U.S. patent number 3,646,688 [Application Number 04/741,511] was granted by the patent office on 1972-03-07 for apparatus for countercurrent heat treatment of biological tissue.
This patent grant is currently assigned to Astra Nutrition Aktiebolag. Invention is credited to Sven Olof Osterman.
United States Patent |
3,646,688 |
Osterman |
March 7, 1972 |
**Please see images for:
( Certificate of Correction ) ** |
APPARATUS FOR COUNTERCURRENT HEAT TREATMENT OF BIOLOGICAL
TISSUE
Abstract
A device and a method for a continuous heat treatment of
biological tissue material that may or may not be disintegrated,
such material comprising, e.g., fish, wherein the material is
treated with heat in countercurrent to the material flow using a
vertically arranged container provided with at least one vertically
arranged shaft mounted for rotation. The shaft is provided with
stirrers each having a vertical and helical pitch and being adapted
to work the material zone by zone in vertical and horizontal
directions.
Inventors: |
Osterman; Sven Olof (Molndal,
SW) |
Assignee: |
Astra Nutrition Aktiebolag
(Molndal, SW)
|
Family
ID: |
20291925 |
Appl.
No.: |
04/741,511 |
Filed: |
July 1, 1968 |
Related U.S. Patent Documents
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Application
Number |
Filing Date |
Patent Number |
Issue Date |
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662819 |
Aug 23, 1967 |
3565634 |
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Foreign Application Priority Data
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Jun 30, 1967 [SW] |
|
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10215/67 |
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Current U.S.
Class: |
34/168 |
Current CPC
Class: |
F26B
17/1483 (20130101); B01F 7/24 (20130101); A23J
1/04 (20130101); A23K 10/22 (20160501) |
Current International
Class: |
A23K
1/10 (20060101); A23J 1/04 (20060101); A23J
1/00 (20060101); F26B 17/14 (20060101); B01F
7/24 (20060101); F26B 17/12 (20060101); F26b
017/12 () |
Field of
Search: |
;34/73,166,168,173,175,176,177,182,60,64,65,241 ;23/270
;99/348 |
References Cited
[Referenced By]
U.S. Patent Documents
Primary Examiner: Sukalo; Charles
Assistant Examiner: Ramey; Harry B.
Parent Case Text
The present invention is a continuation-in-part application of
United States application Ser. No. 662,819, filed Aug. 23, 1967,
now U.S. Pat. No. 3,565,634, and relates to a device for a
continuous heat treatment of biological tissue material, this
material being or not being disintegrated, by means of a gaseous
heat transmission medium in countercurrent to the material flow,
said device comprising a vertically arranged container provided
with at least one vertical shaft mounted for rotation, the
container being provided with a feeding device connected to its
upper portion and a discharge device connected to its lower portion
for the material and at least one lower feeding conduit and at
least one upper discharge conduit for the gaseous heat transmission
medium.
Claims
I claim:
1. An apparatus for the continuous treatment of disintegratable
biological tissue material with a gaseous heat transmission medium
moving in countercurrent relationship to the flow of the tissue
material comprising a vertically disposed container, a
material-feeding means for supplying material to the upper portion
of said container, a material discharge means for removing material
from the lower portion of said container, a heat transmission
medium distribution means for supplying a gaseous heat transmission
medium to the lower portion of the container, and a lifting means
for circulating the material within a series of successive vertical
zones by interrupting the downward flow of the material and
displacing it upwardly whereafter it is allowed to repeat its
downward movement through the zone in countercurrent relationship
to the gaseous heat transmission medium, said lifting means
comprising a vertically disposed shaft arranged for continuous
rotation in one direction and at least one separate stirrer
attached to said shaft within each zone, each stirrer being spaced
from said shaft, having a helicoidal pitch, and being arranged so
that its downward edge is its leading edge as it rotates with said
shaft.
2. The apparatus according to claim 1 wherein each stirrer presents
a smooth surface toward the direction of material flow, said
surface being substantially straight in a radial direction from
said shaft.
3. An apparatus according to claim 2 wherein each stirrer is vane
shaped and rectangular in cross section.
4. An apparatus according to claim 1 wherein the edge of each
stirrer which encircles said shaft partially defines the surface of
a cylinder which is concentric with the rotational axis of said
shaft.
5. An apparatus according to claim 1 wherein the edge of each
stirrer which encircles said shaft partially defines the surface of
a truncated cone which is concentric with said shaft and which
tapers toward the top of said container.
6. An apparatus according to claim 5 wherein the outer edge of the
lower part of each stirrer substantially coincides with the inside
surface of said container.
7. An apparatus according to claim 1 wherein the width of each
stirrer is equal to more than 5 percent of the inside diameter of
said container and less than 25 percent of the inside diameter of
said container.
8. An apparatus according to claim 1 wherein the vertical pitch of
each stirrer is constant.
9. An apparatus according to claim 1 wherein the vertical pitch of
each stirrer decreases in an upward direction.
10. An apparatus according to claim 1 wherein the vertical pitch of
each stirrer decreases in a downward direction.
11. An apparatus according to claim 1 wherein the vertical pitch of
each stirrer varies from one part of said stirrer to another.
12. An apparatus according to claim 1 wherein the outer edge of
each stirrer partially defines the surface of a cylinder concentric
with said shaft and substantially coinciding with the inner surface
of said container.
13. An apparatus according to claim 1 wherein the upper surface of
each stirrer is inclined so that a point on its outer edge is in a
different horizontal plane from a corresponding point on its inner
edge.
14. An apparatus according to claim 21 wherein said shaft is
axially movable in a vertical direction within said container
whereby the stirrers can be caused to reciprocate.
Description
The object of the present invention is to provide a continuously
operating device having high efficiency with regard on the one hand
to the quantity per time unit and on the other hand to the heat
treatment of the treated material.
Another object of the invention is to provide a device in which
there is obtained an indulgent treatment of the material, which is
a very important requirement as otherwise heat-sensitive biological
tissue material easily is decomposed.
Still another object of the invention is to provide a device that
is easily cleaned which is an indispensable condition as the device
is used for heat treatment of biological material which is to be
consumed by human beings and by animals.
Further, the object of the device according to the invention is
that it should be used for many purposes such as boiling and
coagulating of the treated material by means of direct or for the
evaporation of volatile substances, which are chemically or
physically bonded to the material in question, by means of a direct
heating.
Hitherto, for such purposes devices have been used (see e.g., U.S.
Pat. Nos. 2,264,390 and 2,536,345), said devices comprising one or
several cylindrical containers provided with on the one hand a
mantle arranged about the container for indirect heating of the
container with its contents and on the other hand with a feeder
screw arranged in the interior of the container and provided with a
conveyor for the conveyance and stirring of the material. However,
these devices present considerable drawbacks for the reason that
the mantle surface of the container by the indirect heating must be
very hot if a high efficiency is to be obtained and thereby the
biological material which often is very sensitive, is exposed to
the risk of being decomposed. Moreover, there is not obtained an
even packing of the treated material over the whole area but the
material will be gathered towards the lower portion of the
container. Direct stream that may be introduced will thus pass over
the material and the close contact required between the material
and the steam is not obtained. Further, the risk increases for a
decomposition of sensitive material by means of the high contact
pressure against the lower portion of the container and thereby a
larger contact against the hot mantle surface.
Another known device (German "Auslegeschrift" No. 1,011,270 and
U.S. Pat. NO. 2,776,894) comprises a vertically arranged
cylindrical container provided with horizontal planes at mutual
distances. In this device where a zone is formed between two
planes, each plane is provided with an opening for connection to
the zones defining the zones. Further, arranged on a vertical shaft
mounted for rotation, there are, wings running along the upper
sides of the planes. These wings feed the material past the
openings through which the material falls down such that there is
obtained a conveyance of the material. The material is exposed to
heat treatment in counterflow by means of direct gas during the
conveyance from an upper plane to a lower plane, the gas being
introduced through openings arranged in each plane, these openings
being in connection with feeding conduits for the direct gas. This
device presents in the first hand the drawback that it is very
difficult to clean the same, which is a very important
inconvenience at the manufacture of products which are to be
consumed by human beings or animals. Further, there is not formed
any quite continuous bed of material but there is obtained a kind
of series treatment stations which further restricts the range of
use.
In another known construction (U.S. Pat. No. 2,806,298), the device
comprises a cylindrical, vertically arranged container provided
with a vertical shaft mounted for rotation, this shaft carrying
radially directed and helically arranged vanes of varying lengths.
This device presents the drawback that there is not obtained any
efficient feeding movement from the wall of the container such that
there occurs a lower heat transmission to the material. The device,
which is intended for a batchwise treatment of the material, is
constructed for a treatment of the material by means of
high-pressure steam which is injected in the container with an
important force and there is obtained a fluid bed.
Another known device (U.S. Pat. No. 3,075,298) comprises a
vertically arranged cylindrical container, which has a double
mantle and is provided with feeding and discharging devices for the
material. It is further provided with a vertical shaft mounted for
rotation and carrying radially arranged vanes inclining in relation
to the horizontal plane, said vanes shaped as sectors. The material
is heat treated in counterflow at a force conveyance from above and
downward by means of the inclining vanes and for the reason that
the inclining vanes are shaped as sectors there is obtained no open
center. There is thus no possibility for a treatment zone by zone
of the material with a radially directed displacement of the same
but the material is only vertically displaced along a helical path.
Thus, the material will not be loosened but instead be compressed.
Further, the device presents the drawback that certain material to
a great extent is stuck to the vanes such that the material is
exposed to a long heat treatment, whereat the same may be
decomposed. According to this sticking to the vanes the device is
further hard to clean and the material will for this reason form a
favorable surrounding for an undesired growth of bacteria.
The drawbacks explained in the aforegoing have been completely
eliminated by means of the device according to the present
invention which is characterized thereby that the shaft carries a
number of stirring devices arranged at a distance from the shaft,
said stirring devices having a vertical helicoidal pitch and being
adapted to treat the material zone by zone in vertical and
horizontal direction.
The stirrers present a smooth surface toward the direction of
material flow, this surface being substantially straight in a
radial direction from the shaft. The stirrers are preferably shaped
as blades or vanes having a rectangular cross section. For the
reason that the helical stirrers are plane, there is obtained a
better lifting surface and a better vertical displacement of the
material.
The helical stirrers should according to a preferred embodiment of
the invention operate in the direction opposite to the flow of
material.
By means of the described embodiments there is obtained a stirring
and homogeneous mixing of the material at every level defined by
the helical stirrers. Thereby the material is lifted by the
stirrers and moved against the center such that there is obtained
an efficient heat transmission.
According to another preferred embodiment the helical stirrers are
arranged such that they form at least one interrupted open
helix.
In the device according to the invention the lifting ability of the
stirrers should be essentially equal to the streaming through in
downward direction in the free area. The lifting force is thereat
depending on the width of the helical stirrers, their pitch and
speed.
According to a further embodiment the helical stirrers are arranged
to run along an imaginary cylindrical mantle surface being coaxial
to the shaft, the stirrers being preferably adapted to rotate in
the vicinity of the internal surface of the container and the
imaginary mantle surface will essentially coincide with the inner
surface of the container.
Further, the upper end portions of the helical stirrers may with
advantage be situated in one imaginary cylindrical mantle surface
and the lower end portions of the stirrers be situated in another
imaginary mantle surface, the imaginary mantle surfaces being
concentric to the shaft and present different radii and the lower
end portions of the stirrer are preferably adapted to rotate in the
vicinity of the inner surface of the container, the other mantle
surface preferably coinciding with the inner surface of the
container.
The upper surface of a stirrer may be inclined so that a point on
its outer edge is in a different horizontal plane from a
corresponding point on its inner edge.
As mentioned in the aforegoing the lifting force should be
essentially equal to the streaming through in the free area. Thus,
the width of the stirrer is one of the factors influencing the
lifting force and the stirrers, for this reason, preferably have a
width between 5 and 25 percent of the inner diameter of the
container.
In respect to the pitch of the stirrers it can be constant or vary
vary within each stirrer as well as the pitch can be different for
different stirrers arranged in different parts of the container.
The vertical pitch may decrease in an upward direction or in a
downward direction.
According to still a preferred embodiment of helical stirrers are
arranged on an axially displaceable shaft with a movement back and
forth.
The invention will now be described with reference to the
accompanying drawings. In the drawings:
FIG. 1 shows an axial section through a preferred embodiment of the
invention;
FIG. 2 shows a preferred embodiment in particular at a large
diameter of the container;
FIG. 3 shows an axial section through another preferred
embodiment;
FIG. 4 shows a section on the line IV--IV in FIG. 3;
FIG. 5 shows an axial section of a third embodiment of the
invention;
FIG. 6 shows a section on the line VI--VI in FIG. 5;
FIGS. 7 and 8 show embodiments similar to the one shown in FIGS. 5
and 6; and
FIGS. 9, 10, 11, and 12 show further embodiments of the
invention.
The embodiment of the device according to the invention shown in
FIG. 1 comprises a vertically arranged cylindrical container 1
provided with a mantle 2 for an indirect heating of the container
1. The heat quantity fed to the mantle is then adjusted for giving
the inner wall of the container the same temperature as the treated
material and such that only pure heat losses by means of radiation
and steam formation are compensated for. The mantle 2 is here
provided with a supply conduit 3 connected to the lower portion of
the container 1 and a discharge conduit 4 connected to the upper
portion of the container 1 for heating medium for heat transmission
the mantel, this medium may, e.g., comprise water steam. Further,
arranged at the top of the container 1 is a horizontally extending
feeding screw 5 with a stream mantle for feeding biological
material. The lower portion 6 of the container 1 is tapering
conically downward and a horizontally arranged discharge screw 7
with a steam mantle is connected to this conical portion 6 so as to
discharge the heat-treated biological material. The feeding and
discharging screws 5 and 7 are provided with a mantle in order that
the material either shall maintain a temperature already obtained
or for an addition of heat such that direct steam does not have to
be fed in excess for a pure heating. In the lower portion of the
container 1 above the conical portion 6 there is arranged a feeding
conduit 8 for a gaseous heat transmission medium. The feeding
conduit 8 is preferably connected to a distribution means 9
comprising for instance two tubes crossing each other and provided
with a number of apertures 10 to give an even distribution of the
gaseous heat transmission medium. At the upper end of the container
1 there is, above the feeding screw 5, further arranged a conduit
11 for the discharge of the gaseous heat transmission medium. The
conduit 11 is then with advantage connected to a heat exchanger 12
taking the shape, e.g., of a condenser for cooling the heat
transmission medium. Further a vertical shaft 13 mounted for
rotation is arranged in the container 1 and the axis of the shaft
13 coincides with the central axis of the container 1. The shaft 13
carries at a distance from the same helical stirrers 14 arranged
along the inside of the container 1, each stirrer 14 presenting a
vertical helicoidal pitch. The pitch of the stirrers 14 is in this
embodiment shaped in such a way and the stirrers 14 arranged in
such a way that they form an open helix having interruptions at
certain intervals. The helical stirrers 14 are in this embodiment
attached to the shaft 13 by means of stays 15 which are arranged
about the shaft with an angular distance of 90.degree.. The helical
stirrers 14 are in this case arranged such that they form a
complete turn about the shaft 13 whereupon an opening corresponding
to a quarter of a turn is arranged before the beginning of the
subsequent helical stirrer. By means of a motor, not shown, the
shaft 13 is brought to rotate such that the helical stirrers tend
to lift the material fed to the container 1.
Level sensors 16 are arranged below the mouth of the feeding screw
5 in the container 1, these level sensors having for their object
to control the feeding of the material to the container such that a
rather constant material quantity all the time is contained in the
container during a continuous operation. Further, an inspection
window 17 is arranged in the wall of the container to allow a
visual inspection.
Temperature and pressure indicators 18 are arranged at different
levels to control the feeding of the gaseous heat transmission
medium.
Feeding conduits 19 are arranged at different distances from the
feeding conduit 8 along the container 1 through which conduits more
gaseous heat transmission medium can be fed at need.
At large diameters of the container 1 it might be advisable, as
shown in FIG. 2, to arrange the helical stirrers 14, such that some
of them run along the inner surface of the container 1 and such
that the rest run along an imaginary mantle surface 21, which has a
diameter that is smaller than the radius of the container 1. In the
embodiments of FIGS. 1 and 2, the edge of the stirrers 13 and 14
which encircle the shaft 13 partially define the surface of a
cylinder which is concentric with the rotational axis of the shaft
13. Also in this case the helical stirrers 14 should be arranged in
such a way that all of them at their rotation lift the material fed
to the container 1. In this embodiment it is advisable that the
outer as well as the inner helical stirrers have the same pitch,
i.e., such that the pitch measured in meters will be the same for
the outer as well as the inner helical stirrers.
The FIGS. 3 and 4 show another embodiment of the invention
according to the invention in which the helical stirrers 14 as a
difference to the embodiment shown in FIG. 1 do not run along a
cylindrical surface having its center in the center of the shaft 13
but run along and partially define the surface of an imaginary
truncated cone tapering towards the top of the container 1, the
center axis of this cone coinciding with the rotating shaft 13.
This could also be explained in such a way that the upper
limitation of the helical stirrers 14 runs along an imaginary
cylindrical mantle surface 20, which has a smaller radius than the
cylindrical mantle surface along which the lower end portion of the
helical stirrers 14 runs. In a corresponding way the helical
stirrer 14 may with its lower end portion run along a cylindrical
mantle surface, which has a smaller radius than the imaginary
cylindrical mantle surface, along which the upper end portion of
the helical stirrer 14 runs.
As obvious from the FIGS. 5 and 6, the container 1 is provided with
two shafts 13 mounted for rotation, the helical stirrers 14 then
being arranged at a distance from their respective shafts. However,
if the cylinder 1 is cylindrical, a large part of the cross section
will be situated outside the operation area of the helical stirrers
14. For this reason it might be advisable to shape the container
with an oblong cross section, which has been indicated in FIG. 5 by
means of a phantom line which gives a better correspondence between
the container 1 and the operation area of the helical stirrers. It
might in certain cases also be advisable further to adjust the
cross section of the container 1 to the operation area of the
helical stirrers 14 as indicated by means of the dash-and-dot line
in FIG. 6. According to this embodiment the shafts 13 may rotate in
the same or in opposite directions. However, the helical stirrers
14 should always be arranged in such a way that they, at the
rotation, lift the material fed to the container 1.
It is further obvious from FIGS. 7 and 8 that more than two shafts
13 may be arranged in the container. It might then be preferred to
arrange the shaft such that they can be rotated to describe a
circular path such that all the material in the container is
influenced by the rotating stirrers.
In the embodiment shown in FIG. 9 the helical stirrers 14 are
displaced in relation to each other such that they work within the
operation area or level of the neighboring stirrer.
Of course, it might also be advisable, in certain cases, to arrange
the stirrers with larger mutual distances such that there is
obtained an untouched layer between each level of mixing and
loosening.
The stirrers 14 may be constructed as shown in FIG. 10 so that the
pitch decreases in an upward direction, or as shown in FIG. 11 so
that the pitch decreases in a downward direction. Another
arrangement is illustrated in FIG. 12 in which the surface 22 of
the stirrer 14 is inclined so that a point 23 on its outer edge is
in a different horizontal plane from a point 24 on its inner
edge.
So as further to lift and thus to loosen the biological material
during the heat treatment the shaft or the shafts may be adapted to
be axially displaced. They may then be mounted, e.g., in such a way
that they after a rotation of one revolution have completed one or
several movements up and down.
In certain cases it may of course also be advisable to arrange the
helical stirrers such that they have different rotation speeds in
relation to each other. One may then arrange the stirrers on two
concentric shafts which are rotated with different speeds or
arrange some helical stirrers on the inner side of the container
and some on the shaft, the container then being rotated with one
speed and the shaft with another speed.
Due to the fact that the helical stirrers are arranged at a
distance from the shaft there is obtained a device at which it is
very easy to remove residues of the material such that an undesired
bacteria growth is prevented. The open center of the device about
each shaft contributes to the easiness of access to each stirrer at
the cleaning.
The embodiment described in the aforegoing according to FIG. 1 will
in the following be described with respect to its way of operation
at some different ranges of use but it is of course in no way
limited thereto.
EXAMPLE 1
A fish material, which has been extracted in an extraction plant
(not shown) with sec-butanol is, after a primary separation of the
solvent by means of a centrifugation fed into the upper end of the
container 1 by means of the horizontally arranged feeding screw 5.
The protein material, which contains 45 percent dry substance, 40
percent water and 15 percent solvent is humid but not dripping. Due
to the fact that the container 1, which has a diameter of 300
millimeters and an effective height of 2.5 meters, is open about
the center, it is readily filled with the material. Direct steam is
then introduced on the one hand through the conduit 3 to the mantle
2 for indirect heating of the container 1 and the material and on
the other hand through the conduit 8, the distribution means 9 and
the openings 10 to the interior of the container 1 for direct
heating of the material. When the direct steam entered into the
container 1 contacts the protein material a part of the steam will
condense and at the same time the solvent present in the protein
material will evaporate and be brought along by the remaining steam
flow. The upwards streaming mixture of solvent and steam will at
optimal conditions, i.e., with correctly added steam quantity in
relation to the quantity of solvent in the protein material, only
after a short passage through the protein material, comprise the
azeotropic mixture of solvent and water steam. Repeated
condensation and evaporation of the solvent-water steam will occur
in all the protein material in the container. The protein material
will thus serve as filler bodies in a destillation column. When the
azeotropic steam mixture leaves the protein material, it is fed via
the conduit 11 to the heat exchanger 12 taking the shape of a
condenser, where it is condensed. As the solvent has been removed
from protein material by means of the heat treatment the protein is
conveyed away from the container 1 by means of the horizontally
arranged discharge screw 7 connected to the conical part 6, to a
drier plant, not shown. By means of this discharge the protein
material will move continuously downward in the container 1 under
the influence of the gravity. Said distillation effect will then be
reinforced thereby that a recirculation is created by means of the
movement downwards of the protein material.
Simultaneously with the feeding of the protein material into the
container 1 by means of the feeding screw 5, the shaft 13 mounted
for rotation is started and is given such a rotation that the
helical stirrers 14 arranged on the shaft 13 tend to lift the
protein material fed to the container 1. The stirring speed may
then be varied but should not exceed 45 revolutions per minute. The
width of the stirrers is 30 millimeters and they are arranged at a
distance of about say 5 millimeters from the inner surface of the
container. Further, the pitch of the stirrers is 200 millimeters
per revolution.
Due to the fact that the stirrers 14 are not arranged such that
they form a continuous path they will operate within a defined area
or within a defined level. For the reason that they operate
opposite to the movement direction of the material, there will
further be obtained a lifting and thus also a loosening of the
protein material within several defined levels and thereby that the
protein material is lifted from the periphery and is moved inward
and toward the center and returned towards the periphery there is
prevented a channel formation in the material bed. For the reason
that the area closest to the shaft is open, the material closest to
the shaft is forced to participate in the horizontal, essentially
radial displacement within the material. Thereby, there takes place
a continuous material exchange along the side of the container 1
such that there is prevented a channel formation due to a material
shrinking by means of solvent removal also along this side. For the
reason that the helical stirrers 14 give this lifting and
conveyance towards the center at each level, there does not occur
any total mixing in the whole of the container 1 but only a
homogenization within the level. It is thereby obtained a
concentration gradient of the mixture of solvent and steam such
that a material completely free from solvent can be discharged from
the container.
During the heat treatment and the homogenization and as the protein
material is conveyed away the level sensors 16 indicate the highest
point of the material bed such that when the highest point of the
material bed reaches the lower level sensor 16a, the feeding screw
5 is started whereby new material is fed to the container. When the
highest point of the material bed reaches the upper level sensor
16b, the feeding of protein material is stopped. Thus, it is hereby
possible to have a constant quantity of material in the container
1, which renders continuous process possible.
Further, in order to insure that a material completely freed from
solvent leaves the container 1, it is possible to adjust the
addition of direct steam by means of impulses from a temperature
and/or pressure indicator at different levels within the material
bed. The steam addition can then be adjusted in such a way that a
pressure compensated temperature of 100.degree. C., i.e., a
material completely freed from solvent, is present in the container
1 at a suitable level above the feeding place 9 for the direct
steam and the discharge screw 6 for the material.
In order further to increase the distillation effect, it is
possible to introduce, through the secondary feeding conduits 19
arranged at different levels, a mixture of solvent and steam with a
composition corresponding to the mixture of solvent and steam at
the actual level in the material bed.
The humid protein material discharged from the container at a rate
of 400 kilograms per hour, which by means of heat has been freed
from solvent, contains only 100 p.p.m. solvent, i.e., 100
milligrams solvent per kilogram of discharged humid protein
material, which at the feeding to the container contained up to 15
percent solvent. One hundred p.p.m. solvent in humid material means
then that the solvent residue is only 40 p.p.m. when the material
has been dried. Thus, an efficient solvent removal has been
obtained by means of the use of the process described.
EXAMPLE 2
Also this test had reference to the removal of solvent from
extracted fish material. Fishmeal extracted by means of isopropanol
in which the proportions were 65 percent dry substance and 15
percent water and 20 percent solvent was fed to the container. The
heat treatment was carried out in the same way as in Example 1.
The humid fish protein freed from solvent contained only 80 p.p.m.
solvent, which when the fish protein was dried gave a residual
content of 35 p.p.m.
In the Examples 1 and 2 hereabove it has been illustrated the
solvent removal of a protein material from fish but of course other
materials may be used, such as extracted soybean meal, rape,
cocoa.
The fish protein obtained according to Examples 1 and 2 had a good
quality and did not show any destruction, which is an indication of
that an indulgent treatment is obtained at a solvent removal in the
device according to the invention.
The device according to FIG. 1 was in the following example used as
a boiler and biological material, such as fish, animal muscle
tissue or cellulose material was heat treated by means of direct
steam.
EXAMPLE 3
In this case fresh fish was fed in the same way as in Example 1
into the container 1 while direct steam was fed in counterflow to
the material flow. By means of the shaft 13 arranged in the
container 1 and provided with the stirrers 14, there is obtained a
complete mixing and homogenization at every level such that a
complete boiling of the material is obtained thereby that the steam
is forced to pass through and brought to close contact with the
material fed therein. The continuity at the feeding and the
discharge is obtained in the same way as in the Example 1, and also
in this case it is obtained, by means of the pressure and
temperature indicators, a completion of the boiling before the
material leaves the container 1 via the discharge screw 7.
The material discharged from the container in the above Example 3
is completely boiled. There has been obtained by means of the
boiling a complete denaturation of the protein of the fish such
that the protein has been given a suitable form for further
treatment such as extraction. The material obtained did not show
any tendency for destruction.
The fish protein obtained in Examples 1 and 2 has by means of the
heat treatment carried out been deodorized. Amines hard to condense
have been removed from the material. There are of course other
methods of deodorizing animal material. It is, e.g., suitable to
use a mixture of ethanol and water in gaseous form for this
deodorization.
EXAMPLE 4
In order to deodorize fish protein which contains amines that are
hard to condensate, the material was inserted through the feeding
screw 5 into the container 1 in the same way as in Example 1.
However, instead of introducing only direct steam through the
distributor 9, there was introduced a gaseous mixture of ethanol
and water (95/5 ). For the rest, the material was treated in the
same way as in Example 1. By means of the helical stirrers 14
arranged on the shaft 13, there is obtained at the rotation of the
shaft, a complete mixing and homogenization at each level such that
the introduced steam mixture of ethanol and water is brought to
contact all the material and there is achieved a complete
deodorization thereby that the amines having a bad smell are
removed. The continuity of the feeding and the discharge is
obtained in the same way as in Example 1. By use of the device
described there is obtained a fish protein free from smell as freed
from amines of bad smell.
The examples here above have been described with reference to the
device shown in FIG. 1 but treatments according to the examples can
be carried through by means of the embodiments of the invention
shown in FIGS. 2-9. The use of the latter is merely depending on
the rate per time unit required from the device, which is obtained
by means of the increased area of the container.
The devices described in the foregoing may operate also at negative
pressure when a very heat-sensitive material is to be freed from
solvent or to be deodorized. Also a boiling may be carried out at a
lower pressure and temperature but in such a case the temperature
for a coagulation is to be maintained in case a coagulation is
necessary for the continued treatment of the material.
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