EP2459009A1 - Method for production of extruded cereal product and such product - Google Patents

Method for production of extruded cereal product and such product

Info

Publication number
EP2459009A1
EP2459009A1 EP11718795A EP11718795A EP2459009A1 EP 2459009 A1 EP2459009 A1 EP 2459009A1 EP 11718795 A EP11718795 A EP 11718795A EP 11718795 A EP11718795 A EP 11718795A EP 2459009 A1 EP2459009 A1 EP 2459009A1
Authority
EP
European Patent Office
Prior art keywords
product
cereals
extruded
mixture
products
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.)
Withdrawn
Application number
EP11718795A
Other languages
German (de)
English (en)
French (fr)
Inventor
Romualdas Grikstas
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.)
UAB Naujasis Nevezis
Original Assignee
UAB Naujasis Nevezis
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 UAB Naujasis Nevezis filed Critical UAB Naujasis Nevezis
Publication of EP2459009A1 publication Critical patent/EP2459009A1/en
Withdrawn legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12CBEER; PREPARATION OF BEER BY FERMENTATION; PREPARATION OF MALT FOR MAKING BEER; PREPARATION OF HOPS FOR MAKING BEER
    • C12C1/00Preparation of malt
    • C12C1/02Pretreatment of grains, e.g. washing, steeping
    • AHUMAN NECESSITIES
    • A23FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23LFOODS, FOODSTUFFS OR NON-ALCOHOLIC BEVERAGES, NOT OTHERWISE PROVIDED FOR; PREPARATION OR TREATMENT THEREOF
    • A23L7/00Cereal-derived products; Malt products; Preparation or treatment thereof
    • A23L7/10Cereal-derived products
    • A23L7/197Treatment of whole grains not provided for in groups A23L7/117 - A23L7/196
    • AHUMAN NECESSITIES
    • A23FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23LFOODS, FOODSTUFFS OR NON-ALCOHOLIC BEVERAGES, NOT OTHERWISE PROVIDED FOR; PREPARATION OR TREATMENT THEREOF
    • A23L7/00Cereal-derived products; Malt products; Preparation or treatment thereof
    • A23L7/10Cereal-derived products
    • A23L7/198Dry unshaped finely divided cereal products, not provided for in groups A23L7/117 - A23L7/196 and A23L29/00, e.g. meal, flour, powder, dried cereal creams or extracts
    • AHUMAN NECESSITIES
    • A23FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23PSHAPING OR WORKING OF FOODSTUFFS, NOT FULLY COVERED BY A SINGLE OTHER SUBCLASS
    • A23P30/00Shaping or working of foodstuffs characterised by the process or apparatus
    • A23P30/20Extruding
    • CCHEMISTRY; METALLURGY
    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12CBEER; PREPARATION OF BEER BY FERMENTATION; PREPARATION OF MALT FOR MAKING BEER; PREPARATION OF HOPS FOR MAKING BEER
    • C12C7/00Preparation of wort
    • C12C7/04Preparation or treatment of the mash
    • C12C7/047Preparation or treatment of the mash part of the mash being unmalted cereal mash

Definitions

  • the invention is related to the food industry and may be used for production of beverages, fermented beverages, ethyl alcohol and concentrates of cereal extracts.
  • a method for producing a cereal adjunct for use in brewing is known (EP patent EP02251 10, publ. 1987-06-10, C08B30/12; C12C5/02; C12C7/047; C12G3/02; C08B30/00; C12C5/00; C12C7/00; C12G3/02), where starch-bearing product (barley or wheat) is crushed and extruded.
  • starch-bearing product barley or wheat
  • a moisture content of the starch product before extrusion is at least 20%, and extrusion is effected under high shear conditions, therefore, additional external heating is not used.
  • the extruded product is dried to moisture content less than 14%.
  • the shortcoming of this method is that products are crushed before extrusion, besides, the amount and size of insoluble fibrous materials (hulls) is not regulated.
  • the closest known technical solution is an extruded beer adjunct processing device and processing method thereof (US patent application 20100189869, publ. 2010-07- 29 AC12C704F1 ), where rice, maize, sorghum, barley, wheat, with a moisture content of less than 15%, are crushed to 0.65 - 2.0 mm particles, then are moistened to a moisture content of 10 - 30%.
  • the mass obtained is fed to the extruder, where the mass temperature is gradually elevated from 7- 25° to 60 - 95 °C, then extruded adjunct for brewing is ejected through the outlet, cooled to the ambient temperature and milled to particles of 0.9 - 2.0 mm in diameter.
  • the object of present invention is method for production_of the extruded cereal product, where cereals, products thereof and/or mixtures thereof are used, containing from 4 to 20% of insoluble fibrous materials, by weight of dry matter, and/or preparing a mixture of cereals and/or products thereof, containing from 4 to 20% of insoluble fibrous materials, by weight of dry matter. Then said cereals and/or products thereof and/or mixture thereof are stirred, moistened with water and/or with water steam at 0 - 100 °C temperature up to a moisture content of 15 - 50%, extruded and ejected the product having 100 - 180 °C temperature through the apertures, which diameter is from 3 to 10 mm.
  • the cereals and/or products thereof and/or a mixture thereof are moistened with water or with water steam during from 0.5 min. to 12 hours.
  • the extruded mixture should contain from 20 to 100% of unmilled cereals or mixtures thereof.
  • the amount of ingredients, composing the extruded cereal product from cereals, products thereof and/or mixtures thereof, in weight percentage, is:
  • barley and/or wheat rye, triticale, oat, maize, buckwheat, rice, sorghum, peas and/or mixtures thereof (by weight of dry matter) from 85 to 96;
  • insoluble fibrous materials contained from 4 to 20;
  • the particle size of 80-90% of total mass of said extruded cereal product is from 2.1 to 5 mm.; bulk density of said product is from 350 to 600 g/dm 3 and hydration capacity is from 1.5 to 3.0 cm 3 /g.
  • the mixture of the extruded cereal product and crushed cereal malt at the ratio 1 :1 has extractibility in water from 79.5 to 85% by the weight of dry matter.
  • the extruded cereal product is used in production of fermented beverages (e.g., beer, kvass), ethyl alcohol, concentrates of cereal extracts.
  • fermented beverages e.g., beer, kvass
  • ethyl alcohol ethyl alcohol
  • the extruded cereal product and barley, rye or other cereal malt is poured into the water, mixed, heated, and filtered.
  • the amount of the extruded cereal product in the mixture thereof with malt is from 5 to 90%.
  • the mash is produced, containing equal mass quantities of milled barley malt and extruded barley product.
  • the technological conditions of mash mixing and filtration do not differ from the routine brewing regimes.
  • the fluctuation range of the physical and chemical characteristics of the mash and wort are presented in the table.
  • Extractibility extract fine
  • % d.m. 80 - 85 4.5.1
  • extractibility in the water calculated according to the weight of dry matter, is determined in the mixture of the cereal product and ground cereal malt (ratio 1 :1 ), according to the European Brewery Convention (EBC) methods 4.5.1 "Extract of malt: Congress mash";
  • bran, hulls and/or insoluble fibrous materials by way of calculation according to research or data of initial crude material composition.
  • Food barley with a moisture content of 12% is cleaned in the screener and magnetic separator. Then, 100 kg of barley is fed into the tank with a mixer, adding 40 kg of heated to a temperature of 25 °C drinking water, and mixing periodically for 2 hours. After that some 10 kg of water is poured out. Barley with a moisture content of about 32% is fed into the extruder, where it is extruded, and after reaching a temperature of 140 - 150 °C the product is ejected out through the apertures of 7 mm in diameter. The extruded barley slices are crushed into particles of 2.5 - 5 mm in size and dried. The physical and chemical characteristics of the obtained extruded cereal product are as follows:
  • the extruded cereal product is used in the production of beer, beer beverages, and concentrates of cereal extracts.
  • Example 2 The extruded cereal product is used in the production of beer, beer beverages, and concentrates of cereal extracts.
  • Raw products - food rye, wheat, triticaie - are cleaned in the screener and magnetic separator.
  • Wheat is ground to the course meal with particle size of 1 .5 - 2.5 mm, and whole-grain triticaie is ground to fine flour.
  • a mixture is made of 20 kg unmilled rye, 65 kg of wheat meal, 10 kg of whole-grain triticaie flour and 5 kg wheat and/or rye bran.
  • a moisture content of the mixture is 10%, amount of insoluble fibrous materials is 8%.
  • the mixture is fed into the mixer, where it is moistened with 10 kg of water and mixed for about 30 seconds.
  • the mixture with a moisture content of about 18% is fed into the extruder, where it is extruded, and after reaching a temperature of 160 - 180 °C the product is ejected out through the apertures of 3 mm in diameter.
  • the extruded product is crushed to particles of 2.5 - 5 mm in size.
  • the extruded cereal product is used in the production of ethyl alcohol or concentrates of cereal extracts.
  • Example 3 The extruded cereal product is used in the production of ethyl alcohol or concentrates of cereal extracts.
  • Food barley with a moisture content of 12% is cleaned in the screener and magnetic separator. Then, 100 kg of barley is poured into the tank with a mixer, containing 150 kg of drinking water, heated to a temperature of 80 °C, mixing periodically for 6 min. and pouring out excessive water. Barley with a moisture content of about 30% is fed into the extruder, where it is extruded, and after reaching a temperature of 140 - 150°C the product is ejected out through the apertures of 7 mm in diameter. The extruded barley slices are crushed into particles of 2.5-5 mm in size, and dried.
  • the physical and chemical characteristics of the obtained extruded cereal product are as follows:
  • the extruded cereal product as a cereal malt adjunct is used in the production of beer, kvass and concentrates of cereal extracts.
  • Extruding of unmilled cereals by the method of present invention the product with a relatively higher volume mass, unchanged aroma, characteristic of crude product, i.e. without odour and taste, specific for extrudants, is produced, whereof starch is easier and more fully saccharized during mash mixing.
  • whole hulls are preserved, this having a positive effect on the extract filtration process.
  • the extruded cereal products, produced by the present invention exhibit properties, close to barley or rye malt, i.e., they quickly absorb water in the mash boiling kettle; starch hydrolysis and saccharification takes place readily. These products reduce the use of malt in brewing. They may also be used in the production of cereal extracts.

Landscapes

  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Food Science & Technology (AREA)
  • Organic Chemistry (AREA)
  • Health & Medical Sciences (AREA)
  • Polymers & Plastics (AREA)
  • Biochemistry (AREA)
  • Nutrition Science (AREA)
  • Bioinformatics & Cheminformatics (AREA)
  • General Engineering & Computer Science (AREA)
  • General Health & Medical Sciences (AREA)
  • Genetics & Genomics (AREA)
  • Wood Science & Technology (AREA)
  • Zoology (AREA)
  • Manufacturing & Machinery (AREA)
  • Cereal-Derived Products (AREA)
  • Non-Alcoholic Beverages (AREA)
  • Medicines Containing Plant Substances (AREA)
EP11718795A 2010-09-28 2011-03-31 Method for production of extruded cereal product and such product Withdrawn EP2459009A1 (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
LT2010077A LT5842B (lt) 2010-09-28 2010-09-28 Ekstruduoto grūdų produkto gamybos būdas ir produktas
PCT/LT2011/000006 WO2012044141A1 (en) 2010-09-28 2011-03-31 Method for production of extruded cereal product and such product

Publications (1)

Publication Number Publication Date
EP2459009A1 true EP2459009A1 (en) 2012-06-06

Family

ID=44140849

Family Applications (1)

Application Number Title Priority Date Filing Date
EP11718795A Withdrawn EP2459009A1 (en) 2010-09-28 2011-03-31 Method for production of extruded cereal product and such product

Country Status (3)

Country Link
EP (1) EP2459009A1 (lt)
LT (1) LT5842B (lt)
WO (1) WO2012044141A1 (lt)

Families Citing this family (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
RU2609298C1 (ru) * 2015-10-02 2017-02-01 Олег Иванович Квасенков Способ производства концентрата квасного сусла
RU2609454C1 (ru) * 2015-10-02 2017-02-01 Олег Иванович Квасенков Способ производства концентрата квасного сусла
RU2609338C1 (ru) * 2015-10-05 2017-02-01 Олег Иванович Квасенков Способ получения концентрата квасного сусла
RU2609956C1 (ru) * 2015-10-06 2017-02-07 Олег Иванович Квасенков Способ получения концентрата квасного сусла
RU2609942C1 (ru) * 2015-10-06 2017-02-07 Олег Иванович Квасенков Способ получения концентрата квасного сусла

Family Cites Families (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4350714A (en) * 1979-08-02 1982-09-21 The Quaker Oats Company Corn bran expanded cereal
US4497840A (en) * 1981-06-29 1985-02-05 The Quaker Oats Company Cereal foods made from oats and method of making
US4759942A (en) * 1985-09-19 1988-07-26 General Foods Corporation Process for producing high fiber expanded cereals
GB8528981D0 (en) 1985-11-25 1986-01-02 Billington & Son Ltd Edward Producing cereal adjunct
DE4232585A1 (de) * 1992-09-23 1994-03-24 Mannesmann Ag Dreiphasige Lichtbogenofenanlage mit Drossel
KR19980703564A (ko) * 1993-12-28 1998-11-05 빌르에르 고 가용성 섬유의 시리얼 식품
US6010732A (en) * 1997-11-04 2000-01-04 General Mills, Inc. Grain based extruded product and process of making
CN100457884C (zh) * 2005-12-09 2009-02-04 山东理工大学 啤酒辅料挤压蒸煮的加工方法、加工装置和糖化方法
SE534934C2 (sv) * 2009-06-01 2012-02-21 Biovelop Ab Cerealieprodukt av havre samt metod för att tillverka densamma

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
See references of WO2012044141A1 *

Also Published As

Publication number Publication date
LT5842B (lt) 2012-05-25
LT2010077A (lt) 2012-04-25
WO2012044141A1 (en) 2012-04-05

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