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US1345657A - Method of crystallizing margarin - Google Patents

Method of crystallizing margarin Download PDF

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Publication number
US1345657A
US1345657A US159597A US15959717A US1345657A US 1345657 A US1345657 A US 1345657A US 159597 A US159597 A US 159597A US 15959717 A US15959717 A US 15959717A US 1345657 A US1345657 A US 1345657A
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Prior art keywords
margarin
emulsion
trough
cooling
water
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US159597A
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Zeuthen Anders Carl August
Larsen Martin
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    • AHUMAN NECESSITIES
    • A23FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23DEDIBLE OILS OR FATS, e.g. MARGARINES, SHORTENINGS OR COOKING OILS
    • A23D7/00Edible oil or fat compositions containing an aqueous phase, e.g. margarines
    • A23D7/02Edible oil or fat compositions containing an aqueous phase, e.g. margarines characterised by the production or working-up
    • A23D7/04Working-up
    • A23D7/05Working-up characterised by essential cooling

Definitions

  • the object of the invention is to decrease the quantity of water and the amount of cold required.
  • the invention is principally characterized in that the emulsion and the water are moved in relation to each other in such a manner that at the same time that each has its principal direction of movement, they are thoroughly mixed with each other, by the aid of mechanical means, and thus, while they pass the same, suitably long course, either in the same or opposite directions, or partly in thesame and partly in opposite directions, they perform other movements at several points in this course, owing to the influence ofthe mechanical means, the emulsion and the margarin thereby being subjected, in an effective manner, to the influence of the water and the cold.
  • the invention admits of indirect cooling, the emulsion being exposed to the. effect of mechanical stirring-members while it is being conducted through the aforesaid cooling course, where it is indirectly cooled.
  • the apparatus required for the performance of the invention is principally re stricted to a combination of an emulsor with a crystallizingor cooling course of the aforesaid kind, both functioning continuously, thus a plant considerably simpler than those generally used in margarin factories.
  • Figures 1, 2, and 3 show schematically, by way of example, a form of construction of the crystallization course of the aforesaid kind, in longitudinal section plan, and transverse section, respectively.
  • Figs. 47 are transverse sections through other forms of construction.
  • a trough 7 there is journaled a shaft 8 carrying a number of wings 9 and having an exterior drivingmember 10.
  • the trough is prolonged by an upwardslantlng pipe 11, or a spout, with one or more worms 12.
  • a water-supply 13 At this end of the trough there is a water-supply 13.
  • the emulsor 14 with the outlet 15 are disposed, and here, in the trough,
  • the emulsion from the outlet 15 When the emulsor is functioning, and the water is let on, the emulsion from the outlet 15 will thus flow down into a mass of water which moves in the direction of the lower arrow 17, and will itself move in the direction indicated by the upper arrow 18 toward the pipe or spout 11. taneously with the revolution of the wing-shaft 8, 9 and the worm 12, the emulsion and water in the trough 7 W111 be thoroughl mixed with each other. The warm emulsion from the outlet 15 will meet comparatively warm water, which is just about to flow out through the overflow pipe 16, while, as it proceeds, the emulsion meets colder and still colder water.
  • the separated margarin will here be kneaded and raised by the worm 12, and if, in the trough 7 or at some other point, there is added the necessary amount of salt, etc., the margarin will leave the apparatus at the mouth 19 in a finished condition.
  • the trough, and therewith the main direction of movement of the emulsion-and the water need not be straight, but may be ti -shaped, zig-zag, etc. llnstead of a single trough with a single wing-shaft, it is possible, as shown in Fig. 4, to use a double trough 7 and 70, with two shafts 8and 80, whose wings 9 and 90 mesh into each other.
  • the transverse section-profile of the trough may be varied in many difierent ways. It
  • Fig. 6 shows an example of a wing 9 in the shape of a circular, plane, or tortuous disk with a segment 20 cut out. One or more such disks may eventually be disposed between or alternating with the more open wings 9, according to Figs. 3-5, such an arrangement being shown at 9, hi s. l and 2.
  • this method is performed in such a manner that indirect cooling is entirely or partially used, either the trough may be furnished with cooling-jacket 21, Fig. 7 or the shaft and wings may be made hollow as at 22 and be connected with the pipecontaining the supply of cooling means, or both methods may be used simultaneously.
  • the apparatus used for kneading the margarin may, of course, be of any other suitable kind than that here shown.
  • a method of crystallizing margarin which consists in causing the emulsion and a cooling agent to travel through a common course and transversely moving the emulsion and cooling agent relative to each other during such travel.
  • a method of crystalli'zing margarin by means of cooling the emulsion with a cooling fluid characterized in that the emulsion and the cooling fluid are moved in relation to each other in such manner that while they are running through the same course, one is by mechanical means also caused to perform transverse movements in relation to the other.
  • a method of crystallizing margarin by means of cooling the emulsion with a cooling fluid characterized in that the emulsion and the cooling fluid are moved in relation to each other in such manner that while they are running through the same course, one is by mechanical means also caused to perform transverse movements in relation to the other, the equalization of the temperature at every point of the course being as perfect as possible.
  • a method for crystallizing margarin by means of cooling of the emulsion with a coolingfluid characterized in that the emulsion and the cooling fluid are moved in relation to each other in such manner that while they are running in the same course in opposite directions, one is by mechanical meansalso caused to perform transverse movements in relation to the other.
  • a method for crystallizing margarin by means of cooling of the emulsion with a cooling fluid characterized in that the emulsion and the cooling fluid are moved in relation to each other in such a manner that while they are running through the same course, they are by mechanical means also caused to perform transverse movements in relation to each other.

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  • Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Food Science & Technology (AREA)
  • Polymers & Plastics (AREA)
  • Colloid Chemistry (AREA)

Description

A. C. A. ZEUTHEN AND M. LARSEN.
METHOD OF GRYSTALLIZING MARGAR|N.-
APPLIQATION FILED APR. 3. 191.7.
Patented July W240 If, l h fll 1111111.;
METHOD UT CEYSTALLIZTNG: MARGARIN.
leaner...
specification. of Letters Patent.
Patented ,nu e, react application filed April 3, 1917. serial No. 159,597.
To all whom it may concern:
Be it known that we, Animus CARL AU- oUsr ZEUTHEN and MARTIN LARSEN, subjects of the King of Denmark, residing at Silkeborg, in the Kingdom of Denmark, have invented certain new and useful Tmprovements in Methods of Crystallizing Margarin, of which the following is a specification.
According to the method generally used in margarin factories for separating (crystallizing) margarin, animal or vegetable, from the emulsion by means of direct or indirect cooling of the emulsion with water, and subsequent washing, comparatively great quantities of water of comparatively low temperature are required.
The object of the invention is to decrease the quantity of water and the amount of cold required. The invention is principally characterized in that the emulsion and the water are moved in relation to each other in such a manner that at the same time that each has its principal direction of movement, they are thoroughly mixed with each other, by the aid of mechanical means, and thus, while they pass the same, suitably long course, either in the same or opposite directions, or partly in thesame and partly in opposite directions, they perform other movements at several points in this course, owing to the influence ofthe mechanical means, the emulsion and the margarin thereby being subjected, in an effective manner, to the influence of the water and the cold.
llnstead of the here presupposed direct cooling, the invention admits of indirect cooling, the emulsion being exposed to the. effect of mechanical stirring-members while it is being conducted through the aforesaid cooling course, where it is indirectly cooled.
The apparatus required for the performance of the invention is principally re stricted to a combination of an emulsor with a crystallizingor cooling course of the aforesaid kind, both functioning continuously, thus a plant considerably simpler than those generally used in margarin factories.
In the drawing, Figures 1, 2, and 3 show schematically, by way of example, a form of construction of the crystallization course of the aforesaid kind, in longitudinal section plan, and transverse section, respectively. Figs. 47 are transverse sections through other forms of construction.
Tn a trough 7 there is journaled a shaft 8 carrying a number of wings 9 and having an exterior drivingmember 10. At one end the trough is prolonged by an upwardslantlng pipe 11, or a spout, with one or more worms 12. At this end of the trough there is a water-supply 13. At the opposite end of the trough the emulsor 14 with the outlet 15 are disposed, and here, in the trough,
there is disposed an overflow 16 for the water.
When the emulsor is functioning, and the water is let on, the emulsion from the outlet 15 will thus flow down into a mass of water which moves in the direction of the lower arrow 17, and will itself move in the direction indicated by the upper arrow 18 toward the pipe or spout 11. taneously with the revolution of the wing-shaft 8, 9 and the worm 12, the emulsion and water in the trough 7 W111 be thoroughl mixed with each other. The warm emulsion from the outlet 15 will meet comparatively warm water, which is just about to flow out through the overflow pipe 16, while, as it proceeds, the emulsion meets colder and still colder water. Owing to the function of the wing-shaft, there is the very best possible equalization of temperature in every transverse section of the trough, and, furthermore, the separation and washing of the margarin is promoted, so thatthe required uantity of water is' comparatively small. he wings 9 have such a shape that they work the mixture toward the watersupply, where the trough is open, the oblique plpe, or spout, 11 acting as water-lock.
The separated margarin will here be kneaded and raised by the worm 12, and if, in the trough 7 or at some other point, there is added the necessary amount of salt, etc., the margarin will leave the apparatus at the mouth 19 in a finished condition. The trough, and therewith the main direction of movement of the emulsion-and the water, need not be straight, but may be ti -shaped, zig-zag, etc. llnstead of a single trough with a single wing-shaft, it is possible, as shown in Fig. 4, to use a double trough 7 and 70, with two shafts 8and 80, whose wings 9 and 90 mesh into each other. The transverse section-profile of the trough may be varied in many difierent ways. It
may, f. -i., be circular, as shown in lFi 5, or it may be closed in some other way. y the term wings there may also be understood Simulportion of the transverse section of the trough, depending upon how much or how little it is desired to dam up the current of water. Fig. 6 shows an example of a wing 9 in the shape of a circular, plane, or tortuous disk with a segment 20 cut out. One or more such disks may eventually be disposed between or alternating with the more open wings 9, according to Figs. 3-5, such an arrangement being shown at 9, hi s. l and 2.
hen this method is performed in such a manner that indirect cooling is entirely or partially used, either the trough may be furnished with cooling-jacket 21, Fig. 7 or the shaft and wings may be made hollow as at 22 and be connected with the pipecontaining the supply of cooling means, or both methods may be used simultaneously. The apparatus used for kneading the margarin may, of course, be of any other suitable kind than that here shown.
We claim- 1. A method of crystallizing margarin, which consists in causing the emulsion and a cooling agent to travel through a common course and transversely moving the emulsion and cooling agent relative to each other during such travel.
2. A method of crystalli'zing margarin by means of cooling the emulsion with a cooling fluid, characterized in that the emulsion and the cooling fluid are moved in relation to each other in such manner that while they are running through the same course, one is by mechanical means also caused to perform transverse movements in relation to the other.
3. A method of crystallizing margarin by means of cooling the emulsion with a cooling fluid, characterized in that the emulsion and the cooling fluid are moved in relation to each other in such manner that while they are running through the same course, one is by mechanical means also caused to perform transverse movements in relation to the other, the equalization of the temperature at every point of the course being as perfect as possible. w
4:. A method for crystallizing margarin by means of cooling of the emulsion with a coolingfluid, characterized in that the emulsion and the cooling fluid are moved in relation to each other in such manner that while they are running in the same course in opposite directions, one is by mechanical meansalso caused to perform transverse movements in relation to the other.
5. A method for crystallizing margarin by means of cooling of the emulsion with a cooling fluid, characterized in that the emulsion and the cooling fluid are moved in relation to each other in such a manner that while they are running through the same course, they are by mechanical means also caused to perform transverse movements in relation to each other.
In testimony, that we claim the foregoing as our invention, we have signed our names in presence of two subscribing witnesses.
ANDERS CARL AUGUST ZEUTIIEN. MARTIN LARSEN. Witnesses:
P. HOFMAN BAUJ, ERNEST BOUTARD.
US159597A 1917-04-03 1917-04-03 Method of crystallizing margarin Expired - Lifetime US1345657A (en)

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Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2611707A (en) * 1948-04-01 1952-09-23 Lever Brothers Ltd Method and apparatus for manufacturing margarine
US4447463A (en) * 1982-11-19 1984-05-08 Land O'lakes, Inc. Process for producing a butter/margarine blend product
US4911553A (en) * 1986-11-28 1990-03-27 House Food Industrial Co., Ltd. Method and apparatus for feeding solid-liquid mixture
US20020090428A1 (en) * 2000-10-12 2002-07-11 Warf C. Cayce Treatment fluid application apparatus for foodstuffs and methods related thereto

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2611707A (en) * 1948-04-01 1952-09-23 Lever Brothers Ltd Method and apparatus for manufacturing margarine
US4447463A (en) * 1982-11-19 1984-05-08 Land O'lakes, Inc. Process for producing a butter/margarine blend product
US4911553A (en) * 1986-11-28 1990-03-27 House Food Industrial Co., Ltd. Method and apparatus for feeding solid-liquid mixture
US20020090428A1 (en) * 2000-10-12 2002-07-11 Warf C. Cayce Treatment fluid application apparatus for foodstuffs and methods related thereto
US20050058013A1 (en) * 2000-10-12 2005-03-17 Alcide Corporation Treatment fluid application apparatus for foodstuffs and methods related thereto

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