| 序号 | 专利名 | 申请号 | 申请日 | 公开（公告）号 | 公开（公告）日 | 发明人 |
|---|---|---|---|---|---|---|
| 181 | Biopolymer structures and parts | JP2006533765 | 2004-06-14 | JP2007517078A | 2007-06-28 | マイケル・ジェー・リーベル; ミルトン・ジェー・リーベル |
| 本発明は、組成物に関するものであり、それは、発酵固体およびサーモアクティブ材料を含むバイオポリマーとして参照される。 本発明はまた、発酵固体およびサーモアクティブ材料を配合することから成るバイオポリマーを作る方法を含む。 本バイオポリマーは、工場の製品に成形することができる。 そのような工場の製品を成形する方法は、たとえば押出し加工、射出成形、または発酵固体とサーモアクティブ材料を配合することを含む。 バイオポリマーから成形された構造体は、木材代替品、窓部品、ドア部品、サイディング組立て材および他の構造体を含むことができる。 | ||||||
| 182 | Method for producing plant extract | JP2005110500 | 2005-04-07 | JP2006290756A | 2006-10-26 | WATANABE TAKEHIRO; FUJITA RUMI; TAGASHIRA MOTOYUKI; KANDA TOMOMASA; HIGUCHI SEIICHI; TANABE MASAYUKI |
| <P>PROBLEM TO BE SOLVED: To provide a technique for efficiently producing high-purity water-soluble polyphenols in a short time from e.g. hop bracts obtained as a byproduct in a beer brewing process. <P>SOLUTION: A method for producing a refined plant extract is provided, comprising treating a plant extract with a clay mineral such as bentonite to remove bivalent cations therefrom. A method for producing polyphenols is provided, comprising passing such a refined plant extract through a column to adsorb polyphenols to the column followed by passing a solvent through the column to elute the aimed water-soluble polyphenols. A method for producing water-soluble hop bract polyphenols is also provided, comprising the step of adding bentonite to a hop bract extract liquid and leaving the resultant liquid at rest under acidic conditions, the step of making a solid-liquid separation to obtain a supernatant, and the step of subjecting the supernatant to column refining, cooling the resultant polyphenol fraction supernatant and leaving it at rest to deposit water-insoluble components followed by making a solid-liquid separation. <P>COPYRIGHT: (C)2007,JPO&INPIT | ||||||
| 183 | Steam reformer that accompanied the internal hydrogen purification | JP52264399 | 1998-10-14 | JP3454362B2 | 2003-10-06 | エドランド，ディヴィッド・ジェイ; プレッジャー，ウィリアム・エイ |
| 184 | Wet brewer's grains husks peeling method and apparatus | JP17456394 | 1994-07-26 | JP2834407B2 | 1998-12-09 | KISHI SOTARO; SHIBA YOSHIO; MYAKE HIDEKAZU; UIRUHERUMU KYUNTSUERU |
| 185 | Ethanol denaturating agent | JP10419398 | 1998-04-01 | JPH10287601A | 1998-10-27 | MANSFELD GERD; OELKERS EGON; PETERS KLAUS |
| PROBLEM TO BE SOLVED: To obtain an ethanol denaturating agent having a similar denaturating effect to that of diethylphthalate and a weak peculiar smell capable of harmonizing with all aromatizing components. SOLUTION: This ethanol modifying agent is obtained by containing the following A to G; A. 50-250 pt.wt. benzyl salicylate, B. 5-40 pt.wt. (i) 4,6,6,7,8,8 hexamethyl-1,3,4,6,7,8-hexahydrocyclopenta[g]benzopyran or (ii) oxacyclohexadeca-12- and/or -13-en-one, each of which may be dissolved in 5-40 pt.wt. (E and/or F), C. 10-100 pt.wt. a 1-4 C alkylester of a hydrogenated root oil, D. 40-240 pt.wt. 2-pentylphenylpropanol, E. 200-500 pt.wt. benzyl benzoate, F. 100-400 pt.wt. dipropylene glycol, and G. 150-300 pt.wt. triethyl citrate. COPYRIGHT: (C)1998,JPO | ||||||
| 186 | Separation of yeast from fermentation broth of fermentation tank | JP15566584 | 1984-07-27 | JPS6058066A | 1985-04-04 | MUELLER HANS |
| 1. A process for separation of yeasts from fermentation broths of a fermentation tank (1) particularly for the production of compressed yeast for baking purposes, as well as compressed yeast from alcoholic fermentation which accrues in the production of alcohol, wine and beer, characterised in that the fermentation broth is forced through a pressure filter with filter elements (30) freely suspended within a filter vessel (21) the filter elements (30) of which are covered with fine filter fabrics or membranes, that after the build-up of a filter cake, the filter vessel (21) is drained of the residual liquid, the yeast filter cake is washed with water, blown out with compressed air or another compressed gas and freed from the filter fabrics by means of a pressure surge with compressed gas in the opposite direction to that of filtration and extracted from the filter vessel (21). | ||||||
| 187 | JPS5850633B2 - | JP8663776 | 1976-07-22 | JPS5850633B2 | 1983-11-11 | PIEERU KONBU; JAN RADEI |
| 188 | JPS5835660B2 - | JP10216274 | 1974-09-06 | JPS5835660B2 | 1983-08-04 | JAN MANII; SHARURU MONTAN; PIEERU REINOO; SHARURU GONCHE; JATSUKU DARUDENNU |
| 189 | Recovery of concentrated alcohol waste liquid | JP9955781 | 1981-06-25 | JPS5754589A | 1982-04-01 | FURIIDORITSUHI YOSEFU TSUTSUKA; GEORUKU OSUTOHAUSU |
| 190 | JPS50134836A - | JP2793075 | 1975-03-07 | JPS50134836A | 1975-10-25 | |
| 191 | JPS5075862A - | JP10216274 | 1974-09-06 | JPS5075862A | 1975-06-21 | |
| 192 | JPS5030150A - | JP3937974 | 1974-04-06 | JPS5030150A | 1975-03-26 | |
| 193 | SPENT SOLIDS PROCESSING | PCT/GB2013053026 | 2013-11-15 | WO2014076494A3 | 2014-08-07 | ROSS JOHN MORRIS; LYNCH CORNELIUS MARTIN |
| The present invention provides a process for producing biogas and/or methane from solid spent products derived from, for example, the mashing process of malt whisk(e)y and/or beer production, processing of sugar or other industrial processes. There is also provided a system for producing biogas and/or methane from solid spent products derived from, for example, the mashing process of malt whisk(e)y and/or beer production, processing of sugar or other industrial processes. | ||||||
| 194 | BIOADHESIVES AND PROCESSES FOR MAKING SAME | PCT/US2013026440 | 2013-02-15 | WO2013123397A3 | 2013-11-21 | RIEBEL MICHAEL J; WINSNESS DAVID J; KREISLER KEVIN E; DAHMES FORREST L |
| A dried distiller soluble based bioadhesive composition and method for producing the dried distiller soluble based bioadhesives are disclosed, as well as derivatives thereof. The produced dried distillers solubles derives from co-products of corn fermentation facilities, and is advantageously comprised in part of water-soluble proteins. The method for producing the dried distillers solubles generally involves separation and/or introduction of targeted constituents and/or physiochemical treatment to facilitate use as an adhesive. Use of the method and bioadhesive compositions disclosed herein will improve the economics of fermentation by increasing co-product value, reducing plant-wide energy utilization, decreasing waste and emissions, and increasing overall product yield from each bushel of corn consumed. | ||||||
| 195 | INTEGRATED PROCESS OF FILTRATION TO DRY BREWER'S SPENT GRAIN | PCT/PT2010000016 | 2010-04-05 | WO2010117288A1 | 2010-10-14 | CARVALHO JORGE MANUEL RODRIGUES DE; MACHADO REMIGIO DE MATOS; RODRIGUES RICARDO ANNDRLE DUARTE; HENRIQUES CARLOS MIGUEL CARVALHO; CORREIA PAULO FERNANDO MARTINS DE MAGALHAES |
| The present invention relates to a process and the corresponding equipment, which is able to dehydrate the brewer's spent grain (BSG), from 72 - 85% to 15% moisture, resulting in a stabilized product with the same protein, fibre and lipid content. The dehydration process involves several stages, two of which are mechanical (filtration and membrane squeezing) and a last one which consists in vacuum drying using hot water or low pressure water vapour as heat source. The energy for the process is available at zero cost in the brewing industry, through the use of the process hot water, or the low pressure vapour coming from the co-generation units. The dehydrated BSG is a stabilized product and may be used as food for humans and for animals, ruminants and non- ruminants, and as raw material for biotechnological and pharmaceutical applications. | ||||||
| 196 | METHOD AND DEVICE FOR PRODUCING ELECTRICITY AND CONVERSION PRODUCTS, SUCH AS ETHANOL | PCT/NL2009000056 | 2009-03-06 | WO2009110790A3 | 2010-06-24 | SANDERS JOHAN PIETER MARINUS; MEESTERS KOEN PETER HENRI; VAN DEN BROEK JOHANNES GERARDUS BERNARDUS |
| The invention relates to a method for producing electricity and conversion products such as ethanol, comprising the steps of: i) separating a starch source into a starch-rich fraction and a residual fraction; ii) heating the starch-rich fraction for the purpose of gelling the starch; iii) releasing the gelled starch from the starch-rich fraction; iva) converting the gelled starch enzymatically into sugars; ivb) converting the sugars fermentatively into the conversion products; v) further processing the conversion products from the conversion medium; vi) generating biogas from residual fraction; vii) generating electricity and heat from biogas and/or residual fraction via cogeneration of heat and electricity; and viii) using the generated heat in one or more steps i) to vi). | ||||||
| 197 | METHOD AND DEVICE FOR DRYING BYPRODUCTS | PCT/EP2008000978 | 2008-02-08 | WO2008095722B1 | 2008-12-18 | CASPERS GERALD; KLEIN CHRISTIAN; KRELL LOTHAR |
| The invention relates to a method and to a device for drying byproducts which are obtained during the treatment of raw materials containing starch and sugar, in particular after the fermentation and distillation thereof. According to the invention, the byproduct is fractionated in a clarifying phase having a high liquid portion and in a thickening phase. Said thickening phase is transformed, according to a conditioning method, into particles having a uniform geometry and said particles are dried in a pneumatic fluidised bed drying system having a relative intergranular void volume in the fluidised bed of between 0.5 and 0.92. | ||||||
| 198 | OIL RECOVERY FROM DRY CORN MILLING ETHANOL PRODUCTION PROCESSES | PCT/US2007084633 | 2007-11-14 | WO2008061120A3 | 2008-09-25 | RANDHAVA SARABJIT; KAO RICHARD L; CALDERONE STEVEN G; RANDHAVA AJAIB S |
| A corn oil extraction process is disclosed. The process includes the recovery of corn oil and other co-products, including but not limited to steam, electric power and chemicals, from an ethanol production process and in particular, a process that involves dry corn milling methods. The process involves extraction of oil from milled corn and residues from the fermentation step, including thick stillage, distillers wet grain, distillers dry grain and distillers dry grains with solubles, by the application of an alkyl acetate, phase separation and recovery of the separated matter. A process of drying wet co-product using ethanol and carbon dioxide from the production facility is also disclosed. | ||||||
| 199 | DIETARY FIBRES | PCT/IB2007052769 | 2007-07-11 | WO2008010156A2 | 2008-01-24 | ERASMUS CORINDA |
| A process (10) for obtaining a valuable product from plant material (58) comprising both proteinaceous material and fibrous material includes brushing or scrubbing the plant material in a wet condition in a separation stage (12) against a separation medium, thereby forcing proteinaceous material through the separation medium and retaining fibrous material on the separation medium, and withdrawing a fibre-rich product and a protein-rich product (35) from the separation stage (12). | ||||||
| 200 | STEAM REFORMER WITH INTERNAL HYDROGEN PURIFICATION | PCT/US9821670 | 1998-10-14 | WO9919456A8 | 1999-07-08 | EDLUND DAVID J; PLEDGER WILLIAM A |
| A steam reformer with internal hydrogen purification includes internal bulk hydrogen purification, internal hydrogen polishing to remove trace levels of carbon monoxide and carbon dioxide, an integrated combustion method utilizing waste gas to heat the reformer, efficient integration of heat transfer and a compact design. The steam reformer includes a concentric cylindrical architecture with the outermost shell (50) nesting an annular combustion region (60), and annular reforming region (62), and annular hydrogen transport region (54) and cylindrical polishing region (56). | ||||||
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