GB366516A - Improved manufacture of food products and medicinal preparations from corn milling by-products - Google Patents

Improved manufacture of food products and medicinal preparations from corn milling by-products

Info

Publication number
GB366516A
GB366516A GB31294/30A GB3129430A GB366516A GB 366516 A GB366516 A GB 366516A GB 31294/30 A GB31294/30 A GB 31294/30A GB 3129430 A GB3129430 A GB 3129430A GB 366516 A GB366516 A GB 366516A
Authority
GB
United Kingdom
Prior art keywords
flour
products
germs
alcohol
bye
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
Application number
GB31294/30A
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.)
Individual
Original Assignee
Individual
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 Individual filed Critical Individual
Publication of GB366516A publication Critical patent/GB366516A/en
Expired legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C11ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
    • C11BPRODUCING, e.g. BY PRESSING RAW MATERIALS OR BY EXTRACTION FROM WASTE MATERIALS, REFINING OR PRESERVING FATS, FATTY SUBSTANCES, e.g. LANOLIN, FATTY OILS OR WAXES; ESSENTIAL OILS; PERFUMES
    • C11B1/00Production of fats or fatty oils from raw materials
    • C11B1/10Production of fats or fatty oils from raw materials by extracting

Landscapes

  • Chemical & Material Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Wood Science & Technology (AREA)
  • Organic Chemistry (AREA)
  • Cosmetics (AREA)
  • Medicines Containing Plant Substances (AREA)

Abstract

In preparing food products an oily substance containing lipoids and lipoid-soluble vitamins, obtained by extracting with an organic solvent the germ-containing bye-products of husking or milling seeds, particularly cereals, or the germs separated from said bye-products, and a powder or flour containing hydrosoluble vitamins obtained by milling the extracted germs and sifting to separate the powder or flour from the cortical elements of the germs are added to the food products. The bye-products or germs are dried in ovens up to 60-70 DEG C., sorted, passed if necessary through a grinding mill, extracted with boiling alcohol, preferably with ethyl alcohol at reduced pressure and not over 70 DEG C. The alcohol is distilled from the extract and the residue freed from the last traces of it by means of a hot air current or by drying in an oven at 60-70 DEG C. An emulsion is then made of the residue in an alkali solution, e.g. a 30 per cent solution of caustic soda, and is added to the food product. The extracted germs freed from alcohol are ground in a mill preferably having porcelain or other smooth rollers and then sifted to separate the flour from the cortical elements, 5-15 per cent of the flour being added in preparing an alimentary paste from groats or flour, together with 0,25-1 per cent of the oily substance. The Specification as open to inspection under Sect. 91 (3) (a) comprises also the extraction of the oily substance by pressure and its use in preparing medicinal and other emulsions and oils. This subject-matter does not appear in the Specification as accepted.ALSO:An oily substance containing lipoids and lipoid-soluble vitamins, obtained by extracting with an organic solvent the germ-containing bye-products of husking or milling seeds, particularly cereals, or the germs separated from said bye-products, and a powder or flour containing hydrosoluble vitamins obtained by milling the extracted germs and sifting to separate the powder or flour from the cortical elements of the germs are added to food products. The bye-products are dried in ovens at up to 60-70 DEG C., sorted, passed if necessary through a grinding mill, extracted with boiling alcohol, preferably with p ethyl alcohol at reduced pressure and not over 70 DEG C. The alcohol is distilled from the extract and the residue freed from the last traces of it by means of a hot air current or by drying in an oven at 60-70 DEG C. An emulsion is then made of the residue in an alkali solution, e.g. a 30 per cent solution of caustic soda, and is added to the food product. The extracted germs freed from alcohol are ground in a mill preferably having porcelain or other smooth rollers and then sifted to separate the flour from the cortical elements, 5-15 per cent of the flour being added in preparing an alimentary paste from groats or flour, together with 0,25-1 per cent of the oily substance. The Specification as open to inspection under Sect. 91 (3) (a) comprises also the extraction of the oily substance by pressure. This subject-matter does not appear in the Specification as accepted.ALSO:In preparing food products, e.g. macaroni, vermicelli, and other alimentary pastes, bread, biscuits, infant foods, and chocolate, an oily substance containing lipoids and lipoid-soluble vitamins obtained by extracting with an organic solvent the germ-containing bye-products of husking or milling seeds, particularly cereals, or the germs separated from said bye-products, and a powder or flour containing hydrosoluble vitamins obtained by milling the extracted germs and sifting to separate the powder or flour from the cortical elements of the germs are added to the food products. The bye-products are dried in ovens at up to 60-70 DEG C., sorted, passed if necessary through a grinding mill, extracted with boiling alcohol, preferably with ethyl alcohol at reduced pressure and not over 70 DEG C. The alcohol is distilled from the extract and the residue freed from the last traces of it by means of a hot air current or by drying in an oven at 60-70 DEG C. An emulsion is then made of the residue in an alkali solution, e.g. a 30 per cent solution of caustic soda, and is added to the food product. The extracted germs freed from alcohol are ground in a mill preferably having porcelain or other smooth rollers and then sifted to separate the flour from the cortical elements, 5 to 15 per cent of flour being added in preparing an alimentary paste from groats or flour, together with 0-25 to 1 per cent of the oily substance. The Specification as open to inspection under Sect. 91 (3) (a) comprises also the extraction of the oily substance by pressure and its use in preparing medicinal and other emulsions and oils. This subject-matter does not appear in the Specification as accepted.
GB31294/30A 1929-10-19 1930-10-18 Improved manufacture of food products and medicinal preparations from corn milling by-products Expired GB366516A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
IT366516X 1929-10-19

Publications (1)

Publication Number Publication Date
GB366516A true GB366516A (en) 1932-01-18

Family

ID=11245794

Family Applications (1)

Application Number Title Priority Date Filing Date
GB31294/30A Expired GB366516A (en) 1929-10-19 1930-10-18 Improved manufacture of food products and medicinal preparations from corn milling by-products

Country Status (1)

Country Link
GB (1) GB366516A (en)

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US7524522B2 (en) 2006-08-18 2009-04-28 Mor Technology, Llc Kernel fractionation system
US7612220B2 (en) 2006-08-18 2009-11-03 Mor Technology, Llc Carbon dioxide extraction of corn germ oil from corn germ
US8227012B2 (en) 2006-08-18 2012-07-24 Mor Technology, Llc Grain fraction extraction material production system
US8747931B2 (en) 2007-10-24 2014-06-10 Mor Supercritical, Llc Super critical fluid extraction and fractionation of bran extraction materials
US10486083B2 (en) 2016-04-06 2019-11-26 Kiinja Corporation Separator for fractional separation of supercritical carbon dioxide extracts
US11305212B2 (en) 2016-04-06 2022-04-19 Kiinja Corporation Multifunctional vessels for extraction and fractionation of extracts from biomass

Cited By (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US7524522B2 (en) 2006-08-18 2009-04-28 Mor Technology, Llc Kernel fractionation system
US7612220B2 (en) 2006-08-18 2009-11-03 Mor Technology, Llc Carbon dioxide extraction of corn germ oil from corn germ
US8227012B2 (en) 2006-08-18 2012-07-24 Mor Technology, Llc Grain fraction extraction material production system
US8551553B2 (en) 2006-08-18 2013-10-08 Mor Technology, Llc Grain endosperm extraction system
US8603328B2 (en) 2006-08-18 2013-12-10 Mor Supercritical, Llc Carbon dioxide corn germ oil extraction system
US8747106B2 (en) 2006-08-18 2014-06-10 Mor Technology, Llc Power production using grain fractionation products
US8747931B2 (en) 2007-10-24 2014-06-10 Mor Supercritical, Llc Super critical fluid extraction and fractionation of bran extraction materials
US10486083B2 (en) 2016-04-06 2019-11-26 Kiinja Corporation Separator for fractional separation of supercritical carbon dioxide extracts
US10625175B2 (en) 2016-04-06 2020-04-21 Kiinja Corporation Extractor for high pressure extraction of a matrix
US11235261B2 (en) 2016-04-06 2022-02-01 Kiinja Corporation Separator for fractional separation of supercritical carbon dioxide extracts
US11305212B2 (en) 2016-04-06 2022-04-19 Kiinja Corporation Multifunctional vessels for extraction and fractionation of extracts from biomass
US11478726B2 (en) 2016-04-06 2022-10-25 Kiinja Corporation Extractor for high pressure extraction of a matrix

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