter the heating
liquid is conveyed via a heating device 12 back to the pressure
pump Pdh. In a similar manner to that shown in FIG. 1, a branch
supply conduit 13 is connected up to the forward conduit 10 of the
heating circuit and leads into the return conduit 11 before
reaching the suction pump Psh, the said branch leading from a flow
regulator 14 of the forward conduit 10. The said regulator is set
to the viscosity of the heating liquid used and also adjusted in
accordance with the internal flow resistance of the particular
mould 1 used. Furthermore, a cooling liquid circuit is provided,
with a forward conduit 15, a pressure pump Pdk, a return conduit 16
and a suction pump Psk. From this latter the heating liquid is
conveyed back to the pressure pump Pdk concerned, via a storage
container 17 and/or a cooling device not shown in the drawing.
Between the forward conduit 15 and the return conduit 16, and in a
similar manner to the version with the heating circuit, is a
branch-flow supply conduit 18 for the suction pump Psk concerned.
This branch supply conduit 18 starts from a flow regulator 19 built
into the forward conduit 15. Before the mould is reached, the
forward conduit 10 of the heating circuit and the forward conduit
15 of the cooling circuit lead into one common supply conduit 21,
to the mould 1, a nonreturn valve 20 of the customary kind being
interrelated in the case of each of the said forward conduits. In
similar fashion, one common discharge conduit 22 leads from the
mould and then branches off into the two return conduits 11 and 16.
In this version shown in FIG. 2, likewise, a pressure gauge can be
mounted shortly before the mould 1 is reached, or on this latter.
The flow regulators 14 and 19 are set either according to the said
pressure gauge or according to the characteristic numbers allocated
to the mould in question. They ensure that the suction pump Psh or
Psk, as the case may be, is at all times fed with an adequate
quantity of liquid, so that the correct flow takes place through
the heating and cooling devices. Furthermore, this system keeps the
mould free of excessive internal pressures.
It is naturally also possible, in the case of heating and cooling
circuits separate from each other, for an overflow valve 6, in
accordance with the version shown in FIG. 1, to be mounted in the
branch-flow supply conduit, 13 or 18, as the case may be.
The mould 1 shown in FIG. 3 is likewise of the double-walled type,
with an internal chamber 2 for the through-flow of heating or
cooling liquid. A forward conduit 3 leads into this internal
chamber 2, and a return conduit 4 starts from the latter. To this
extent, this version coincides with these shown in FIGS. 1 and 2
and described in the foregoing. In the forward conduit 3 a pressure
pump 24 is provided. The return conduit 4 leads to a storage
container 25, which may contain a heating or cooling device 26.
From there the liquid is conveyed via a conduit 27 back to the
pressure pump 24, appropriate control mechanisms being
provided.
The invention provides that between the pressure pump 24 and the
mould 1 a branch-flow supply conduit 28 is to be connected up to
the forward conduit 3, lead direct into the storage container 25
and contain an overflow valve 29. The branch conduit 28, however,
can also lead into the return conduit 4 before the storage
container 25 is reached. The mould 1 bears a pressure gauge 30 for
the liquid caused to pass through the apparatus. The overflow valve
29 is set by hand in accordance with the said gauge. The pressure
gauge 30 can also be connected up to the forward conduit 3 shortly
before the mould 1 is reached. Furthermore, a control line 31,
shown in dot-and-dash lines, is mounted between the pressure gauge
30 and the overflow valve 29, via which said line the overflow
valve 29 can be automatically controlled.
A further component shown in dot-and-dash lines is a flow regulator
32 in the forward conduit 3, and this can be provided in place of
the overflow valve 29, and the branch conduit 28 is then connected
to it. This flow regulator 32 is set in accordance with the
internal flow resistance of the particular mould 1 employed, either
in accordance with the pressure gauge 30 or in accordance with the
characteristic numbers allocated to the mould concerned. This keeps
the mould free of excessive internal pressures.
FIG. 3 shows, in dot-and-dash lines, a further variant, in which,
with the container 25 constructed as a simple storage container,
i.e. without cooling or heating device 26, a pump 33 is provided
behind it, by which the liquid is pumped out of the storage
container 25 into a special heating or cooling device 34, from
which it is conveyed to the pressure pump 24 via a conduit 35.
In the drawing, only one heating or cooling device 26, 34, is shown
in each case. An appropriate cooling device is to be connected in
parallel with a heating device, suitable control mechanism being
provided in order to ensure that the heating circuit is closed, via
the heating device, and that the cooling circuit is closed, via the
cooling device, and that in either case the branch-flow conduit 28
takes effect. This is why the heating circuit and the cooling
circuit have a section of forward conduit and a section of return
conduit in common. The branch conduit 28 then leads, in each case,
into the conduit which the said circuits have in common.
It is also possible to provide, in a manner not shown in the
drawing, a heating liquid circuit and a cooling liquid circuit
separate therefrom, a pressure pump 24 and a storage container 25
and, in accordance with the invention, a branch conduit 28 with an
overflow valve 29 or flow regulator 32, then being associated with
each circuit.
In practice the entire apparatus forms part of a machine,
particularly a rotary machine, for the production of plastic
bodies. The apparatus to which the invention relates is then
mounted in or on the body of the machine.
* * * * *