US2819190A - Counter-current diffusion tower - Google Patents

Counter-current diffusion tower Download PDF

Info

Publication number
US2819190A
US2819190A US343167A US34316753A US2819190A US 2819190 A US2819190 A US 2819190A US 343167 A US343167 A US 343167A US 34316753 A US34316753 A US 34316753A US 2819190 A US2819190 A US 2819190A
Authority
US
United States
Prior art keywords
tower
chips
extraction
screw conveyor
height
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Lifetime
Application number
US343167A
Inventor
Kather Willy
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
BMA Braunschweigische Maschinenbauanstalt AG
Original Assignee
BMA Braunschweigische Maschinenbauanstalt AG
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by BMA Braunschweigische Maschinenbauanstalt AG filed Critical BMA Braunschweigische Maschinenbauanstalt AG
Application granted granted Critical
Publication of US2819190A publication Critical patent/US2819190A/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Images

Classifications

    • CCHEMISTRY; METALLURGY
    • C13SUGAR INDUSTRY
    • C13BPRODUCTION OF SUCROSE; APPARATUS SPECIALLY ADAPTED THEREFOR
    • C13B10/00Production of sugar juices
    • C13B10/08Extraction of sugar from sugar beet with water
    • C13B10/10Continuous processes
    • C13B10/102Continuous processes having rotatable means for agitation or transportation

Definitions

  • the manner of charging and conducting the chips may vary; outside screw conveyors are being used which are located at the periphery of the towers and lead into the lower portion thereof; the screw conveyors may also be housed in a tube located in the tower, the materials to be extracted being fed into the upper portion of the tower and transported through the same in a downward direction; thereupon, the traveling direction is reversed and the charge is conducted in the operative sphere of a counter-currently operative main conveyor.
  • Methods are also known, where the charge to be extracted is pumped into the lower portion of the tower and supplied into the operative range of a screw conveyor effecting the upward travel thereof.
  • retarders are in most cases vertical plates fastened to the inner wall of the tower and radially extending into its inner space; a plurality of superposed retarders is generally provided.
  • the retarders extend vertically through the entire height of the spaces between the individual sections or portions of the interrupted screw conveyors and it is the general belief that these retarders, if distributed along the inner face of the tower, effect an upward transport of the chips in the form of coherent bodies or packages.
  • This package-type transport of the chips was considered to be necessary as it is assumed that in this manner the downflowing extraction liquid would be distributed over the cross section of the chip packages or bodies, that the same, therefore, would be uniformly passed-through by the liquid and that all chips contained in the packages would be contacted by the liquid.
  • the retarder plates located in the spaces between two successive screw conveyor portions or threads were converted by the increased rotational speed into vertebral elements, whereby the chips between the individual screw threads were energeticallyacted upon, agitated, and simultaneously circularly and axially displaced.
  • the space between two adjacent screw conveyor threads is incompletely filled.
  • the degree of this height reduction will depend upon the nature and particular properties of the chips; the reduced height of the retarder plates should preferably vary between about one fourth and three fourths of the smallest height between the successive screw conveyor sections.
  • the height of the retarder plates should be increased.
  • the retarder plates height variable may, for instance, be realized by making the retarder plates rotatable about a horizontal axis; by the rotation of these retarder plates about their horizontal axis the vertical height will vary.
  • the retarders may also be shaped to act as swivellers by making the same swingable about a horizontal axis; it is interesting to note that the retarding action exerted upon the upwardly moved chips was not handicapped or interfered with by the movement of the retarders, Whereas, as already stated above, the diffusion and washing efliciency was greatly improved.
  • At least four retarders are provided.
  • the length of the individual retarders in the radial direction of the tower may vary.
  • the above recited measures serve to greatly increase the turbulence of the comminuted chips in the individual superposed transporting zones.
  • Fig. 1 is a vertical sectional view of a diffusion tower for the extraction of sugar beet chips in conformity with the invention
  • Pig. 2 is a perspective view of a retarder plate applied to the inner face of the tower.
  • the charge such as particularly comminuted sugar beet chips is upwardly moved in the tower 1 in anopposite direction to the downflowing extraction fluid.
  • the lifting of the charge is effected by an interrupted or subdivided screw conveyor provided with superposed groups of. vanes 3, 4, 5.
  • vertical flow retarder plates 6 are disposed between individual conveyor screws or portions, which extend throughout the entire height of the spaces between these conveyor screws and are fixed to the inner wall. of the tower.
  • the retarders 7 constructed. in. conformity with the invention only extend through a portion of the. spaces or the height between two conveyor screw sections; consequently, the charge is enabled to move and to rotate: independently relative to the action of the retarder plates 7.
  • the invention as explained before, therefore, utilizes this important action of the retarder plates at the same time eliminating their disadvantages.
  • the retarders or damming plates. 7 may be fixed to the tower for a rotation about their horizontal axis 8, 9, see Fig. 2, by a motor 10.
  • the rotatable plates 7 may be fastenedv to the tower in any desired also inclined position.
  • the invention is not only successfully applicable to the extraction of sugar beet chips but also. well usable for a washing and particularly cellulose washing action.
  • An extraction tower for comminuted vegetable matter and particularly for sugar beet chips comprising a center shaft, an interrupted screw conveyor subdivided by said shaft into superposed sections, said sections defining vertically superposed free spaces between adjacent threads thereof, said threads serving to transport the charge of said chips upwardly, means to conduct a leaching fluid in opposite direction to the upwardly moved charge, radially extending vertical fiat flow retarder plates connected to the tower in said spaces having a height which is less than the smallest distance between two suecessive screw conveyor threads, said retarder plates being adapted to rotate.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Biochemistry (AREA)
  • Organic Chemistry (AREA)
  • Screw Conveyors (AREA)
  • Apparatuses For Bulk Treatment Of Fruits And Vegetables And Apparatuses For Preparing Feeds (AREA)

Description

Jan. 7, 1958 w. KATHER 2,819,190
COUNTER-CURRENT DIFFUSION TOWER Filed March 18, 195.3
e, 9 I" i I" l 7 I I 6 l al n INVENTOR: WILLY KATHER,
Mp w
United States Patent COUNTER-CURRENT DIFFUSION TOWER Willy Kiither, Braunschweig, Germany, assignor toBraunschweigische Maschinenbauanstalt, Braunschweig, Germany, and Pfeifer & Langen, Koln, Germany Application March 18, 1953, Serial No. 343,167 Claims priority, application Germany November 18, 1952 3 Claims. (Cl. 127-7) These vertical towers are circularly shaped; the mateu rials to be extracted are conducted through these towers in anupward direction, whereas the extraction fluid flows in an opposite downward direction.
The manner of charging and conducting the chips may vary; outside screw conveyors are being used which are located at the periphery of the towers and lead into the lower portion thereof; the screw conveyors may also be housed in a tube located in the tower, the materials to be extracted being fed into the upper portion of the tower and transported through the same in a downward direction; thereupon, the traveling direction is reversed and the charge is conducted in the operative sphere of a counter-currently operative main conveyor.
Methods are also known, where the charge to be extracted is pumped into the lower portion of the tower and supplied into the operative range of a screw conveyor effecting the upward travel thereof.
A particular difiiculty prevails with regard to the operation of these extraction towers which is caused by the maintenance of a constant all-over surface contact of the charge components during its upward travel with the downflowing extraction fluid.
It is presently the general belief of the art that this important problem may be satisfactorily solved by subdividing the screw conveyor into interrupted separate parts and by locating flow retarders in the spaces or interstices between these individual conveyor parts or sections.
These retarders are in most cases vertical plates fastened to the inner wall of the tower and radially extending into its inner space; a plurality of superposed retarders is generally provided. The retarders extend vertically through the entire height of the spaces between the individual sections or portions of the interrupted screw conveyors and it is the general belief that these retarders, if distributed along the inner face of the tower, effect an upward transport of the chips in the form of coherent bodies or packages. This package-type transport of the chips was considered to be necessary as it is assumed that in this manner the downflowing extraction liquid would be distributed over the cross section of the chip packages or bodies, that the same, therefore, would be uniformly passed-through by the liquid and that all chips contained in the packages would be contacted by the liquid.
Extensive observation has indeed proven that the package" transport of the chips, whereby the packages completely fill the vertical spaces between the screw conveyor portions, advantageously influence the extraction and the diffusion capacity of the towers.
However, in accordance with experience made by the inventor a great disadvantage of this measure prevails 2,819,190 Patented Jan. 7, 1958 insofar as it is impossible to control the density and resistive capacity of these chip packages, to cause them to pass through the tower with a constant uniform speed and remain permeable by the liquid solvent. During the transport of these chip packages through the tower fre- .quent cloggings and stoppages occur, which cause a great pressure increase in the interior of the packages. The .cause of these difficulties has never been ascertained.
Investigations carried-outby the inventor resulted in the following entirely novel and surprising recognition. It was found that the hitherto customary practice of transporting the chip packages or chip bodies through the extraction at the usual small rotary speed of the screw conveyor greatly restricts the leaching efliciency and operative capacity of the towers. Moreover, the surprising fact was ascertained by the inventor that a height reduction of the retarder plates eventually in combination with an increase of the rotational speed of the screw conveyor causes a surprising change of the working conditions. Therefore, in conformity with the invention the height of the retarder plates is kept smaller than the smallest distance between two directly superposed screw conveyor threads. 1
The retarder plates located in the spaces between two successive screw conveyor portions or threads were converted by the increased rotational speed into vertebral elements, whereby the chips between the individual screw threads were energeticallyacted upon, agitated, and simultaneously circularly and axially displaced.
Due to the height reduction of the retarder plates the space between two adjacent screw conveyor threads is incompletely filled. The degree of this height reduction .will depend upon the nature and particular properties of the chips; the reduced height of the retarder plates should preferably vary between about one fourth and three fourths of the smallest height between the successive screw conveyor sections.
If very finely divided chips are treated the height of the retarder plates should be increased.
Since the size of the chips often varies it is advisable to make the retarder plates height variable. This object may, for instance, be realized by making the retarder plates rotatable about a horizontal axis; by the rotation of these retarder plates about their horizontal axis the vertical height will vary.
The retarders may also be shaped to act as swivellers by making the same swingable about a horizontal axis; it is interesting to note that the retarding action exerted upon the upwardly moved chips was not handicapped or interfered with by the movement of the retarders, Whereas, as already stated above, the diffusion and washing efliciency was greatly improved.
In the known chip extraction towers having vertical .fiow retarding or damming plates vertically extending throughout the full height of the spaces between two conveyor screw sections the rotational speed of the screw conveyor is adjusted to a 0.6 to 1.3 rotations per minute. In conformity with the invention the rotational speed amounts to between above 1.3 and up to 6 rotations per minute.
In order to further improve the extraction at least four retarders are provided. The length of the individual retarders in the radial direction of the tower may vary.
The above recited measures serve to greatly increase the turbulence of the comminuted chips in the individual superposed transporting zones.
It was found that by the application of the invention the extraction losses of sugar are reduced to about 50 per cent at an equal discharge rate of the extraction fluid.
The invention will now be described more in detail and with reference to the attached drawing.
in the drawing:
Fig. 1 is a vertical sectional view of a diffusion tower for the extraction of sugar beet chips in conformity with the invention, and
Pig. 2 is a perspective view of a retarder plate applied to the inner face of the tower.
The charge such as particularly comminuted sugar beet chips is upwardly moved in the tower 1 in anopposite direction to the downflowing extraction fluid.
The lifting of the charge is effected by an interrupted or subdivided screw conveyor provided with superposed groups of. vanes 3, 4, 5.
In the hitherto customary extraction towers vertical flow retarder plates 6 are disposed between individual conveyor screws or portions, which extend throughout the entire height of the spaces between these conveyor screws and are fixed to the inner wall. of the tower. The retarders 7 constructed. in. conformity with the invention only extend through a portion of the. spaces or the height between two conveyor screw sections; consequently, the charge is enabled to move and to rotate: independently relative to the action of the retarder plates 7. The invention, as explained before, therefore, utilizes this important action of the retarder plates at the same time eliminating their disadvantages.
The retarders or damming plates. 7 may be fixed to the tower for a rotation about their horizontal axis 8, 9, see Fig. 2, by a motor 10.
The rotatable plates 7 may be fastenedv to the tower in any desired also inclined position.
The invention is not only successfully applicable to the extraction of sugar beet chips but also. well usable for a washing and particularly cellulose washing action.
Since certain changes in carrying out the above process could be made without departing from the scope thereof, it is intended that all matter contained in the above description or shown in the accompanying drawing shall be interpreted as illustrative and not in a limiting sense.
What I claim is:
1. An extraction tower for comminuted vegetable matter and particularly for sugar beet chips comprising a center shaft, an interrupted screw conveyor subdivided by said shaft into superposed sections, said sections defining vertically superposed free spaces between adjacent threads thereof, said threads serving to transport the charge of said chips upwardly, means to conduct a leaching fluid in opposite direction to the upwardly moved charge, radially extending vertical fiat flow retarder plates connected to the tower in said spaces having a height which is less than the smallest distance between two suecessive screw conveyor threads, said retarder plates being adapted to rotate.
2. In an extraction tower according to claim 1, means for driving the screw conveyor at a rate of 1.3 to 6 rotations of the screw conveyor per minute.
3. In an extraction tower according toclaim 1, means for vertically adjusting said retarder plates to vary their operative heights.
References Cited in the file of this patent UNITED STATES PATENTS

Claims (1)

1. AN EXTRACTION TOWER FOR COMMINUTED VEGETABLE MATTER AND PARTICULARLY FOR SUGAR BEET CHIPS COMPRISING A CENTER SHAFT, AN INTERRUPTED SCREW CONVEYOR SUBDIVIDED BY SAID SHAFT INTO SUPERPOSED SECTIONS, SAID SECTIONS DEFINING VERTICALLY SUPERPOSED FREE SPACES BETWEEN ADJACENT THREADS THEREOF, SAID THREADS SERVING TO TRANSPORT THE CHARGE OF SAID CHIPS UPWARDLY, MEANS TO CONDUCT A LEACH-
US343167A 1952-11-18 1953-03-18 Counter-current diffusion tower Expired - Lifetime US2819190A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
DE2819190X 1952-11-18

Publications (1)

Publication Number Publication Date
US2819190A true US2819190A (en) 1958-01-07

Family

ID=7999004

Family Applications (1)

Application Number Title Priority Date Filing Date
US343167A Expired - Lifetime US2819190A (en) 1952-11-18 1953-03-18 Counter-current diffusion tower

Country Status (1)

Country Link
US (1) US2819190A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2928760A (en) * 1953-12-08 1960-03-15 Christoffersen Hans Jacob Apparatus for continuous lixiviation
US3953224A (en) * 1974-03-16 1976-04-27 Braunschweigische Maschinenbauanstalt Extraction tower for sugar beets cossettes or crushed sugar cane
US3970469A (en) * 1974-11-30 1976-07-20 Braunschweigische Maschinenbauanstalt Extraction tower
US4154798A (en) * 1976-04-09 1979-05-15 Luwa Ag Apparatus for producing a homogeneous, chemically reactive system

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1971632A (en) * 1930-09-15 1934-08-28 Anderson Co V D Feeding mechanism for presses
US2637666A (en) * 1949-07-01 1953-05-05 Langen Eugen Extraction tower for comminuted material of vegetable or plant origin, particularly sugar beets

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1971632A (en) * 1930-09-15 1934-08-28 Anderson Co V D Feeding mechanism for presses
US2637666A (en) * 1949-07-01 1953-05-05 Langen Eugen Extraction tower for comminuted material of vegetable or plant origin, particularly sugar beets

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2928760A (en) * 1953-12-08 1960-03-15 Christoffersen Hans Jacob Apparatus for continuous lixiviation
US3953224A (en) * 1974-03-16 1976-04-27 Braunschweigische Maschinenbauanstalt Extraction tower for sugar beets cossettes or crushed sugar cane
US3970469A (en) * 1974-11-30 1976-07-20 Braunschweigische Maschinenbauanstalt Extraction tower
US4154798A (en) * 1976-04-09 1979-05-15 Luwa Ag Apparatus for producing a homogeneous, chemically reactive system

Similar Documents

Publication Publication Date Title
US2337137A (en) Apparatus for the treatment of solid materials with liquids
US1956293A (en) Process of and apparatus for producing liquid dispersions
US2819190A (en) Counter-current diffusion tower
US2637666A (en) Extraction tower for comminuted material of vegetable or plant origin, particularly sugar beets
US1569778A (en) Continuous automatic separator
US2390388A (en) Method and apparatus for solvent extraction
US2557629A (en) Method and apparatus for continuous centrifugal separation
US3519130A (en) Apparatus for classifying of finegrained solids in wet condition
US1991490A (en) Centrifugal separation
US3155697A (en) Continuous countercurrent process for the transition of substances between a liquid and a solid phase
US1139825A (en) Method of treating mixtures of liquids and solids.
US1996547A (en) Separator and method
US3111490A (en) Centrifuge machine
US1046447A (en) Apparatus for separating materials of different specific gravity.
US2428789A (en) Spiral conveyor classifier
DE1432809A1 (en) Sieve centrifuge, especially sugar centrifuge
US3821857A (en) Continuous drying of solid particles
US3881876A (en) Apparatus for sink-float liquid contacting of solids
US1650685A (en) Process and apparatus for separating liquids from solids
US3794521A (en) Diffusion tower
US3245542A (en) Centrifuge having perforate frusto-conical basket
US2742343A (en) Circulation of granular solids through a process system
US1609933A (en) Method of and apparatus for removing free moisture from substances
US2280895A (en) Apparatus and method for dispersing liquids
DE951140C (en) Sieve centrifuge for removing liquids from thick matter