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-productsInfo
- 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
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C11—ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
- C11B—PRODUCING, 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
- C11B1/00—Production of fats or fatty oils from raw materials
- C11B1/10—Production 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.
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)
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 |
-
1930
- 1930-10-18 GB GB31294/30A patent/GB366516A/en not_active Expired
Cited By (12)
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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