(19) |
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EP 0 131 063 A1 |
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EUROPEAN PATENT APPLICATION |
(43) |
Date of publication: |
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16.01.1985 Bulletin 1985/03 |
(22) |
Date of filing: 12.07.1983 |
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International Patent Classification (IPC)4: B65B 1/12 |
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(84) |
Designated Contracting States: |
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BE CH DE FR GB LI |
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Applicant: PIMI SPA |
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Bologna (IT) |
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(74) |
Representative: Sassatelli, Franco T., Dr. |
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c/o INIP
5, via Ruggi 40137 Bologna 40137 Bologna (IT) |
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(54) |
Double screw disaerator |
(57) @ The system brings the product alternatively in feeding motion on two lines in contact
with the counterposed walls of an envelope to centrally converge in the interspace
between the pair of screws (9,10) side by side between their intercrossing spirals.
The feeding system in a conduct, where a vacuum compartment is operating, avoids that
the advancing product obstructs the conduct.
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[0001] The invention refers to a disaeration equipment for reducing the volume of powdery
products permitting to lower the production costs, in particolar those of the packing
material, of the storing areas, the transport ones and by increasing the speed of
the outomatic machine manufacturing. The above equipment permits a particular employ
in the manufacturing lines and can be combined with a dosing implement for automatic
manufacturing and sacking machines. The equipment is capable of condensing powders
with any degree of granulometry, smoothness and chemical composition and it employs
an equipment for self-regulating vacuum and electrical con- rrol board for the automatic
working and regulation. The compartment is structured in powder seal parts and can
be easily disassembled for performing the inside cleaning.
[0002] In explicating versions, inside parts are foreseen in stainless steel with employ
of sealed equipments, or in explosion-proof construction. In special executions, the
employ is foreseen for using transport "con tainers" and of production unities in
general. The exigency of disaeration equipments for powdery products corresponds to
precise exigencies of reducing the costs of production and of a better conversation
of products such as those in sealed packing. The proceeding consents a volume reduction
variable from 20 to 80% according to the features of the product to be produced and
can be employed in any production pro cess.
[0003] At present, equipments are used in which the powder is foreseen to be put into a
cylindrical conduct where the feed motion if performed by means of a screw feeder
and disaeration is obtained by compression thickening of the product against the cylindrical
wall and suction effect carried out by a vacuum assembly using a suction pump. This
proceeding has considerable employ limits and can be used with powders having low
specific weight only such as antigarasites in general. The feed motion of the screw
in the conduct, in fact, causes a thickening of the pow-
der with a "plug" effect which blocks the powder feed motion. The contrivance according
to the invention permits to obviate this inconvenien ce and allows to operate with
powders of any type whatever with variable granulcmetry and weight. This is possible
thanks to the fact that a fee ding compartment for the power feeding of new conception,
substantially characterized by a pair of screws fitted side by side and the spirals
of which are intersecting each other in a conduct having simmetrical half-parts of
containment. In this way, the fed material is brought in succes sion in the interspace
between the intersected spirals. This avoids the thickening with continuous effect
in the feed conduct wall and, therefore, permits the products transport phase for
the disaeration purpose.
[0004] In the execution shown as an example of the proceeding, the positioning of the two
shafts 2 and 3 is foreseen with pinions 4 and 5 connected by means of chains 6 and
7 to a motor variator 8. Two screws 9 and 10 are connected to these two shafts and
after having crossed the vacuum case 11, they are sustained by the two supports 12
and 13 contained in the machine base 14. The two screws in the vacuum case inside
are contained in two symmetrical half-parts 15 and 16, which form a total fee ding
envelope of the powder. This envelope is structured according to po rous and metal
layers for support. To operate the equipment, the powder product is introduced into
the machine head and the screws 9 and 10 are started which transport it up to the
unloading point 14. In the vacuum chamber 11, the air contained in the product is
sucked, while the envelope structure formed by half-parts 15 and 16 prevent the products
from been sucked with the air. The unloaded product appears compact and agglomerated.
Essentially, the proceeding allow versatility of employ for all the production processes
of powders in general because the double screw system permits the mechanical compaction
of the product by means of a mechanical tamping and a continuous feeding transport.
This is pos sible through the fact that the fed product, in contact with the outer
walls of the feeding conduct, is put into the interspace between the two intersecting
spiral screws.
[0005] In the not limiting execution form of Table 1, fig. 1 is the view of the disaeration
plant in perspective view for employ condition, showing the vacuum assembly as an
accessory and electrical control board. Fig. 2 is the longitudinal section view of
the machine showing the double screw feeding compartment. Fig. 3 is the transversal
section of the ma chine in correspondence vith the double screw to point out the section
of the feeding compartment which brings alternatively the product forward in contact
with the conterposed inside walls and with the interspace between the screw spirals.
In practice, the particulars of execution, the shape and similar of the invention
may vary, in an analogous way to the structuration of the feeding conduct, to the
screw sizes and to the power of vacuum assembly. All elements are moreover liable
to be replaced by other equivalent ones.
1) Double screw disaerator, characterized by the fact that it allows to operate with
powders of any specific weight and granulometry what ever by means of a proceeding
which brings alternatively into feeding the product on two lines into contact with
the oounterposed walls of envelope to converge centrally in the interspace formed
by the pair of screws one near the other between their intercrossing spirals. This
feeding susten of the product in the conduct, where a compartment is operating for
the vacuum, to allow the sucking effect, avoids that the obstruction in the product
feeding should clop the conduct. This is permitted by the fact that the obstruction
with effect continuity is avoided in the feeding conduct.
2) Double screw disaerator, according to the previous claim, cha- recterized by the
fact that, in a version, a compartment has been foreseen which employs head 1 for
positioning shafts 2 and 3 with pinion 4 and 5 connected to a motor variator 8 by
means of two chains. To these two shafts, two screws 9 and 10 are connected which
having crossed the vacuum case 11 are sustained by two supports 12 and 13 con., tained
in the machine base 14. The two screws are positined in a conduct formed by two symmetrical
half-parts 15 and 16. For operating the machine , the product in powder is introduced
into the machine head and the two screws 9 and 10 are started which transport it to
the unloading point 14. In the vacuum chamber 11, the air contained in the product
is sucked and the product cane out from the point 14 compact and agglomerated.
3) Execution form of a disaeration compartment substantially as described and illustrated
for the above spefied purposes.
