US3494275A - System for producing margarine - Google Patents

System for producing margarine Download PDF

Info

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
Application number
US734439A
Inventor
Lennart Adolf Bondesson
Hilding Sven Svensson
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.)
Alfa Laval AB
Original Assignee
Alfa Laval AB
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 Alfa Laval AB filed Critical Alfa Laval AB
Application granted granted Critical
Publication of US3494275A publication Critical patent/US3494275A/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Images

Classifications

    • AHUMAN NECESSITIES
    • A01AGRICULTURE; FORESTRY; ANIMAL HUSBANDRY; HUNTING; TRAPPING; FISHING
    • A01JMANUFACTURE OF DAIRY PRODUCTS
    • A01J21/00Machines for forming slabs of butter, or the like
    • A01J21/02Machines for forming slabs of butter, or the like with extruding arrangements and cutting devices, with or without packing devices
    • 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

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
US734439A 1967-06-07 1968-06-04 System for producing margarine Expired - Lifetime US3494275A (en)

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)

* Cited by examiner, † Cited by third party
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)

* Cited by examiner, † Cited by third party
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

Patent Citations (7)

* Cited by examiner, † Cited by third party
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)

* Cited by examiner, † Cited by third party
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

Similar Documents

Publication Publication Date Title
US5360055A (en) Method and apparatus for heat treating a fluid product
US3494275A (en) System for producing margarine
GB972747A (en) Improvements in and relating to flowing-fluid temperature control systems
GB1272787A (en) Tubular heat transfer device
GB1136486A (en) Steam infuser for heating liquids
US2392021A (en) Heat exchange apparatus
EP4068984B1 (en) Plant for pasteurizing foodstuffs or beverages filled into closed containers by way of a process liquid
GB1188164A (en) A Plant for Continuous Heat Treatment of a Liquid Product
GB1093451A (en) Preparation of polyamides
EP0101104B1 (en) A process and an apparatus for producing edible emulsions
US2197118A (en) Heat transfer apparatus
GB1282003A (en) Improvements in or relating to the sterilisation of containers
US2414623A (en) Heating system
US2632505A (en) Concentration of charrable heatsensitive liquids
US2676651A (en) Evaporating apparatus
DE823126C (en) Centrifugal separator for cleaning beer
US2201056A (en) Apparatus for pasteurizing liquids
US890684A (en) Apparatus for heating, cooling, and pasteurizing liquids.
DE3125561C2 (en)
US1821934A (en) Heat interchanger
DE3003663A1 (en) METHOD AND DEVICE FOR REDUCING THE LOSS OF HEATING THROUGH CIRCULAR VESSEL CARRIER
DE964116C (en) Process for degassing and cooling fluids used for human consumption or nourishment
SE509020C2 (en) Plant for heat treatment of a liquid food product
US1687941A (en) Steam and other vapor power plant utilizing caustic soda or other auxiliary fluids
DE340943C (en) Drinking water heater