| 序号 | 专利名 | 申请号 | 申请日 | 公开（公告）号 | 公开（公告）日 | 发明人 |
|---|---|---|---|---|---|---|
| 41 | 砂糖の製造方法 | JP2010529761 | 2009-09-15 | JPWO2010032724A1 | 2012-02-09 | 小原 聡; 聡 小原; 杉本 明; 明 杉本; 義文 寺島 |
| 本発明は、効率よく砂糖を製造し、同時に効率よくエタノールを製造する方法を提供することを目的とする。本発明は、蔗糖分解酵素を有さない微生物で植物由来の糖液を発酵させる前処理工程と、発酵させた糖液から砂糖を製造する工程とを有することを特徴とする砂糖の製造方法を提供する。また、本発明は、蔗糖分解酵素阻害剤の存在下で、植物由来の糖液を微生物で発酵させる前処理工程と、発酵させた糖液から砂糖を製造する工程とを有することを特徴とする砂糖の製造方法を提供する。 | ||||||
| 42 | Method for stably producing glucose syrup, and glucose mixed syrup, and method for supplying them | JP2007311061 | 2007-11-30 | JP2009131221A | 2009-06-18 | GOTO KATSUSHI; TAKADA MASAYASU; YAMAMOTO KEN; TAKEUCHI SHOGO; OKANE OSAMU; ITAKURA KENTO; UEHARA AYAKO; ENOMOTO KENICHI; WAKUI KAZUHIRO |
| <P>PROBLEM TO BE SOLVED: To provide a method for producing a glucose syrup or glucose mixed syrup with its concentration kept high, or with increased glucose level and without crystal precipitation, and to provide a method for supplying or storing the same. <P>SOLUTION: The method for producing and supplying a glucose syrup or a mixed syrup of glucose and fructose includes the steps of preparing a mixed solution of glucose and a glucooligosaccharide and/or sucrose, storing and/or transporting the mixed solution, and then breaking down the glucooligosaccharide and/or sucrose into monosaccharides by heating and/or enzymolysis. <P>COPYRIGHT: (C)2009,JPO&INPIT | ||||||
| 43 | Method of filtration dairy water flow | JP2001559275 | 2001-02-06 | JP2003522539A | 2003-07-29 | ジョナサン・ケー・ウェイル; スティーブン・エー・ロス; マイケル・スペイド |
| (57)【要約】 濾過法によるシアリルオリゴサッカリドの単離で遭遇される純度に関する特別な問題は、ラクトースからの分離である。 分子サイズの類似性のため、濾過による廃棄水流から、ラクトースの存在しないシアリルオリゴサッカリドを単離することはしばしば困難である。 従って、酪農水流から高い純度で、シアリルオリゴサッカリドを得るための濾過方法が所望されるであろう。 本発明は、シアリルオリゴサッカリドとラクトースとを含む酪農水流をプロセッシングする方法を提供することによりこの問題を解決し、ここでは酪農水流が、シアリルオリゴサッカリドの分離の前に、ラクトースの加水分解を果たすように処理される。 | ||||||
| 44 | Dextrose in powder form and its preparation | JP36839099 | 1999-12-24 | JP2000189075A | 2000-07-11 | MORALY FRANCK; LABERGERIE ERIK; LIS JOSE; LEFEVRE PHILIPPE |
| PROBLEM TO BE SOLVED: To obtain a dextrose in a powder form, suitable for industrial use, hardly causing the change in texture of a product, and useful in a field of sweets, especially for production of chocolate by increasing the content of the dextrose and its α-crystal form, decreasing the content of water and regulating compressibility so as to be within a specific range. SOLUTION: This dextrose in a powder form has at least 99% content of the dextrose, >=95% content of its α-crystal form, up to 1% water content, and >=80 N, preferably 100-200 N compressibility expressed in terms of the resistance against destruction of a tablet having a cylindrical shape with convex faces (having 14 mm radium of curvature), and 13 mm diameter, 6 mm thickness and 0.764 g weight, in other word 1.3 g/ml bulk density. A compound of the dextrose in the powder shape is preferably obtained by continuously granulating a dextrose powder mainly in the α-crystal form in a mixer-granulator or the like by using a binder such as water, and drying the obtained granules. | ||||||
| 45 | Composition and method for hydrolyzing complex carbohydrate | JP7322492 | 1992-02-25 | JPH0595800A | 1993-04-20 | KAARU JII HERAAKUBISUTO; KUREIGU EI DOOSHIERU |
| PURPOSE: To obtain the subject composition comprising each specific components, and useful for the analysis of unknown carbohydrates because of giving monosaccharides in high yield through hydrolyzing carbohydrates along with minimal decomposition of the monosaccharides. CONSTITUTION: This composition comprises (A) a volatile fluoro- or chloroaliphatic carboxylic acid (pref. trifluoroacetic acid), (B) an acylating agent (pref. acetic acid), and (C) an alkylating agent (e.g. an alcohol) or water (pref. water). This composition is intended for hydrolyzing and protecting the glycosidic bonds in carbohydrates (derivatives). COPYRIGHT: (C)1993,JPO | ||||||
| 46 | Separation of sugars | JP6985783 | 1983-04-20 | JPS58193700A | 1983-11-11 | JIYOSEFU JIEEMUZU ZUPANSHITSUK |
| 47 | JPS5840474B2 - | JP6129476 | 1976-05-28 | JPS5840474B2 | 1983-09-06 | MITSUSHERU SHUNAIDAA |
| 48 | Enzymatic use for converting organic substance to at least one other organic substance by enzynatic reaction | JP6129476 | 1976-05-28 | JPS51144787A | 1976-12-13 | MITSUSHIERU SHIYUNAIDAA |
| 49 | Solid agave syrup compositions | US14414627 | 2013-07-11 | US10144980B2 | 2018-12-04 | John Lawrence Rowe |
| The present invention relates to a agave syrup product having a low water content. The agave syrup product retains the physical and palatable properties of untreated agave syrup while having a prolonged shelf-life. It can be advantageously used to sweeten beverages (such as hot beverages) and in the manufacture of pharmaceutical compositions (such as throat lozenges) and/or confectionary. | ||||||
| 50 | CHROMATOGRAPHIC SEPARATION OF SACCHARIDES USING POLYMERIC MACROPOROUS ALKYLENE-BRIDGED RESIN | US15542128 | 2016-02-26 | US20180257003A1 | 2018-09-13 | Daryl J. Gisch; Christopher R. Eicher; Stephen Pease; Gongwei Pu |
| A method for chromatographically separating a first saccharide from a liquid eluent comprising the first saccharide and a second saccharide by passing the liquid eluent through a bed including a polymeric macroporous alkylene-bridged resin in calcium form. | ||||||
| 51 | SACCHARIFYING BIOMASS | US15935821 | 2018-03-26 | US20180209001A1 | 2018-07-26 | Marshall MEDOFF; Thomas Craig MASTERMAN |
| Biomass feedstocks (e.g., plant biomass, animal biomass, and municipal waste biomass) are processed to produce useful products, such as fuels. For example, systems are described that can convert feedstock materials to a sugar solution, which can then be fermented to produce ethanol. | ||||||
| 52 | Method for the hydrolysis of pelletizable biomasses using hydrohalic acids | US14435180 | 2013-10-11 | US10006098B2 | 2018-06-26 | Matthias Schmidt; Frank Kose |
| The invention relates to the hydrolytic breakdown of plant biomasses via hydrohalic acids, preferably so-called hydrochloric acid. Ligneous biomasses were preferably hydrolyzed in the past because other types of biomasses, for instance straw, are only able to be filled into the reactors with a very low density and they tend towards compacting in the course of the process. The invention solves this problem with two modifications. First of all, pelletizable biomasses are completely or partially loaded in the form of pellets and a heavily increasing filling density is achieved because of that. Secondly, the hydrolysis reactors are tilted, preferably arranged between 30° and 60°, and compacting is prevented. The economic effectiveness of both modifications is to be determined in practical tests for every pelletizable biomass. It is possible that one of the two modifications can be omitted. | ||||||
| 53 | INTEGRATED METHODS FOR TREATING LIGNOCELLULOSIC MATERIAL | US15573801 | 2016-05-25 | US20180148804A1 | 2018-05-31 | Robert Jansen; James Alan LAWSON; Noa LAPIDOT; Neta MATIS; Bassem HALLAC |
| The present disclosure relates to methods of processing lignocellulosic material to obtain cellulose and cellulose sugars. Also provided are compositions of cellulose hydrolysates. | ||||||
| 54 | Saccharifying biomass | US14498144 | 2014-09-26 | US09957580B2 | 2018-05-01 | Marshall Medoff; Thomas Craig Masterman |
| Biomass feedstocks (e.g., plant biomass, animal biomass, and municipal waste biomass) are processed to produce useful products, such as fuels. For example, systems are described that can convert feedstock materials to a sugar solution, which can then be fermented to produce ethanol. | ||||||
| 55 | Continuous Centrifuge Systems With Multiple-Stage Mixing | US15296667 | 2016-10-18 | US20180105889A1 | 2018-04-19 | Steven Myers; Graham Vidler; William Temple |
| The present disclosure includes a centrifuge system for processing a massecuite composition. The centrifuge system may include a centrifuge having a vertical spindle, a housing, and a basket disposed within the housing. The basket may include a central hub coupled to the vertical spindle for rotation therewith, a cup coupled to the central hub or an end of the vertical spindle, and a loading cone positioned over the cup and coupled to the cup by a plurality of vanes extending outward from the cup to the loading cone. The loading cone may have a wide end open towards a bottom of the basket, and the plurality of vanes may be radially spaced apart. The centrifuge system may further include a feed pipe vertically disposed above the cup and having a feed outlet oriented towards the cup. The cup defining a cavity oriented in a direction away from the central hub. | ||||||
| 56 | Method of producing sugar solution | US14395231 | 2013-04-25 | US09926613B2 | 2018-03-27 | Junpei Kishimoto; Hiroyuki Kurihara; Atsushi Minamino; Katsushige Yamada |
| A method of producing a sugar liquid includes filtering a sugar liquid through a nanofiltration membrane and collecting a sugar liquid from the feed side, wherein a sugar liquid containing an organic liquid compound having a relative dielectric constant of not less than 17 at 25° C. is filtered through the nanofiltration membrane. | ||||||
| 57 | CHROMATOGRAPHIC SEPARATION OF SACCHARIDES USING STRONG ACID EXCHANGE RESIN INCORPORATING PRECIPITATED BARIUM SULFATE | US15540493 | 2016-02-26 | US20180001313A1 | 2018-01-04 | Daryl J. GISCH; Christopher R. EICHER |
| A method for chromatographically separating a first saccharide from a liquid eluent comprising the first saccharide and a second saccharide by passing the liquid eluent through a bed comprising a gel-type strong acid cation exchange resin in calcium form, wherein precipitated barium sulfate is incorporated within the resin. | ||||||
| 58 | Methods for treating lignocellulosic materials | US14537530 | 2014-11-10 | US09783861B2 | 2017-10-10 | Robert Jansen; Philip Travisano; Lee Madsen; Neta Matis; James Alan Lawson; Noa Lapidot; Aharon M. Eyal; Timothy Allen Bauer; Ziv-Vladimir Belman; Bassem Hallac; Michael Zviely |
| The present invention relates to methods of processing lignocellulosic material to obtain hemicellulose sugars, cellulose sugars, lignin, cellulose and other high-value products. Also provided are hemicellulose sugars, cellulose sugars, lignin, cellulose, and other high-value products. | ||||||
| 59 | Tagatose production from deproteinized whey and purification by continuous chromatography | US13916021 | 2013-06-12 | US09150938B2 | 2015-10-06 | Anil R. Oroskar |
| Disclosed is a process for the production of d-tagatose from deproteinized whey or whey permeate containing lactose after acid hydrolysis to provide a hydrolysate comprising 1 equivalent of d-glucose and 1 equivalent of d-galactose for each unit of lactose converted. More particularly, the invention relates to a process for the isomerization of d-galactose to d-tagatose and the use of a simplified separation scheme based on simulated moving bed (SMB) separation. The isomerization of d-galactose to d-tagatose is carried out in the presence of calcium oxide or calcium hydroxide. The process is useful for providing a simplified processing route to providing pure d-tagatose and glucose syrup as two products from lactose hydrolysate isomerate. D-tagatose is useful as a food additive, as a sweetener, as a texturizer, as a stabilizer, or as a humectant. | ||||||
| 60 | METHOD FOR PRODUCING SWEETENER COMPOSITIONS AND SWEETENER COMPOSITIONS | US14440975 | 2013-10-23 | US20150275319A1 | 2015-10-01 | Avraham Baniel |
| The invention provides a method for producing a sweetener component comprising forming a syrup selected from the group consisting of 70%-95% glucose with water, 70%-95% fructose with water and 70%-95% sucrose with water at a temperature below 140° C., dissolving up to 30% nano-cellulose therein and cooling to form a substantially clear solid which solid can then be pulverized to form a granular sweetener composition, wherein when the solid contains up to 9% nanocellulose it is then ground to be used per se as a sweetener, while when the solid contains from 9% to 30% nanocellulose it is ground together with an additional amount of granulated sweetener selected from the group consisting of sucrose, fructose and glucose or a comestible granular component requiring sweetening and combinations thereof to form a granular composition containing between 2 and 10% nanocellulose. | ||||||
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