Classifications

• • A—HUMAN NECESSITIES
  • A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
  • A23J—PROTEIN COMPOSITIONS FOR FOODSTUFFS; WORKING-UP PROTEINS FOR FOODSTUFFS; PHOSPHATIDE COMPOSITIONS FOR FOODSTUFFS
  • A23J1/00—Obtaining protein compositions for foodstuffs; Bulk opening of eggs and separation of yolks from whites
  • A23J1/006—Obtaining protein compositions for foodstuffs; Bulk opening of eggs and separation of yolks from whites from vegetable materials

Definitions

• the invention relates to a method for obtaining protein from vegetable raw material and a plant for carrying it out.
• vegetable raw material is understood to mean all types of vegetation, e.g. Grass, herbs, aquatic plants, algae and also shrubs and trees, provided, however, that they can be brought into a starting form suitable for the invention. It is known to use a part of the raw material mentioned for food purposes, especially for the production of animal food, the raw material being pretreated, essentially crushed and dried so that it becomes a handy dry product, e.g. Pellets or flour, can be processed.
• the drying of grass which is used in the form of hay for feeding cattle when fresh grass is not available, is generally known. When drying in air and in the drying plants, however, the plant liquid is essentially lost and a large part of the protein contained in the plants is destroyed. In the known drying systems, part of the
• the vegetable raw material is processed mechanically and is separated into a liquid phase and a solid phase, the protein-containing solid being processed into a dry product, while the dry substance, which also contains protein, is Liquid coagulates, the coagulate is separated from the residual liquid and processed into a dry product.
• the system used to carry out the method according to the invention with a loading and metering device is characterized by a squeezing and grinding station for the raw material with a subsequent first separating device.
• Device for separating the liquid from the solid phase through a drying and briquetting station for the solid, through a coagulating station for the liquid phase obtained from the first separating device, with a subsequent second separating device for separating the coagulate from the residual liquid and by a second drying and briquetting station for the coagulate.
• the invention is shown in the drawing in an exemplary embodiment and described below. Show it;
• FIG. 1 shows a block diagram of a plant for carrying out the method according to the invention for obtaining protein from vegetable raw material
• Fig. 2 is a side view
• Fig. 3 is a plan view of a schematic representation of a system with its individual devices, which corresponds to the system of FIG. 1.
• the arrow 1 denotes the continuous and metered input of vegetable raw material into a processing plant.
• the raw material arrives in a squeezing and grinding station represented by block 2, in which the raw material is crushed and digested, a part of the juice already being squeezed out.
• the raw material treated in this way passes into a first separating device 3, in which the liquid phase is separated from the solid phase.
• the solid is fed into a first drying and briquetting station 4, where it is heated, pressed and pelletized
• the liquid is conveyed into a coagulation station 5 and treated there with a coagulation aid.
• the liquid treated in this way then passes into a second separating device 6, in which the coagulate is separated from the residual liquid.
• the coagulate is dried, pressed and processed into pellets in a second drying and briquetting station 7, while the residual liquid indicated by arrow 8 can be used further, e.g. for the production of yeast or for use as fertilizer or for the production of biogas.
• the pellets produced in the two drying and briquetting stations 4, 7 represent an easy-to-use product which can be stored, packaged and transported in a known manner.
• the system shown in FIGS. 2 and 3 has a dosing device 10 into which the raw material is delivered.
• the raw material is fed to a feed roller 12 with drivers * 13 by a conveyor belt 11, while the metering is carried out by means of a rotary flap 14.
• the feed roller 12 conveys the raw material onto a conveyor belt 15 with which a rotating, crushing and grinding mechanism 16 is loaded.
• the crushing and grinding mechanism 16 is a twin-screw press of special design, in which the raw material is crushed, crushed, i.e. unlocked, and partially juiced.
• a roller juicer is connected to the squeezing and grinding mechanism 16, in which the raw material is separated into a liquid phase and a solid phase.
• the roller juicer 17 has rotating rollers 18 which roll on the raw material in a filter material and squeeze it out. Transport takes place at the same time
• the drying and briquetting unit 20 is a screw press of a special design in which the solid is dried, pressed and formed into pellets. It is essential that these pellets are a finished product that does not require further treatment.
• the pellets are merely cooled on a conveyor belt 21 and, at the end of the conveyor belt, are stored, packaged and transported in a manner not shown.
• the liquid obtained in the horizontal roller juicer 17 is collected in a trough 22 and conveyed via a line 23 into a coagulation device 24, in which the dry substance of the liquid is coagulated by a coagulation aid 25.
• the Koagulier engaged 24 can operate in arge Ch 'or operate continuously.
• the coagulated liquid passes through a line 26 into a roller juicer 27, in which the coagulate is separated from the residual liquid.
• the roller juicer 27 can be designed in the same way as the roller juicer 17 and can also be mounted horizontally.
• the coagulate is fed via a line 28 to a drying and briquetting plant 29, where it is dried, pressed and shaped into pellets, whereupon the pellets are cooled on a conveyor belt 30 and passed on for further treatment.
• the drying and briquetting unit 29 is designed in the same way as the drying and briquetting unit 20 for the treatment of the solid.
• the residual liquid obtained in the roller juicer 27 is collected in a tub 31 and discharged through a line 32.
• a container 33 is indicated in FIG. 2, in which the residual liquid is collected. It has been shown that this residual liquid can serve as food for some fish species.
• a protein concentrate with 40-60% crude protein can be produced from the liquid contained in the roller juicer 17 from the dry substance contained therein. With the exception of methionine, this protein concentrate meets the maximum requirements placed on a protein used in human nutrition.
• the solid separated from the liquid serves as feed in the same way as an alfalfa or natural grass green meal.
• Protein concentrate moisture 6.0% crude protein 48.0% crude fiber 2.0% crude ash 12.0% NFE 28.0% crude fat 4.0% (of which 15 - 24% linoleic acid) - 7 -
• the relatively simple construction of the plant also allows it to be made mobile and to be used wherever a corresponding raw material is available.
• the residual liquid obtained in the roller juice press 27 is used on the spot as a fertilizer.
• the percentages given above are percentages by weight.
• other separating devices can also be used, for example centrifuges or filter presses.
• the squeezing and grinding mechanism 16, the roller juice press 17 and the drying and briquetting press 20 are replaced by a single screw press which, as already described above, opens up the raw material on the inlet side, crushes it and squeezes it out to separate the juice, while in the outlet side Part of the drying, the removal of any steam and the briquetting takes place.
• the system is further simplified and the space requirement is reduced, so that it can also be mobile.

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• Life Sciences & Earth Sciences (AREA)
• Chemical & Material Sciences (AREA)
• Biochemistry (AREA)
• Engineering & Computer Science (AREA)
• Food Science & Technology (AREA)
• Polymers & Plastics (AREA)
• Fodder In General (AREA)
• Fertilizers (AREA)

Applications Claiming Priority (2)

Publications (1)

Family

ID=4247743

Family Applications (1)

Country Status (9)

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Family Cites Families (6)

• 1982
  • 1982-05-17 CH CH3061/82A patent/CH648188A5/de not_active IP Right Cessation
• 1983
  • 1983-05-09 HU HU832271A patent/HUT37011A/hu unknown
  • 1983-05-09 EP EP83901355A patent/EP0108762A1/de not_active Withdrawn
  • 1983-05-09 JP JP58501493A patent/JPS59500846A/ja active Pending
  • 1983-05-09 WO PCT/CH1983/000058 patent/WO1983003952A1/de not_active Application Discontinuation
  • 1983-05-17 IT IT21126/83A patent/IT1169727B/it active
• 1984
  • 1984-01-13 FI FI840124A patent/FI840124A0/fi not_active Application Discontinuation
  • 1984-01-16 NO NO840141A patent/NO840141L/no unknown
  • 1984-01-16 DK DK0184/84A patent/DK18484D0/da not_active Application Discontinuation

Non-Patent Citations (1)

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