GB486163A - Improvements in or relating to the treatment of distillery slop - Google Patents
Improvements in or relating to the treatment of distillery slopInfo
- Publication number
- GB486163A GB486163A GB9755/37A GB975537A GB486163A GB 486163 A GB486163 A GB 486163A GB 9755/37 A GB9755/37 A GB 9755/37A GB 975537 A GB975537 A GB 975537A GB 486163 A GB486163 A GB 486163A
- Authority
- GB
- United Kingdom
- Prior art keywords
- solids
- cloth
- slop
- rye
- barley
- 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
- 239000007787 solid Substances 0.000 abstract 10
- 239000004744 fabric Substances 0.000 abstract 7
- VTYYLEPIZMXCLO-UHFFFAOYSA-L Calcium carbonate Chemical compound [Ca+2].[O-]C([O-])=O VTYYLEPIZMXCLO-UHFFFAOYSA-L 0.000 abstract 6
- 239000000706 filtrate Substances 0.000 abstract 6
- VLKZOEOYAKHREP-UHFFFAOYSA-N n-Hexane Chemical compound CCCCCC VLKZOEOYAKHREP-UHFFFAOYSA-N 0.000 abstract 6
- 239000007788 liquid Substances 0.000 abstract 5
- CSCPPACGZOOCGX-UHFFFAOYSA-N Acetone Chemical compound CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 abstract 4
- RTZKZFJDLAIYFH-UHFFFAOYSA-N Diethyl ether Chemical compound CCOCC RTZKZFJDLAIYFH-UHFFFAOYSA-N 0.000 abstract 4
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 abstract 4
- 241000209219 Hordeum Species 0.000 abstract 4
- 235000007340 Hordeum vulgare Nutrition 0.000 abstract 4
- 241000209056 Secale Species 0.000 abstract 4
- 235000007238 Secale cereale Nutrition 0.000 abstract 4
- 240000008042 Zea mays Species 0.000 abstract 4
- 235000016383 Zea mays subsp huehuetenangensis Nutrition 0.000 abstract 4
- 235000002017 Zea mays subsp mays Nutrition 0.000 abstract 4
- 235000013339 cereals Nutrition 0.000 abstract 4
- 238000000855 fermentation Methods 0.000 abstract 4
- 230000004151 fermentation Effects 0.000 abstract 4
- 238000001914 filtration Methods 0.000 abstract 4
- 235000009973 maize Nutrition 0.000 abstract 4
- 238000012216 screening Methods 0.000 abstract 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract 4
- JVTAAEKCZFNVCJ-UHFFFAOYSA-M Lactate Chemical compound CC(O)C([O-])=O JVTAAEKCZFNVCJ-UHFFFAOYSA-M 0.000 abstract 3
- 238000009835 boiling Methods 0.000 abstract 3
- 229910000019 calcium carbonate Inorganic materials 0.000 abstract 3
- 239000003153 chemical reaction reagent Substances 0.000 abstract 3
- 238000010438 heat treatment Methods 0.000 abstract 3
- 239000003921 oil Substances 0.000 abstract 3
- 230000001376 precipitating effect Effects 0.000 abstract 3
- 241000283690 Bos taurus Species 0.000 abstract 2
- XSTXAVWGXDQKEL-UHFFFAOYSA-N Trichloroethylene Chemical group ClC=C(Cl)Cl XSTXAVWGXDQKEL-UHFFFAOYSA-N 0.000 abstract 2
- 238000005660 chlorination reaction Methods 0.000 abstract 2
- 238000000605 extraction Methods 0.000 abstract 2
- 239000012065 filter cake Substances 0.000 abstract 2
- JVTAAEKCZFNVCJ-UHFFFAOYSA-N lactic acid Chemical compound CC(O)C(O)=O JVTAAEKCZFNVCJ-UHFFFAOYSA-N 0.000 abstract 2
- 239000010865 sewage Substances 0.000 abstract 2
- 239000002904 solvent Substances 0.000 abstract 2
- 239000000470 constituent Substances 0.000 abstract 1
- 230000000694 effects Effects 0.000 abstract 1
- 235000014655 lactic acid Nutrition 0.000 abstract 1
- 239000004310 lactic acid Substances 0.000 abstract 1
- 239000000047 product Substances 0.000 abstract 1
Classifications
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23K—FODDER
- A23K10/00—Animal feeding-stuffs
- A23K10/30—Animal feeding-stuffs from material of plant origin, e.g. roots, seeds or hay; from material of fungal origin, e.g. mushrooms
- A23K10/37—Animal feeding-stuffs from material of plant origin, e.g. roots, seeds or hay; from material of fungal origin, e.g. mushrooms from waste material
- A23K10/38—Animal feeding-stuffs from material of plant origin, e.g. roots, seeds or hay; from material of fungal origin, e.g. mushrooms from waste material from distillers' or brewers' waste
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P60/00—Technologies relating to agriculture, livestock or agroalimentary industries
- Y02P60/80—Food processing, e.g. use of renewable energies or variable speed drives in handling, conveying or stacking
- Y02P60/87—Re-use of by-products of food processing for fodder production
Landscapes
- Life Sciences & Earth Sciences (AREA)
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Polymers & Plastics (AREA)
- Animal Husbandry (AREA)
- Molecular Biology (AREA)
- Mycology (AREA)
- Physiology (AREA)
- Health & Medical Sciences (AREA)
- Zoology (AREA)
- Botany (AREA)
- Biotechnology (AREA)
- Food Science & Technology (AREA)
- Fats And Perfumes (AREA)
- Processing Of Solid Wastes (AREA)
- Preparation Of Compounds By Using Micro-Organisms (AREA)
Abstract
Oils are extracted from the distillery slop obtained by fermentation of grain (e.g. maize, rye, barley) to produce alcohol. The slop is heated under a pressure sufficient to maintain it liquid above 240 DEG F., until it is continuously filtrable through cloth, and the solids are removed. Such heating may be at temperatures corresponding to the boiling points of water at suitable gauge pressures. Removal of solids takes place by filtration through cloth, with or without the use of filter aids, when oil is obtained from the filter cake by extraction with solvents such as acetone, ether, hexane, trichlorethylene, which may be preceded by screening, e.g. through an 8-mesh screen.ALSO:Lactic acid is recovered from the liquid constituents of distillery slop obtained by fermentation of grain (e.g. maize, rye, barley) to produce alcohol. The slop is heated under a pressure sufficient to maintain it liquid above 240 DEG F., until it is continuously filterable through cloth, and the solids are removed. Such heating may be at temperatures corresponding to the boiling points of water at suitable gauge pressures. Removal of solids may take place by settling, or by filtration, which may be preceded by screening, e.g. through an 8-mesh screen. The filtrate is mixed with a reagent, e.g. calcium carbonate, for precipitating an insoluble lactate, which may be filtered off.ALSO:Distillery slop obtained by fermentation of grain (e.g. maize, rye, barley) to produce alcohol is heated under a pressure sufficient to maintain it liquid above 240 DEG F., until it is continuously filtrable through cloth, and the solids are removed. Removal of solids may take place by centrifuging, by settling, or by filtration, e.g. through cloth, maybe without the use of filter aids, which may be preceded by screening, e.g. through an 8-mesh screen, and may be followed by a sewage disposal system such as a trickle filter or by chlorination. Part of the filtrate may be mixed with a reagent, e.g. calcium carbonate, for precipitating an insoluble lactate, which may be filtered off and part of this or the original or both filtrates may be concentrated and re-fermented.ALSO:Distillery slop obtained by fermentation of grain (e.g. maize, rye, barley) to produce alcohol is heated under a pressure sufficient to maintain it liquid above 240 DEG F., until it is continuously filtrable through cloth, and the solids are removed. Such heating may be at temperatures corresponding to the boiling points of water at suitable gauge pressures. Removal of solids may take place by centrifuging, by settling, or by filtration, e.g. through cloth, maybe without the use of filter aids (when oil may be obtained from the filter cake by pressing or by extraction with solvents such as acetone, ether, hexane, trichlorethylene), which steps may be preceded by screening, e.g. through an 8-mesh screen (when the solids may be dried for cattle fodder), and may be followed by a sewage disposal system such as a trickle filter or by chlorination. Part of the filtrate may be mixed with a reagent, e.g. calcium carbonate, for precipitating an insoluble lactate, which may be filtered off and part of this or the original or both filtrates may be concentrated and re-fermented. The filtrate may be concentrated in a multiple effect evaporator to 70-80 per cent solid content, and the residual water removed in a heat drier; the dried product may be used as cattle fodder.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| GB9755/37A GB486163A (en) | 1937-04-06 | 1937-04-06 | Improvements in or relating to the treatment of distillery slop |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| GB9755/37A GB486163A (en) | 1937-04-06 | 1937-04-06 | Improvements in or relating to the treatment of distillery slop |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| GB486163A true GB486163A (en) | 1938-05-31 |
Family
ID=9878153
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| GB9755/37A Expired GB486163A (en) | 1937-04-06 | 1937-04-06 | Improvements in or relating to the treatment of distillery slop |
Country Status (1)
| Country | Link |
|---|---|
| GB (1) | GB486163A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2011089494A1 (en) | 2010-01-20 | 2011-07-28 | Graeme Douglas Coles | Feed supplement and method |
| US9113645B2 (en) | 2006-09-26 | 2015-08-25 | Novita Nutrition, Llc | Solvent extraction of oil from distillers dried grains and methods of using extraction products |
-
1937
- 1937-04-06 GB GB9755/37A patent/GB486163A/en not_active Expired
Cited By (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US9113645B2 (en) | 2006-09-26 | 2015-08-25 | Novita Nutrition, Llc | Solvent extraction of oil from distillers dried grains and methods of using extraction products |
| US9523062B2 (en) | 2006-09-26 | 2016-12-20 | Novita Nutrition, Llc | Solvent extraction of oil from distillers dried grains and methods of using extraction products |
| US10072232B2 (en) | 2006-09-26 | 2018-09-11 | Novita Nutrition, Llc | Solvent extraction of oil from distillers dried grains and methods of using extraction products |
| US10696921B2 (en) | 2006-09-26 | 2020-06-30 | Novita Nutrition, Llc | Solvent extraction of oil from distillers dried grains and methods of using extraction products |
| US11136508B2 (en) | 2006-09-26 | 2021-10-05 | Novita Nutrition, Llc | Solvent extraction of oil from distillers dried grains and methods of using extraction products |
| US11412761B2 (en) | 2006-09-26 | 2022-08-16 | Novita Nurtition, LLC | Solvent extraction of oil from distillers dried grains and methods of using extraction products |
| US11638433B2 (en) | 2006-09-26 | 2023-05-02 | Novita Nutrition, Llc | Solvent extraction of oil from distillers dried grains and methods of using extraction products |
| US11653675B2 (en) | 2006-09-26 | 2023-05-23 | Novita Nutrition, Llc | Solvent extraction of oil from distillers dried grains and methods of using extraction products |
| WO2011089494A1 (en) | 2010-01-20 | 2011-07-28 | Graeme Douglas Coles | Feed supplement and method |
| AU2010343685B2 (en) * | 2010-01-20 | 2015-08-06 | Rich Technology Solutions Limited | Feed supplement and method |
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