US3494275A - System for producing margarine - Google Patents
System for producing margarine Download PDFInfo
- Publication number
- US3494275A US3494275A US734439A US3494275DA US3494275A US 3494275 A US3494275 A US 3494275A US 734439 A US734439 A US 734439A US 3494275D A US3494275D A US 3494275DA US 3494275 A US3494275 A US 3494275A
- Authority
- US
- United States
- Prior art keywords
- margarine
- heat exchanger
- plate heat
- coolers
- emulsion
- 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
Links
- 235000013310 margarine Nutrition 0.000 title description 40
- 239000003264 margarine Substances 0.000 title description 39
- 238000004806 packaging method and process Methods 0.000 description 12
- 239000000839 emulsion Substances 0.000 description 7
- 238000002844 melting Methods 0.000 description 7
- 230000008018 melting Effects 0.000 description 7
- 239000007787 solid Substances 0.000 description 6
- 238000004519 manufacturing process Methods 0.000 description 5
- JVTAAEKCZFNVCJ-UHFFFAOYSA-N lactic acid Chemical compound CC(O)C(O)=O JVTAAEKCZFNVCJ-UHFFFAOYSA-N 0.000 description 4
- 238000010438 heat treatment Methods 0.000 description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 3
- 235000015844 Citrullus colocynthis Nutrition 0.000 description 2
- 240000000885 Citrullus colocynthis Species 0.000 description 2
- 238000002474 experimental method Methods 0.000 description 2
- 239000003925 fat Substances 0.000 description 2
- 235000019197 fats Nutrition 0.000 description 2
- 208000015181 infectious disease Diseases 0.000 description 2
- 235000014655 lactic acid Nutrition 0.000 description 2
- 239000004310 lactic acid Substances 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 230000003647 oxidation Effects 0.000 description 2
- 238000007254 oxidation reaction Methods 0.000 description 2
- 150000003839 salts Chemical class 0.000 description 2
- 235000002639 sodium chloride Nutrition 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 235000013343 vitamin Nutrition 0.000 description 2
- 229940088594 vitamin Drugs 0.000 description 2
- 229930003231 vitamin Natural products 0.000 description 2
- 239000011782 vitamin Substances 0.000 description 2
- SVUQHVRAGMNPLW-UHFFFAOYSA-N 2,3-dihydroxypropyl heptadecanoate Chemical compound CCCCCCCCCCCCCCCCC(=O)OCC(O)CO SVUQHVRAGMNPLW-UHFFFAOYSA-N 0.000 description 1
- RNAMYOYQYRYFQY-UHFFFAOYSA-N 2-(4,4-difluoropiperidin-1-yl)-6-methoxy-n-(1-propan-2-ylpiperidin-4-yl)-7-(3-pyrrolidin-1-ylpropoxy)quinazolin-4-amine Chemical compound N1=C(N2CCC(F)(F)CC2)N=C2C=C(OCCCN3CCCC3)C(OC)=CC2=C1NC1CCN(C(C)C)CC1 RNAMYOYQYRYFQY-UHFFFAOYSA-N 0.000 description 1
- 241001491130 Ochlerotatus hendersoni Species 0.000 description 1
- 238000005086 pumping Methods 0.000 description 1
- 239000002344 surface layer Substances 0.000 description 1
Images
Classifications
-
- A—HUMAN NECESSITIES
- A01—AGRICULTURE; FORESTRY; ANIMAL HUSBANDRY; HUNTING; TRAPPING; FISHING
- A01J—MANUFACTURE OF DAIRY PRODUCTS
- A01J21/00—Machines for forming slabs of butter, or the like
- A01J21/02—Machines for forming slabs of butter, or the like with extruding arrangements and cutting devices, with or without packing devices
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23D—EDIBLE OILS OR FATS, e.g. MARGARINES, SHORTENINGS OR COOKING OILS
- A23D7/00—Edible oil or fat compositions containing an aqueous phase, e.g. margarines
- A23D7/02—Edible oil or fat compositions containing an aqueous phase, e.g. margarines characterised by the production or working-up
Definitions
- the equipment heretofore used for melting and returning margarin by-passing the packaging machines has certain drawbacks.
- the margarine undergoing melting in the vessel is subjected not only to an undesired oxidation but also to rather great risks of infection, since this vessel is constantly open to the surrounding atmosphere.
- the principal object of the present invention is to eliminate these drawbacks, which have long been recognized in the art of margine production. This object is achieved by providing the system with means for returning through a closed path the margarine that is not immediately packed by the packaging machines, so that it will again pass through all or part of the system, the closed returning means comprising a pro-heater in the form of a tube heat exchanger, or the like, and a melting apparatus in the form of a plate heat exchanger.
- a plate heat exchanger is deemed to be the only kind of heat exchanger which could be considered for the above-noted purpose of melting the returning margarine.
- a plate heat exchanger is not easily adaptable for this purpose. It has proved quite impossible to introduce cold (that is, solid) margarine directly into a plate heat exchanger.
- water, fat, lactic acid, salts, vitamins, etc. are introduced at A. These substances are mixed in a conduit 1 to form an emulsion which passes through a non-return valve 2 to a pump 3 and thence through a plate heat exchanger 4. In the plate heat exchanger, the emulsion is heated to about 38 C. By means of a number of high pressure pumps 5, the emulsion is then pumped to a number of coolers 6 wherein finished margarine is formed. The margarine leaving the coolers 6 has a temperature of about 15 C. and is consequently in a solid state. From these coolers, the finished margarine is pumped by means of the high pressure pumps 5 to a number of packaging machines 7, from which it is normally discharged in packages at B.
- Conduits 8 are surrounded along part of their length by sleeve-like jackets 9 through which hot water is passed by way of suitable inlets and outlets (not shown). In its passage through each jacket 9, the margarine flowing through the corresponding conduit 8 is heated only at its surface layer. This is sufiicient for enabling the margarine to be introduced into a plate heat exchanger 10 without obstructions, the margarine being melted to a liquid state in the exchanger 10.
- the high pressure pumps 5 are used for pumping the margarine through conduits 8 as well as through plate heat exchanger 10.
- the margarine is returned to conduit 1 at the inlet side of pump 3 but at the outlet side of non-return valve 2. In this way, it is caused to flow again through plate heat exchanger 4 and coolers 6.
- the production process may go on continuously and, more particularly, in such a manner that margarine which cannot be packaged immediately, after having been cooled to a solid state, is returned to the production system in a liquid state without having come into contact with the surrounding atmosphere. Oxidation and infections are thereby prevented.
- connection leading from each cooler 6 is provided with a valve 6a operable to direct the solidified margarine selectively to either the corresponding packaging machine 7 or the corresponding return conduit 8.
- the plate heat exchanger 10 is shown with an inlet Illa and an outlet 10!; for the heating medium, whereby the latter flows through the heat exchanger in the same direction as the margarine from pre-heaters 9'.
- a margarine producing system comprising means for supplying an emulsion, a cooler connected to said supply means for solidifying the emulsion to form solid margarine, a machine for packaging solid margarine, and a connection between the cooler and the packaging machine for transmitting solid margarine to said machine, said system including a first closed flow path for the emulsion, means forming a second closed path leading from said connection for receiving margarine not immediately packaged by said machine and returning the unpackaged margarine to a point in said first closed flow path for passage again through at least part of the system, said closed return path including a pre-heater in the form of a tube heat exchanger and a melting apparatus in the form of a plate heat exchanger connected to receive margarine from the pre-heater.
Landscapes
- Life Sciences & Earth Sciences (AREA)
- Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Engineering & Computer Science (AREA)
- Food Science & Technology (AREA)
- Polymers & Plastics (AREA)
- Animal Husbandry (AREA)
- Environmental Sciences (AREA)
- Edible Oils And Fats (AREA)
- Fats And Perfumes (AREA)
- Packging For Living Organisms, Food Or Medicinal Products That Are Sensitive To Environmental Conditiond (AREA)
Description
Feb. 10, 1970 L. A. BONDESSON ETAL 3,494,275
SYSTEM FOR PRODUCING MARGARINE Filed June 4, 1968 I N VE N TORS United States Patent 3,494,275 SYSTEM FOR PRODUCING MARGARINE Lennart Adolf Bondesson, Bandhagen, and Hilding Sven Svensson, Tumba, Sweden, assignors to Alta-Laval AB, Tumba, Sweden, a corporation of Sweden Filed June 4, 1968, Ser. No. 734,439 Claims priority, application Great Britain, June 7, 1967, 26,355/67 Int. Cl. A23d 3/02 US. Cl. 99244 2 Claims ABSTRACT OF THE DISCLOSURE When the margarine coming from the cooler in solidified form is not immediately packaged, it is returned through a closed path so that it passes again through at least part of the production system, the closed return path comprising a pre-heater in the form of a tube heat exchanger, or the like, and a melting apparatus in the form of a plate heat exchanger for receiving the preheated margarine.
In the usual system for producing margarine, water, fat and other substances, such as vitamins, lactic acid, salts, etc., are mixed to for an emulsion which is first heated to a pre-determined temperature in a heat exchanger and is then cooled in a cooler especially adapted for the purpose. The margarine leaving the cooler is then packed by means of a packaging machine.
Unfortunately, faults occur rather often in the packaging machines if a system for production of margarine. This means that all of the margarine leaving the coolers cannot be packaged immediately. To enable the coolers to be kept running continuously, even when small faults arise in any of the packaging machines, a vessel is usually provided in the system for collecting margarine that cannot be packaged by the packaging machines. Margarine collected in a vessel of this kind is melted be heating means arranged in the vessel and is then returned to the system and cooled in order to re-solidify the margarine.
The equipment heretofore used for melting and returning margarin by-passing the packaging machines has certain drawbacks. For example, the margarine undergoing melting in the vessel is subjected not only to an undesired oxidation but also to rather great risks of infection, since this vessel is constantly open to the surrounding atmosphere.
The principal object of the present invention is to eliminate these drawbacks, which have long been recognized in the art of margine production. This object is achieved by providing the system with means for returning through a closed path the margarine that is not immediately packed by the packaging machines, so that it will again pass through all or part of the system, the closed returning means comprising a pro-heater in the form of a tube heat exchanger, or the like, and a melting apparatus in the form of a plate heat exchanger.
From the economic point of view, a plate heat exchanger is deemed to be the only kind of heat exchanger which could be considered for the above-noted purpose of melting the returning margarine. However, a plate heat exchanger is not easily adaptable for this purpose. It has proved quite impossible to introduce cold (that is, solid) margarine directly into a plate heat exchanger. Several experiments have been made in attempting to utilize a plate heat exchanger as a melting apparatus for margarine, but these experiments have not been successful until the advent of the present invention.
Fee
The invention is described in detail below with reference to the accompanying drawing, in which the single illustration is a diagrammatic view of a margarine producing system constructed according to the invention.
In the illustrated system, water, fat, lactic acid, salts, vitamins, etc., are introduced at A. These substances are mixed in a conduit 1 to form an emulsion which passes through a non-return valve 2 to a pump 3 and thence through a plate heat exchanger 4. In the plate heat exchanger, the emulsion is heated to about 38 C. By means of a number of high pressure pumps 5, the emulsion is then pumped to a number of coolers 6 wherein finished margarine is formed. The margarine leaving the coolers 6 has a temperature of about 15 C. and is consequently in a solid state. From these coolers, the finished margarine is pumped by means of the high pressure pumps 5 to a number of packaging machines 7, from which it is normally discharged in packages at B.
If the packaging machines 7 for some reason are unable to package all the margarine leaving the coolers 6, the margarine is pumped into one or more conduits 8. Conduits 8 are surrounded along part of their length by sleeve-like jackets 9 through which hot water is passed by way of suitable inlets and outlets (not shown). In its passage through each jacket 9, the margarine flowing through the corresponding conduit 8 is heated only at its surface layer. This is sufiicient for enabling the margarine to be introduced into a plate heat exchanger 10 without obstructions, the margarine being melted to a liquid state in the exchanger 10.
The high pressure pumps 5 are used for pumping the margarine through conduits 8 as well as through plate heat exchanger 10.
From the plate heat exchanger 10, the margarine is returned to conduit 1 at the inlet side of pump 3 but at the outlet side of non-return valve 2. In this way, it is caused to flow again through plate heat exchanger 4 and coolers 6.
Due to the above described arrangement, none of the coolers 6 needs to be taken out of operation if a small fault should occur in any of the packaging machines 7. The production process may go on continuously and, more particularly, in such a manner that margarine which cannot be packaged immediately, after having been cooled to a solid state, is returned to the production system in a liquid state without having come into contact with the surrounding atmosphere. Oxidation and infections are thereby prevented.
As shown in the drawing, the connection leading from each cooler 6 is provided with a valve 6a operable to direct the solidified margarine selectively to either the corresponding packaging machine 7 or the corresponding return conduit 8. Also, the plate heat exchanger 10 is shown with an inlet Illa and an outlet 10!; for the heating medium, whereby the latter flows through the heat exchanger in the same direction as the margarine from pre-heaters 9'.
We claim:
1. In combination with a margarine producing system comprising means for supplying an emulsion, a cooler connected to said supply means for solidifying the emulsion to form solid margarine, a machine for packaging solid margarine, and a connection between the cooler and the packaging machine for transmitting solid margarine to said machine, said system including a first closed flow path for the emulsion, means forming a second closed path leading from said connection for receiving margarine not immediately packaged by said machine and returning the unpackaged margarine to a point in said first closed flow path for passage again through at least part of the system, said closed return path including a pre-heater in the form of a tube heat exchanger and a melting apparatus in the form of a plate heat exchanger connected to receive margarine from the pre-heater.
2. The combination according to claim 1, in which said plate heat exchanger is arranged for passage of a heating medium therethrough in the same direction as the margarine.
' References Cited UNITED STATES PATENTS 2,353,3-82 7/1944 Barrett 165-66XR Hytte 165-66 Thompson 16566 Elwood et al. 99--122 Elwood et al. 99244 McCuiston 99'234 Froelich 16566 WALTER A. SCHEEL, Primary Examiner 0 ARTHUR O. HENDERSON, Assistant Examiner
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB26355/67A GB1138784A (en) | 1967-06-07 | 1967-06-07 | Plant for production and packaging of margarine |
Publications (1)
Publication Number | Publication Date |
---|---|
US3494275A true US3494275A (en) | 1970-02-10 |
Family
ID=10242380
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US734439A Expired - Lifetime US3494275A (en) | 1967-06-07 | 1968-06-04 | System for producing margarine |
Country Status (5)
Country | Link |
---|---|
US (1) | US3494275A (en) |
DE (1) | DE1767619B2 (en) |
GB (1) | GB1138784A (en) |
NL (1) | NL156029B (en) |
SE (1) | SE324946C (en) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0101104A1 (en) * | 1982-07-08 | 1984-02-22 | Unilever N.V. | A process and an apparatus for producing edible emulsions |
US5375510A (en) * | 1993-05-04 | 1994-12-27 | Miller; Van | Dry butter flake product having high milk solid content |
US20080264272A1 (en) * | 2007-04-26 | 2008-10-30 | Roden Allan D | Apparatus for dispersion of a second phase into a non-newtonian fluid base product |
US20080267008A1 (en) * | 2007-04-26 | 2008-10-30 | Roden Allan D | Method for dispersion of a second phase into a non-newtonian fluid base product |
Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2353382A (en) * | 1942-05-27 | 1944-07-11 | Whiting Milk Company | Timing method and apparatus |
US2659580A (en) * | 1950-04-19 | 1953-11-17 | Separator Ab | Plate heat exchanger |
US2937856A (en) * | 1956-01-26 | 1960-05-24 | Kusel Dairy Equipment Co | Plate heat exchanger |
US3033689A (en) * | 1959-02-03 | 1962-05-08 | Corn Products Co | Method of making margarine |
US3217632A (en) * | 1962-01-19 | 1965-11-16 | Corn Products Co | Apparatus for manufacturing margarine |
US3335655A (en) * | 1966-06-21 | 1967-08-15 | Richardson Merrell Inc | Continuous candy cooker |
US3367409A (en) * | 1965-01-15 | 1968-02-06 | Sulzer Ag | Liquid sterilization treatment plant |
-
1967
- 1967-06-07 GB GB26355/67A patent/GB1138784A/en not_active Expired
-
1968
- 1968-05-20 SE SE6806778A patent/SE324946C/en unknown
- 1968-05-29 DE DE1767619A patent/DE1767619B2/en not_active Withdrawn
- 1968-05-29 NL NL6807587.A patent/NL156029B/en not_active IP Right Cessation
- 1968-06-04 US US734439A patent/US3494275A/en not_active Expired - Lifetime
Patent Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2353382A (en) * | 1942-05-27 | 1944-07-11 | Whiting Milk Company | Timing method and apparatus |
US2659580A (en) * | 1950-04-19 | 1953-11-17 | Separator Ab | Plate heat exchanger |
US2937856A (en) * | 1956-01-26 | 1960-05-24 | Kusel Dairy Equipment Co | Plate heat exchanger |
US3033689A (en) * | 1959-02-03 | 1962-05-08 | Corn Products Co | Method of making margarine |
US3217632A (en) * | 1962-01-19 | 1965-11-16 | Corn Products Co | Apparatus for manufacturing margarine |
US3367409A (en) * | 1965-01-15 | 1968-02-06 | Sulzer Ag | Liquid sterilization treatment plant |
US3335655A (en) * | 1966-06-21 | 1967-08-15 | Richardson Merrell Inc | Continuous candy cooker |
Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0101104A1 (en) * | 1982-07-08 | 1984-02-22 | Unilever N.V. | A process and an apparatus for producing edible emulsions |
US5375510A (en) * | 1993-05-04 | 1994-12-27 | Miller; Van | Dry butter flake product having high milk solid content |
US20080264272A1 (en) * | 2007-04-26 | 2008-10-30 | Roden Allan D | Apparatus for dispersion of a second phase into a non-newtonian fluid base product |
US20080267008A1 (en) * | 2007-04-26 | 2008-10-30 | Roden Allan D | Method for dispersion of a second phase into a non-newtonian fluid base product |
US7895941B2 (en) * | 2007-04-26 | 2011-03-01 | Carmel Engineering, Inc. | Apparatus for dispersion of a second phase into a non-newtonian fluid base product |
US8153178B2 (en) | 2007-04-26 | 2012-04-10 | Carmel Engineering | Method for dispersion of a second phase into a non-Newtonian fluid base product |
US8826813B2 (en) | 2007-04-26 | 2014-09-09 | Carmel Engineering | Apparatus for dispersion of a second phase into a non-Newtonian fluid base product |
Also Published As
Publication number | Publication date |
---|---|
NL6807587A (en) | 1968-12-09 |
DE1767619B2 (en) | 1980-11-27 |
NL156029B (en) | 1978-03-15 |
GB1138784A (en) | 1969-01-01 |
SE324946C (en) | 1977-09-26 |
DE1767619A1 (en) | 1971-09-23 |
SE324946B (en) | 1970-06-15 |
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