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Claims  |
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The following is claimed:
1. In an apparatus for feeding, to a plasticized polymer mass, a powdery
material which contains entrapped air, the combination which comprises:
a. an extruder having an entrance for feeding said polymer, and having an
elongated worm arranged for rotation in a housing and having worm flights
arranged to transport said polymer from said entrance to a polymer exit
formed in said housing,
b. means forming an entrance port for said powdery material together with
its entrapped air, downstream of said polymer entrance, and
c. vent means in said housing upstream of said means (b) but downstream of
said polymer entrance and sealed therefrom.
2. The apparatus defined in claim 1, wherein sealing means are provided for
forming a polymer seal between said vent means (c) and said entrance port
means (b).
3. The apparatus defined in claim 1, wherein means are provided for drawing
said air out of said housing, through said vent means (c).
4. The apparatus defined in claim 1, wherein means are provided for forming
a plasticized polymer seal between said vent means (c) and said entrance
of said extruder (a).
5. The apparatus defined in claim 1, wherein means are provided for forming
a polymer material seal downstream of said entrance port (b), and wherein
vent means are provided downstream of said seal.
6. The apparatus defined in claim 5, wherein said apparatus includes a worm
flight which is running less than full in the vicinity of said vent,
whereby volatiles are vented off at a location downstream of said polymer
material seal, and wherein means are provided downstream of said vent for
extruding the polymer product.
7. In a method for feeding, to a polymer mass, a powdery material which
contains entrapped air, the steps which comprise feeding the main polymer
feed and heating and plasticizing it, and forming it into a polymer seal
within said housing, feeding the powder additive together with its
entrained air into the housing at a point downstream of said polymer
material seal, into contact with the plasticized polymer mass at the
location of the point of introduction of said powdery material, whereby
substantial quantities of said powdery material mix with the plasticized
polymer mass and move downstream together, releasing from said housing, at
a point upstream of the point of introduction of the powdery material, the
air initially contained within said powdery material, and moving said air
from said housing.
8. The method defined in claim 7, wherein a polymer seal is also formed
downstream of the point of addition of said powdery material, said seal
being composed of a mixture of said powdery material and said main polymer
feed.
9. The method defined in claim 8, wherein volatiles are vented from said
mixture of plasticized polymer material and of said powdery material,
downstream of said seal.
10. The method defined in claim 7, wherein said air is drawn by vacuum out
of said housing. |
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Claims  |
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Description  |
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BACKGROUND OF THE INVENTION
This invention relates to an apparatus for feeding a powdery material to a
plasticized polymer mass. Such powdery material usually contains entrapped
air, and it has been a serious problem to feed and to mix the powdery
material with the main polymer feed. When the two are introduced together
in the main feed hopper of an extruder, the entrapped air is forced into
the extruder itself and, as pressure within the extruder increases, the
air is forced rearwardly, out of the main feed opening, entraining the
powdery material and propelling it rearwardly out of the entrance, thus
interfering with the entire feeding operation and causing a safety and
housekeeping problem in the plant in which the extruder is located.
DISCUSSION OF THE PRIOR ART
Various means have been utilized in an attempt to overcome the problem. It
has been proposed to use twin intermeshing screws, in order to engage and
convey both the powdery material and the polymer, but trouble is still
encountered because of the presence of air in the powdery material,
particularly when the speed of the screws is increased to commercial
levels. The air that is forced into the barrel, forcing air rearwardly
toward the hopper, and the air velocity coming back toward the feed hopper
is such that it entrains the powdered additive creating a hazard and a
housekeeping problem.
The same problem is aggravated when the powder happens to contain a small
amount of moisture, which is often the case. The moisture is heated within
the extruder, creating hot water vapor which also is expelled rearwardly
out of the feed hopper, contacting the incoming polymer and powdery
material and causing further entrainment.
Efforts have been made to overcome the problem by using so-called
"crammers" at the feed hopper, which are intended to jam the feed material
in and remove the air. Devices of this general type appear in the U.S.
Pat. to Slater No. 3,183,553, the U.S. Pat. to Oldham et al No. 3,114,930,
and the U.S. Pat. to Davis No. 2,633,074. However, they have proven
mechanically unsatisfactory and are difficult to clean and do not
eliminate entrainment of the powdered additive in the air stream.
BRIEF DESCRIPTION OF THE INVENTION
It now has been discovered that all of the foregoing problems and
disadvantages may be overcome in accordance with this invention, wherein
the extruder is provided with an entrance for feeding the polymer, a
separate entrance is provided for the powdery material, and a vent is
provided between the two entrances. The extruder, of course, has an
elongated worm (or plurality of worms either intermeshing, tangent or
otherwise) together with worm flights arranged to transport the polymer
from the entrance to a polymer exit formed in the barrel. The screws are
less than full of polymer in the area between the powder inlet port and
the air outlet port. A negative pressure is applied to the air outlet port
and is communicated to the powder inlet port to provide a significant
negative pressure at the powder inlet port.
According to this invention, means are provided forming an entrance port
for the powdery material together with its entrapped air, downstream of
the polymer entrance but upstream of the polymer exit, and vent means are
provided in the extruder barrel, upstream of the point at which the
powdery material is introduced, but downstream of the polymer entrance.
In accordance with a preferred form of the invention, means are provided
for withdrawing the air from the barrel vent, such as by using a vacuum
pump, or a vacuum eductor or the like. Further, although the great
majority of the powdery material additive is taken up by the plasticized
polymer mass as it flows downstream past the point of powdery additive
introduction, some of the powdery additive flows upstream with the air.
Accordingly, in accordance with the method of this invention, a main
polymer feed is introduced into the extruder housing and caused to flow
downstream therein, and is caused to form a material seal downstream of
the point of polymer feed. Since the powdery additive is introduced at a
point spaced downstream of the polymer seal and downstream of the vent, a
majority of the powdery additive is taken up in the main flow of polymer
as it flows past the powder feed port, but the air that was originally
present in the powder is caused to flow upstream countercurrently with
respect to the main polymer material, and is released or withdrawn from
the housing at a point upstream of the point of introduction of the
powdery additive but downstream of the polymeric material seal.
It has been discovered that surprisingly effective results are obtained in
accordance with the apparatus and method of this invention; the powdery
material mixes uniformly and intimately with the main polymer, the air
escapes from the housing smoothly and evenly, and it is even possible to
entrap particles of powder that might escape and to return them to the
system without contaminating the surrounding atmosphere.
DETAILED DESCRIPTION OF THE INVENTION
Although the invention will be described in specific terms in the portions
of the specification which follow, it will be appreciated that these
specific terms are used only for the sake of clarity, and are not intended
to limit the scope of the invention, which is defined in the appended
claims.
Turning now to the drawing, the number 10 designates an extruder, which may
be an extruder of any design, either single screw, twin screw,
intermeshing or tangent. It includes a barrel 11, desirably provided with
a heating jacket 12, and contains a screw 13 driven in rotation by a motor
(not shown) in the direction indicated by the arrow appearing at the right
hand portion of the drawing. The extruder 10 is provided with a main
polymer feed hopper 14, through which the liquid or solid polymeric
material to be processed is introduced into the extruder.
The worm 13 has a feed section 15 having flights which are constructed to
feed the polymeric material and form a material seal at the cylindrical
portion 16 of the worm. Such a seal may be formed by shallow forward
flights, or any other restrictive means instead of cylinder 16. In this
manner, the material is tightly packed, as shown, between the cylindrical
portion 16 and the barrel 11, forming a barrier which prevents the passage
of gas, such as air, past the material seal. At a point downstream of the
cylindrical portion 16, a port 20 is provided for the introduction of
powdery additive, which may contain air and frequently does. The worm
flights at that point are "starved" or less than full as indicated at 21,
but become full upstream of cylindrical portion 22 forming another
material seal of the type heretofore discussed. Downstream of the
cylindrical portion 22 a vent 23 may be provided for the release of
volatiles, and an orifice plate 24 is provided at the exit end of the
extruder.
It will be observed that a vent opening 25 is shown in the drawing,
upstream of the powdery additive port 20, but downstream of the cylinder
16, for releasing the air contained in the powdery additive from the
extruder housing. As shown, this vent housing 25 comprises a mechanical
filter having a barrel 30 and a pair of driven worms 31, 32 which may be
either intermeshing or tangent to one another, and which are driven in
rotation as indicated by the arrows thereon, in a manner to prevent any
powdery material from leaving the system, while allowing free passage of
air through and out of the housing 30.
Accordingly, it will be realized that any air that is contained in the
powdery additive is caused to flow upstream in the extruder,
counter-currently to the flow of the main polymer material therein, in the
direction indicated schematically by the arrows appearing in solid lines
in the drawing (to some extent the air flows along the flight faces), and
the air is vented or released out of the extruder through the release
means 25.
It will be appreciated that, because of the pressures that are normally
generated within the extruder housing, the air can be released through the
releasing means 25 under its own pressure. However, it is preferred to
induce the removal of air by drawing a vacuum V on the releasing means 25.
If a small amount of powder is drawn out with the air, it may easily be
contained and collected, by means well known in the art.
When a mechanical filter of the type identified by the number 25 is used,
the rotation of the worms 31, 32 tends to entrap any powder that is
entrained in the air, and to prevent it from leaving the system.
It is important in accordance with this invention to provide polymer seals
downstream of the main polymer feed and upstream of the point of
introduction of powdery additive. This isolates the main polymer feed
hopper 14 from the air that is drawn into the extruder with the powder
additive, and causes the air to flow counter-currently with respect to the
main polymer material, and to be released downstream of the material seal
16.
It is also an important and advantageous feature of this invention to
provide a polymer seal downstream of the point of introduction of the
powdery additive, since this isolates the air and forces it to flow
rearwardly, in a direction counter-current to the flow of the main polymer
material.
Although it is not always an essential feature of this invention, it is
also highly advantageous to provide a vent 23, downstream of the polymer
seal formed at the cylindrical portion 22, for venting off any volatiles
that may be contained in the main polymer feed, in the powdery additive,
or both.
The mechanical filter 30 may be eliminated or replaced by any other vent
means, including an ordinary vent, if desired. But in any event it is
important to apply the vacuum V on vent 30 and to maintain the screw
flights less than full between vent 30 and powder additive port 20, so
that a negative pressure is present at the port 20.
Although this invention has been described in connection with a specific
form thereof, it will be appreciated that many variations may be made,
without departing from the spirit and scope of the invention as defined in
the claims.
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Description  |
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