U.S. patent number 3,770,249 [Application Number 05/263,316] was granted by the patent office on 1973-11-06 for mixing, homogenizing and emulsifying apparatus.
This patent grant is currently assigned to Firma J. S. Pelzholdt. Invention is credited to Armin Schmitt.
United States Patent |
3,770,249 |
Schmitt |
November 6, 1973 |
MIXING, HOMOGENIZING AND EMULSIFYING APPARATUS
Abstract
An apparatus for mixing, homogenizing and emulsifying liquid and
liquid/solid mixtures comprises a plurality of individual chambers
connected in series. Each chamber has the shape of a double frustum
and adjacent chambers are connected to each other by supply and
discharge channels which enter the individual chambers
tangentially.
Inventors: |
Schmitt; Armin (Heusenstamm,
DT) |
Assignee: |
Firma J. S. Pelzholdt
(Frankfurt/Main, DT)
|
Family
ID: |
5811053 |
Appl.
No.: |
05/263,316 |
Filed: |
June 15, 1972 |
Foreign Application Priority Data
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|
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|
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Jun 18, 1971 [DT] |
|
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P 21 30 134.8 |
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Current U.S.
Class: |
366/149; 366/336;
366/165.1; 366/337 |
Current CPC
Class: |
A23G
1/10 (20130101); B01F 5/0604 (20130101); A23G
1/042 (20130101) |
Current International
Class: |
A23G
1/10 (20060101); A23G 1/04 (20060101); B01F
5/06 (20060101); B01f 015/02 () |
Field of
Search: |
;259/4,18,36,DIG.30 |
References Cited
[Referenced By]
U.S. Patent Documents
Primary Examiner: Jenkins; Robert W.
Claims
What is claimed is:
1. In apparatus, for mixing, homogenizing and emulsifying liquid
and liquid/solid mixtures, of the type comprising a plurality of
individual chambers series connected in the flow direction
connected to one another via supply and discharge channels, the
improvement comprising forming the individual chambers in the shape
of a double frustum and providing connecting channels which enter
and leave the individual chambers tangentially in such a way that
in the flow direction adjacent individual chambers are alternately
connected in the area of their largest cross section and then in
the area of their smallest cross section.
2. Apparatus according to claim 1, wherein the individual chambers
comprise frustums arranged with their smallest cross sections
towards one another.
3. Apparatus according to claim 1 wherein the connecting pipes of
the chambers in the flow direction consecutively have smaller cross
sections.
4. Apparatus according to claim 1, wherein the connecting pipes of
the chambers in the flow direction consecutively have larger cross
sections.
5. Apparatus according to claim 1, wherein the individual chambers
comprise a plurality of superimposed and interconnected
frustums.
6. Apparatus according to claim 5, wherein the series connected
individual chambers are arranged approximately in a circular
formation, wherein said housing consists of individual plates
arranged between end plates whereby the frustum shaped halves of
the chamber and connecting pipes are cut into the stacked
individual plates, and wherein the housing is placed in a further
housing whereby the space formed between the housings is provided
with supply and discharge pipes for a cooling or heating
medium.
7. Apparatus according to claim 1, wherein the series connected
individual chambers are arranged approximately in a circular
formation.
8. Apparatus according to claim 1, comprising a housing consisting
of individual plates arranged between end plates whereby the
frustum shaped halves of the chamber and connecting pipes are cut
into the stacked individual plates.
9. Apparatus according to claim 8, wherein the housing is placed in
a further housing whereby the space formed between the housings is
provided with supply and discharge pipes for a cooling or heating
medium.
10. In apparatus, for mixing, homogenizing and emulsifying liquid
and liquid/solid mixtures, of the type comprising a plurality of
individual chambers series connected in the flow direction
connected to one another via supply and discharge channels, the
improvement comprising forming the individual chambers in the shape
of a double frustum and providing connecting channels which enter
and leave the individual chambers tangentially in such a way that
in the flow direction adjacent individual chambers are alternately
connected by means of the area of their smallest cross section
being in communication with the area of their largest cross
section.
11. In apparatus, for mixing, homogenizing and emulsifying liquid
and liquid/solid mixtures, of the type comprising a plurality of
individual chambers series connected in the flow direction
connected to one another via supply and discharge channels, the
improvement comprising forming the individual chambers in the shape
of a double frustum and providing connecting channels which enter
and leave the individual chambers tangentially in such a way that
in the flow direction adjacent individual chambers are alternately
connected by means of the area of their largest cross section being
in communication with the area of their smallest cross section.
Description
BACKGROUND OF THE INVENTION
The invention relates to an apparatus, for mixing, homogenizing and
emulsifying liquid and liquid/solid mixtures, of the type
comprising a plurality of individual chambers arranged in series in
the flow direction which are connected with one another by supply
and discharge channels.
A large number of apparatus are known for mixing, homogenizing and
emulsifying media having a liquid to pasty consistency. In
particular for emulsifying so-called high pressure homogenizing
machines are widely used. These machines generally function in such
a manner that a coarse dispersion prepared in a separate
installation and consisting of the ingredients to be mixed is
brought to an elevated pressure, e.g., 400 kp/cm.sup.2 with the aid
of a volumetrically operating pump.
Immediately thereafter the dispersion is released again through one
or more narrow slot-like cross sections. If for example a water/oil
mixture is subjected to such a treatment then a more or less stable
emulsion is obtained. The grease and water particles are so
deformed during this process that they are divided up into a
plurality of small globules.
The smaller the particle size and the narrower the distribution
spectrum the more stable the emulsion.
Homogenizing machines of the type described only operate with
adequate homogenizing action at pressures in the range of
approximately 50 and above kp/cm.sup.2. As the energy used in
obtaining the necessary pressures cannot be recovered the running
costs of such machines are unnecessarily high. Therefore numerous
other designs have been developed which operate according to most
varied methods. The homogenizing takes place hereby at pressures up
to about 10 kp/cm.sup.2. Due to the smaller pressures the energy
requirements of such machines are correspondingly lower. However
the homogenizing action which in these designs is also
substantially dependent on the pressure gradient level is reduced.
Thus such machines can generally only be used for problems which
are relatively easy to solve. They are not suitable for difficult
tasks.
SUMMARY OF THE INVENTION
An object of the invention is therefore to obviate, or at least
reduce, the described disadvantages particularly the too high power
consumption, the costly and inefficient medium or high pressure
pumps and the coarse dispersion plant.
This problem is solved with an apparatus of the type indicated
hereinbefore according to the invention in that the individual
chambers are formed in the shape of a double frustum and connecting
channels are provided which enter and leave the individual chambers
tangentially in such a way that in the flow direction adjacent
individual chambers are alternately connected in the area of their
largest cross section and then in the area of their smallest cross
section.
As a result of this construction there is a multiple dividing and
recombining of the flow of the material to be mixed of alternating
composition and the homogeneity or efficiency of mixing of the flow
of material to be mixed increases progressively with the number of
separation and/or recombining actions whereby consequently the
physical effect is utilised that both in a vortex source and in the
vortex sump considerable flow distortions occur, i.e., secondary
flows are formed which can lead to a partial mutual displacement of
the particles of the material to be mixed.
As comminutable solid particles on passing through the apparatus
particularly at the edges of the mouth of the connecting channels
can undergo comminution, it is advantageous in view of this to so
design the apparatus that the connecting pipes which enter or leave
the chambers tangentially are successively smaller in their cross
sectional dimensions in the flow direction.
Some substance mixtures e.g., emulsions reveal a strong increase in
their consistency during treatment. For such cases it is therefore
advantageous to successively widen the connecting pipes between the
individual chambers of the apparatus in the flow direction.
A development of the apparatus whereby each chamber is so arranged
relative to the following chamber that its largest or smallest
cross section is located in the plane of the smallest or largest
cross section of the previous chamber leads advantageously to a
very compact possibility of arranging the individual chambers and
therefore to a very compact construction of the apparatus which
similarly can advantageously be so developed that the
series-connected individual chambers are arranged approximately in
a circular formation.
In order to obtain maximum flows it is possible whilst retaining
the same solution principle to so advantageously develop the
apparatus that the individual chambers comprise a plurality of
superimposed and interconnected frustums.
The apparatus according to the invention is also very advantageous
from a constructional and manufacturing viewpoint because it can be
so developed that the centrifugal chamber comprises a housing
consisting of individual plates arranged between end plates whereby
in the frustum-shaped cavities and connecting channels are cut into
the stacked individual plates, and which also leads to the
possibility of accommodating this housing in a further housing
whereby the space formed between the housings is provided with feed
and discharge pipes for a cooling or heating medium, whereby
according to the treatment requirements of the ingredients to be
mixed an appropriate temperature control of the complete apparatus
can take place. Cross sectionally frustum-shaped divisions of the
mixing chamber are already known from U.S. Pat. No. 2,391,110, but
in that case it is a cylindrical container which is axially
traversed over its complete cross section whereby in said container
conical plates are stacked and the plates are completely perforated
on their surfaces. The geometry of the centrifugal chambers
selected in the mixer according to the invention is a purely
functional shape physically pre-determined by the desired flow
pattern -- vortex source/vortex sump. The same applies for the
tangential connecting channels. As opposed to this in the mixer
according to U.S. Pat. No. 2,391,110 there is no necessity for
having the perforated bodies in other than a plate-shaped geometry,
because the flow is always axially directed and no improvement of
the mixing effect can be expected from other external shapes of
said perforated bodies. In the object of U.S. Pat. No. 2,391,110 in
front of and behind each perforated body the same physical
processes take place, i.e., a repetition of equivalent effects.
However in the case of the object of this application the number of
branching paths for the material for mixing increases with an
increasing number of individual chambers according to a
mathematical interrelationship. Thus in principle the object of the
U.S. Patent relates to a parallel and series connection of a
particular number of perforated bodies which are traversed by the
product to be mixed, producing at their outlet cross sections a
free non-directed turbulence which is associated with high pressure
losses and heat generation. Much the same happens with the object
of U.S. Pat. No. 3,417,967 where the product to be mixed flows
through series and parallel connected perforated bodies. Once again
free non-directed turbulence occurs which is linked with high
energy losses and heat generation. Here again the loss factor is at
an estimate at least a tenth power higher than in the mixer
according to the invention.
BRIEF DESCRIPTION OF THE DRAWINGS
For a better understanding of the invention, reference will now be
made, by way of example, to the accompanying drawings, in
which:
FIG. 1 shows a section through an apparatus in accordance with the
invention;
FIG. 2 is a plan view of the apparatus shown in FIG. 1;
FIG. 3 is a section through another embodiment of an apparatus in
accordance with the invention;
FIG. 4 is a section through a further embodiment of an apparatus in
accordance with the invention;
FIG. 5 shows schematically one arrangement of the individual
chambers of an apparatus in accordance with the invention;
FIG. 6 shows schematically a further arrangement of the individual
chambers; and
FIG. 7 shows partly in section and partly in elevation an
arrangement of an apparatus within a thermostatically controlled
housing.
DESCRIPTION OF THE PREFERRED EMBODIMENTS
Referring to the drawings, reference numeral 1 identifies
individual chambers which are connected together by connecting
pipes 2. Each chamber 1 comprises two or more frustums 5 having a
larger end 3 and a smaller end 4. Disposed at either end of the
chambers 1 are plates 6. Between the plates 6 are individual plates
7 into which are cut the frustums 5 as halves of the individual
chambers and the connecting pipes 2. Plates 6 and 7 assembled
together in a stack and correspondingly held together form the
apparatus housing 8 or 8' (FIGS. 5 and 6) to which via supply
openings or pipes 13 the material for mixing is supplied under
pressure and whereby after traversing the individual chambers 1 it
leaves the same again via the discharge opening or discharge pipe
14.
In FIGS. 1 and 2 the individual chambers 1 are series connected in
such a way that the material for mixing initially flows into the
chamber 1 in the area of its smallest cross section and leaves the
same again in the area of largest cross section 3, and in the area
of largest cross section passes into the next chamber 1 which it
then leaves in the area of smallest cross section etc. FIG. 2 shows
clearly the course of the connecting pipe.
The embodiment of FIG. 3 differs from that according to FIG. 1 in
that the individual chambers 1 are to a certain degree nested in
each other i.e., the largest or smallest cross sections 3, 4 of
adjacent chambers are located in common planes.
This leads to the operational difference that the mixture flow
passes from a large cross section via the relevant connecting pipe
into a small cross section.
According to FIG. 4 the chambers are also to a certain extent
multi-staged whereby however all partial areas of one chamber are
directly connected.
As is shown by the flow arrows in this figure there is a greater
fanning out of the total flow and the total throughput is obviously
greater than in the embodiments of FIGS. 1 and 3.
Apart from these variants of the chamber design and arrangement it
is naturally also possible to change the chambers as regards their
formation.
Unlike in the arrangement according to FIGS. 1 to 4 the chambers
according to FIG. 5 are arranged approximately in two circles
parallel to the supply and discharge openings 13, 14 whereas
according to FIG. 6 all are series connected in one approximately
circular formation.
As indicated the apparatus with its individual chambers is
advantageously so constructed that the apparatus housing 8 or 8' is
made from individual plates 7 wherein are cut the chamber halves
and connecting pipes whereafter the correspondingly worked
individual plates are stacked and held together so as to be
precisely aligned with the end plates 6.
The arrangement of such a shousing 8 within the thermostatically
controlled housing 9 provided with supply and discharge pipes 11,
12 to the inner chamber 10 is shown in FIG. 7.
In addition to the indicated advantages this apparatus also
provides the advantages of a minimum expenditure for sealing and
good cleaning possibilities.
* * * * *