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
  • A23J3/00—Working-up of proteins for foodstuffs
  • A23J3/14—Vegetable proteins
  • A23J3/18—Vegetable proteins from wheat
• • A—HUMAN NECESSITIES
  • A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
  • A23L—FOODS, FOODSTUFFS OR NON-ALCOHOLIC BEVERAGES, NOT OTHERWISE PROVIDED FOR; PREPARATION OR TREATMENT THEREOF
  • A23L27/00—Spices; Flavouring agents or condiments; Artificial sweetening agents; Table salts; Dietetic salt substitutes; Preparation or treatment thereof
  • A23L27/50—Soya sauce

Definitions

• the present invention relates to a pelletisation process and more particularly to a process for the pelletisation of a dried gluten material which may be used as a fermenting material for the production of fermented products such as soy sauce and seasonings, etc.
• EP-A-071 1510 claims a process for the production of a fermenting material which comprises using 5-100% by weight of a dried gluten product and 95-0% by weight of wheat as a raw material, adding steam to the material so as to adjust a moisture
• the dried gluten product is said to include dried wheat gluten product, dried corn gluten product
• the fermenting material may be used in the manufacture of fermented products such as soy sauce, miso, seasoning and the like.
• Devitalisation is part of denaturation and can be achieved by heat treatment.
• water can be added in an amount of from 35 19 to 60%, depending on the degree of devitalisation, to form a dough and to facilitate pelletisation. Additional water can be introduced to the pellets, if necessary, to adjust the moisture content to from 35 to 60% based on the. weight of the pellets, so that they are suitable for koji fermentation, before sterilisation and further denaturation by steam. No lumps are produced and no losses occur.
• the devitalisation process is necessary only when the gluten is vital, for example in the case of vital wheat gluten.
• the present invention provides a process for the production of a fermenting material which comprises forming a dough by adding water to a dried gluten in an amount of from 19 to 60% by weight based on the weight of the dough, pelletising the dough and adding water to adjust the moisture content to from 35 to 60% by weight based on the weight of the pellets before sterilising the pellets by steam treatment.
• the dried gluten may be wheat gluten, corn gluten or rice gluten and one or more glutens may be used to produce the pellet.
• the devitalisation may be carried out by heating at a temperature above 60°C, e.g. by means of hot air or contact with hot surface, in a drier, an oven or using a steam jacketed vessel.
• the duration of the devitalisation may be from 5 seconds to 3 hours and depends on the temperature used, generally longer periods of time being required at lower temperatures.
• the devitalisation may be carried out at a temperature from 60° to 200°C over a period of from 3 hours to 5 seconds, preferably from 100° to 120°C over a period of from 30 to 5 minutes.
• wheat such as wheat flour or wheat bran as the carbohydrate source
• the amount of wheat added may be up to to 90%, preferably from 5 to 50% and especially from 10 to 30% by weight based on the weight of the dried raw material.
• the amount of water added to the dried gluten is preferably from 30 to 45% by weight based on the weight of the dough. The amount of water added depends on the vitality of the gluten as well as the composition of the raw materials.
• the dough may be pelletised by conventional means such as a screw press, a meat mincer or a pellet mill.
• the pellets may have either a cylindrical shape with an average diameter of from 1 to 10mm, preferably from 2 to 8mm and especially from 4 to 6mm or they may have a spherical shape with diameter of from 1 to 10mm, preferably from 2 to 8mm and especially from 4 to 6mm.
• the water added to the pellets before sterilisation by steaming preferably increases the moisture content to from 40 to 50% by weight based on the weight of the pellets.
• the pellets may then be made into koji by mixing with carbohydrates, inoculating with Aspergilli and fermenting the koji substrate for about two days.
• the koji may then be converted into a seasoning by conventional methods or by a method as described in EP 0640294 or our co-pending patent applications EP-A-96114850.9 and EP-A- 96202309.9, the entirety of which are hereby incorporated by reference.
• the use of the pellets of the present invention in the koji fermentation gives a good hydrolysis yield due to the ease of disintegration during hydrolysis.
• the process may be carried out continuously, e.g. using a noodle line concept but with a lower precision on the dough thickness and noodle diameter.
• the continuous process includes mixing the ingredients (dried devitalised gluten, wheat flour, wheat bran), pelletisation, addition of water, steaming, cooling and inoculation of spore suspension.
• the substrate is then loaded onto the koji machine for fermentation and subsequent hydrolysis.
• 35kg of vital wheat gluten was devitalised by heating at 100°C in a ribbon blender with a steam jacket for 30 minutes.
• the thus devitalised wheat gluten was mixed with 2.5 kg of wheat bran and 12.5 kg of wheat flour. Water was added to the mixture to obtain a moisture content of 33%w/w.
• the dough formed was then fed into a mincer to produce cylindrical pellets each having a diameter of 5mm. Additional water was introduced to the pellets such that the moisture content of the pellets was 47%w/w.
• the pellets were then steamed at 100°C for 10 minutes and afterwards cooled to below 40°C.
• the cooled pellets were mixed with a liquid suspension of 25g of Aspergillus oryzae spores inoculum.
• Koji fermentation was carried out for 42 hours at 27 - 33°C.
• the matured koji was hydrolysed by adding water to obtain a hydrolysate with a total solid content of 20.2%m/m.
• the hydrolysis was carried out at 4°C for 2 weeks before 2 weeks of moro i fermentation where salt was added at a level of 12%m/m.
• the moromi was pressed and the clear sauce was heat treated at 90°C for 20 minutes.
• the product thus prepared had a light colour, good taste and excellent flavour.
• Example 1 Water was added directly to a mixture of 35kg of rice gluten, 2.5 kg of wheat bran and 12.5 kg of wheat flour to obtain a moisture content of 45%w/w. The dough formed was then fed into a mincer to produce cylindrical pellets each having a diameter of 5mm. A similar procedure for steaming, koji making and sauce preparation was followed as in Example 1.
• the product thus prepared had a light colour, good taste and excellent flavour.
• Example 2 A similar procedure was carried out as in Example 2 except that corn gluten powder was used instead of rice gluten powder and the moisture content of the dough before pelletisation was 35%.w/w. Additional water was introduced to the pellets before steaming such that the moisture content of the pellets was 47%w/w.
• the product thus prepared had a light colour, good taste and excellent flavour.
• Example 2 A similar procedure was carried out as in Example 1 except that 35kg of devitalised wheat gluten was mixed with 2kg of wheat bran and 4 kg of wheat flour and water was added to give a moisture content of 40%w/w before pelletisation.
• Example 2 A similar procedure was carried out as in Example 1 except that 35kg of devitalised wheat gluten was mixed with 5 kg of vital wheat gluten, 2.4kg of wheat bran and 4.7 kg of wheat flour and water was added to give a moisture content of 33%w/w before pelletisation.
• Example 2 A similar procedure was carried out as in Example 1 except that the devitalisation of wheat gluten was carried out by adding directly superheated steam at 1 bar and 150°C to the wheat gluten before mixing with the carbohydrates and forming the pellets.
• Example 2 A similar procedure was carried out as in Example 1 except that the devitalisation of wheat gluten was carried out in a fluidised bed dryer with inlet air temperature set at 110°C.
• Example 9 A similar procedure was carried out as in Example 1 except that the diameter of the pellets were 3 mm.
• Example 2 A similar procedure was carried out as in Example 1 except that the pelletisation was carried out using a screw press.
• Example 2 A similar procedure was carried out as in Example 1 except that the pelletiser used produced spherical granulates with diameter of 3-8mm.
• Example 1 A similar procedure was carried out as in Example 1 except that 25 kg of corn gluten pellets prepared as described in Example 3 were fermented together with the wheat gluten pellets.
• Example 3 A similar procedure was carried out as in Example 3 except that 35 kg of wheat gluten devitalised as described in Example 1 was mixed together with 35 kg of rice gluten, 5 kg of wheat bran and 25 kg of wheat flour before the pelletisation.
• Example 11 A similar procedure was carried out as in Example 11 except that 40 kg of steamed defatted soya bean mill was used instead of corn gluten.
• Example 1 A similar procedure was carried out as in Example 1 except that wheat flour and wheat bran were mixed with vital wheat gluten before devitalisation.
• Example 15 A similar procedure was carried out as in Example 1 except that an inoculum of lactic acid bacteria at 7x10 D cfu/g was added to the steamed pellets before koji fermentation and the hydrolysis was carried out at 35°C for 2 days. Pressing was carried out after the hydrolysis and with salt added to a level of 12%m/m.
• Example 2 A similar procedure was carried out as in Example 1 except that the devitalisation step is omitted and water is added to the mixture of wheat gluten, wheat bran and wheat flour to obtain a moisture content of 20%w/w.

Landscapes

• Life Sciences & Earth Sciences (AREA)
• Chemical & Material Sciences (AREA)
• Food Science & Technology (AREA)
• Nutrition Science (AREA)
• Engineering & Computer Science (AREA)
• Health & Medical Sciences (AREA)
• Polymers & Plastics (AREA)
• Biochemistry (AREA)
• Fodder In General (AREA)
• Seasonings (AREA)
• Soy Sauces And Products Related Thereto (AREA)
• Cereal-Derived Products (AREA)
• Seeds, Soups, And Other Foods (AREA)
• Micro-Organisms Or Cultivation Processes Thereof (AREA)
• Feeding, Discharge, Calcimining, Fusing, And Gas-Generation Devices (AREA)

Priority Applications (15)

Applications Claiming Priority (2)

Related Child Applications (1)

Publications (1)

Family

ID=20429945

Family Applications (1)

Country Status (25)

Cited By (2)

Families Citing this family (12)

Citations (4)

Family Cites Families (3)

• 1998
  • 1998-03-05 SG SG1998000488A patent/SG70069A1/en unknown
• 1999
  • 1999-02-23 DE DE69913502T patent/DE69913502T2/de not_active Expired - Fee Related
  • 1999-02-23 IN IN217MA1999 patent/IN187778B/en unknown
  • 1999-02-23 AU AU29278/99A patent/AU754247C/en not_active Ceased
  • 1999-02-23 NZ NZ506242A patent/NZ506242A/en unknown
  • 1999-02-23 PL PL99342603A patent/PL342603A1/xx unknown
  • 1999-02-23 HU HU0101109A patent/HUP0101109A3/hu unknown
  • 1999-02-23 CA CA002314952A patent/CA2314952A1/en not_active Abandoned
  • 1999-02-23 RU RU2000125110/12A patent/RU2228057C2/ru not_active IP Right Cessation
  • 1999-02-23 SK SK1322-2000A patent/SK13222000A3/sk unknown
  • 1999-02-23 CN CN99803410A patent/CN1291866A/zh active Pending
  • 1999-02-23 TR TR2000/02550T patent/TR200002550T2/xx unknown
  • 1999-02-23 WO PCT/EP1999/001133 patent/WO1999044437A1/en not_active Application Discontinuation
  • 1999-02-23 YU YU50400A patent/YU50400A/sh unknown
  • 1999-02-23 BR BR9908500-3A patent/BR9908500A/pt not_active IP Right Cessation
  • 1999-02-23 IL IL13659799A patent/IL136597A/en not_active IP Right Cessation
  • 1999-02-23 AT AT99910253T patent/ATE255820T1/de not_active IP Right Cessation
  • 1999-02-23 ID IDW20001674A patent/ID25893A/id unknown
  • 1999-02-23 EP EP99910253A patent/EP1059849B1/en not_active Expired - Lifetime
  • 1999-02-23 JP JP2000534062A patent/JP2002505091A/ja active Pending
  • 1999-03-03 KR KR1019990006950A patent/KR19990077557A/ko not_active Ceased
  • 1999-03-05 AR ARP990100956A patent/AR015536A1/es unknown
  • 1999-03-09 TW TW088103584A patent/TW529913B/zh not_active IP Right Cessation
• 2000
  • 2000-08-29 US US09/617,943 patent/US6309680B1/en not_active Expired - Fee Related
  • 2000-08-31 NO NO20004330A patent/NO20004330L/no unknown

Patent Citations (4)

Non-Patent Citations (1)

Also Published As

Similar Documents

Legal Events