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    A PROCESS FOR THE PRODUCTION OF SOYBEAN SUGARS AND THE PRODUCT PRODUCED THEREOF
    2.
    发明申请
    A PROCESS FOR THE PRODUCTION OF SOYBEAN SUGARS AND THE PRODUCT PRODUCED THEREOF 审中-公开
    一种生产大豆糖及其生产产品的方法

    公开(公告)号：WO03056933A2

    公开(公告)日：2003-07-17

    申请号：PCT/IL0200902

    申请日：2002-11-11

    Applicant: OLADUR LTD ,  CEGLA URIEL G ,  SHUSTER MOSHE

    Inventor： CEGLA URIEL G ,  SHUSTER MOSHE

    IPC: A23J7/00 ,  C11B9/02 ,  C13B35/02 ,  C13B35/06 ,  C13B50/00 ,  C13F3/00 ,  C13J1/02 ,  C13J1/06

    CPC classification number: C13B35/02 ,  A23J7/00 ,  C11B9/025 ,  C13B35/06 ,  C13B50/006

    Abstract: The present invention relates to a method for utilizing soy molasses as a source for soy sugars which are of high oligosaccharaide content. The invention provides a method for purifying soy molasses comprising the following steps: (i) contacting the soy molasses with alcohol and hydrocarbon solvent mixture, thereby two layers comprising a lower aqueous-alcohol layer and an upper hydrocarbon layer are formed; (ii) collecting the lower aqueous- alcohol layer; (iii) removing coloring, off-flavor and odorous substances; and (iv) removing minerals, thereby a purified soy molasses of more than 90wt.% sugars, on dry matter basis, is obtained.

    Abstract translation: 本发明涉及利用大豆糖蜜作为高糖寡糖含量的大豆糖的来源的方法。 本发明提供了一种纯化大豆糖蜜的方法，包括以下步骤：（i）使大豆糖蜜与醇和烃溶剂混合物接触，由此形成包含下层含水醇层和上层烃层的两层; （ii）收集下层含水醇层; （iii）除去着色，异味和恶臭物质; 和（iv）去除矿物质，从而获得基于干物质的超过90重量％糖的纯化大豆废糖。

    IMPROVED SUCROSE INVERSION PROCESS
    4.
    发明申请
    IMPROVED SUCROSE INVERSION PROCESS 审中-公开
    改进的SUCROSE反转过程

    公开(公告)号：WO2008097878A2

    公开(公告)日：2008-08-14

    申请号：PCT/US2008052877

    申请日：2008-02-04

    Applicant: TATE & LYLE INGREDIENTS ,  JANSEN ROBERT ,  KERR JOHN ,  BAIADA ANTHONY

    Inventor： JANSEN ROBERT ,  KERR JOHN ,  BAIADA ANTHONY

    IPC: C13B20/14 ,  C13K3/00 ,  C13B35/06

    CPC classification number: C13K3/00 ,  C13B20/14

    Abstract: We disclose a method of inverting sucrose, including (i) determining an initial solids concentration of an aqueous sucrose solution (SoHdS1), an initial bed volume (BV1) of a sucrose inversion resin system, a minimum target inversion percentage (invert%min), a maximum target inversion percentage (invert%max), a target maximum hydroxymethylfuran (HMF) concentration (HMFmdX), a minimum target pH (pHmm), or a maximum target pH (pHmax); (ii) contacting the sucrose inversion resin system with the aqueous sucrose solution under conditions of aqueous solution flow rate in BV,/hr (ratep) and aqueous solution temperature in 0C (temperaturep) to produce an inverted sucrose solution having an inversion percentage (invert%product), an HMF concentration (HMFprocduct), and a pH (pHproduct); (iii) observing an instantaneous inversion percentage (invert%m!>t), an instantaneous HMF concentration (HMFmst), or an instantaneous pH (pHmst) of the inverted sucrose solution; and, if invert%m,t invert%max, HMFm%t > HMFmax, pHmst pHmax; (iv) changing at least one of the aqueous solution flow rate or the aqueous solution temperature such that invert%mm

    Abstract translation: 我们公开了蔗糖反转的方法，包括（i）测定蔗糖反相树脂体系的初始固体浓度（SoHdS1），初始床体积（BV1），最小目标反转百分比（反转百分比） ，最大目标反转百分比（反转百分比最大值），目标最大羟甲基呋喃浓度（HMFmdX），最小目标pH（pHmm）或最大目标pH（pHmax））; （ii）在水溶液流速BV，/ hr（速率）和0℃（温度p）的水溶液温度条件下，将蔗糖反转树脂体系与蔗糖水溶液接触，得到反转百分比反转蔗糖溶液 ％产品），HMF浓度（HMFprocduct）和pH（pH值））。 （iii）观察反转蔗糖溶液的瞬时反转百分比（反相％m> t），瞬时HMF浓度（HMFmst）或瞬时pH（pHmst）; 并且如果反转％m，t <反转％mm，反转％m％t>反相％max，HMFm％t> HMFmax，pHmst pHmax; （iv）改变水溶液流速或水溶液温度中的至少一个，使得转换百分比mm <反转％piodUct =反转％max，HMFprodllct = HMF1113x或pHimu

    A PROCESS FOR THE RECOVERY OF A BROWN FOOD-GRADE SUGAR PRODUCT FROM A SUGAR BEET SOLUTION
    5.
    发明申请
    A PROCESS FOR THE RECOVERY OF A BROWN FOOD-GRADE SUGAR PRODUCT FROM A SUGAR BEET SOLUTION 审中-公开
    从蔗糖饮料中回收棕色食品级产品的方法

    公开(公告)号：WO2007071729A3

    公开(公告)日：2007-09-13

    申请号：PCT/EP2006070008

    申请日：2006-12-20

    Applicant: DANISCO SUGAR AS ,  CARTER MELVIN P ,  JENSEN JOHN PREBEN

    Inventor： CARTER MELVIN P ,  JENSEN JOHN PREBEN

    IPC: C13B35/06 ,  C13B20/00 ,  C13B20/12 ,  C13B20/14 ,  C13B20/18 ,  C13B35/08 ,  C13B50/00

    CPC classification number: C13B35/06 ,  C13B20/123 ,  C13B20/14 ,  C13B20/18 ,  C13B35/08 ,  C13B50/008

    Abstract: The invention relates to a process for the recovery of a brown food-grade sugar product from sugar beet solutions, which can be obtained from various beet sugar process streams, such as thin juice, thick ju ice and molasses. The process com prises providing a sugar beet solution, which contains malodorous volatiles as a result of one or more purif ication processes; subjecting said sugar beet solution to electrodialysis to provide an electrodialyzed liquid, wherefrom malodorous volatiles are at least partly removed; and recovering from said electrodialyzed liquid a product selected from liquid and solid brown sugar products of food-grade and combinations thereof. The invention also relates to food-grade beet sugar products derived from a sugar beet solution. These products are suitable for substituting the corresponding cane sugar derived products. In a further aspect the invention relates to the use of electrodialysis for removing malodorous volatile components from a sugar beet solution.

    Abstract translation: 本发明涉及一种从糖用甜菜溶液中回收棕色食品级糖产品的方法，该方法可从各种甜菜糖加工料流中获得，如稀汁，浓ju冰糖和糖蜜。 该方法提供了甜菜溶液，其由于一种或多种净化过程而含有恶臭挥发物; 对所述甜菜溶液进行电渗析以提供电渗析液体，其中恶臭挥发物至少部分地被除去; 并从所述电渗析液中回收选自食品级的液体和固体红糖产品及其组合的产品。 本发明还涉及从甜菜溶液得到的食品级甜菜糖产品。 这些产品适用于替代相应的蔗糖衍生产品。 在另一方面，本发明涉及电渗析从糖用甜菜溶液中除去恶臭挥发性组分的用途。

    DIRECT PRODUCTION OF WHITE SUGAR FROM SUGARCANE JUICE OR SUGAR BEET JUICE
    6.
    发明申请
    DIRECT PRODUCTION OF WHITE SUGAR FROM SUGARCANE JUICE OR SUGAR BEET JUICE 审中-公开
    直接生产来自苏格兰酵母或糖果甜点的白糖

    公开(公告)号：WO2006050064A2

    公开(公告)日：2006-05-11

    申请号：PCT/US2005038883

    申请日：2005-10-26

    Applicant: SUPERVISOR OF LOUISIANA STATE ,  REIN PETER W ,  BENTO LUIS R S M ,  ELLIS BRUCE M

    Inventor： REIN PETER W ,  BENTO LUIS R S M ,  ELLIS BRUCE M

    IPC: C13B20/08 ,  C13B20/12 ,  C13B20/14 ,  C13B35/06

    CPC classification number: C13B20/123 ,  C13B20/08 ,  C13B20/142

    Abstract: An economical process is disclosed for the direct production of white sugar from clarified juice. Juice from a cane sugar mill, or sugar beet juice, is first contacted with hydrogen peroxide, before passing through granular activated carbon. The juice is then passed through cationic and anionic resins to remove inorganic compounds, colorants, and other impurities. Then the juice may be concentrated and sugar crystallized. White sugar is produced directly, without the need for an intermediate raw sugar crystallization.

    Abstract translation: 公开了用于从澄清果汁直接生产白糖的经济方法。 在通过颗粒活性炭之前，首先将甘蔗糖汁或甜菜汁的果汁与过氧化氢接触。 然后将果汁通过阳离子和阴离子树脂以除去无机化合物，着色剂和其它杂质。 然后果汁可能浓缩，糖结晶。 直接生产白糖，不需要中间原糖结晶。

    SYSTEM AND PROCESS FOR REFINING SUGAR
    7.
    发明申请
    SYSTEM AND PROCESS FOR REFINING SUGAR 审中-公开
    精制糖的系统和方法

    公开(公告)号：WO2013082018A8

    公开(公告)日：2014-07-03

    申请号：PCT/US2012066634

    申请日：2012-11-27

    Applicant: AMALGAMATED RES LLC

    Inventor： KEARNEY MICHAEL M ,  HIEB ALAN W ,  PRYOR TIMOTHY E ,  VELASQUEZ LAWRENCE

    IPC: C13B20/14 ,  C13B30/04 ,  C13B30/14 ,  C13B35/06

    CPC classification number: C13B50/00 ,  C13B20/14 ,  C13B30/04 ,  C13B30/14 ,  C13B35/06

    Abstract: A system (10, 110) and process for refining raw sugar, comprising a melting unit (16, 116) configured to receive the raw sugar and an eluent to produce a melt liquor, a decolorization unit (24, 124) configured to receive the melt liquor and to produce a fine liquor, a crystallization unit (36, 136) configured to fractionate high-purity crystalline sucrose from the fine liquor and to provide a run-off syrup, a softening unit (46, 146) configured to receive the run-off syrup to produce a softened syrup, at least one separation unit (48, 148) configured to receive the softened syrup to produce a low-invert sucrose product, and a recycle line (52, 152) configured to relay the low-invert sucrose product from the at least one separation unit (48, 148) to the melting unit (16, 116).

    Abstract translation: 一种系统（10,110）和用于精制原糖的方法，包括被配置成接收原糖的洗涤单元（16,116）和洗脱液以产生熔融液体;脱色单元（24,124） 熔化液体并产生细液;结晶单元（36,136），其被配置成从所述细液中分馏高纯度结晶蔗糖并提供流出液糖浆;软化单元（46,146），被配置为接收 径流糖浆以产生软化的糖浆，至少一个分离单元（48,148），其构造成接收软化糖浆以产生低转化蔗糖产物;以及再循环管线（52,152） 将蔗糖产物从至少一个分离单元（48,148）反转到熔化单元（16,116）。

    SEPARATION PROCESS
    8.
    发明申请
    SEPARATION PROCESS 审中-公开
    分离过程

    公开(公告)号：WO2011121179A1

    公开(公告)日：2011-10-06

    申请号：PCT/FI2011/050262

    申请日：2011-03-29

    Applicant: DANISCO A/S ,  AIRAKSINEN, Jyrki ,  PAANANEN, Hannu ,  LEWANDOWSKI, Jari ,  LAIHO, Kari

    Inventor： AIRAKSINEN, Jyrki ,  PAANANEN, Hannu ,  LEWANDOWSKI, Jari ,  LAIHO, Kari

    IPC: B01D15/18 ,  C13B20/14 ,  C13B35/06 ,  C07C229/12

    CPC classification number: C13B20/148 ,  B01D15/185 ,  C07C227/40 ,  C13K13/00 ,  C07C229/12

    Abstract: The invention relates to a multi-profile chromatographic sequential SMB process of separating and recovering betaine and sucrose from concentrated raw juice or thick juice. In the process of the invention, the betaine subprofile and the residual subprofile of successive separation profiles are overlapping. A sucrose fraction and a betaine fraction containing also residual components are recovered. Betaine is further separated from the betaine fraction for example by chromatographic processes.

    Abstract translation: 本发明涉及从浓缩的原汁或浓稠汁中分离和回收甜菜碱和蔗糖的多色谱色谱顺序SMB方法。 在本发明的过程中，甜菜碱子档案和连续分离谱的残留子档案重叠。 回收含有残留成分的蔗糖级分和甜菜碱级分。 甜菜碱例如通过色谱法从甜菜碱级分进一步分离。

    SIMULATED MOVING BED BLOCK DISPLACEMENT PROCEDURE
    10.
    发明申请
    SIMULATED MOVING BED BLOCK DISPLACEMENT PROCEDURE 审中-公开
    模拟移动板块位移程序

    公开(公告)号：WO98030724A1

    公开(公告)日：1998-07-16

    申请号：PCT/US1998/000115

    申请日：1998-01-06

    IPC: B01D15/18 ,  C13B20/14 ,  C13B35/06 ,  C13D3/14 ,  C13J1/06

    CPC classification number: C13B35/06 ,  B01D15/185 ,  B01D2215/023 ,  B01D2215/024 ,  C13B20/14

    Abstract: A "block" of betaine is displaced from the circulation loop of an ion exclusion system configured as an SMB without disturbing the normal operation of the system. In practice, a betaine-concentrated fraction is withdrawn (17) from the circulating loop of the SMB while an equal volume of water is introduced (15) to the loop. The circulation loop thereby continues without disruption.

    Abstract translation: 甜菜碱的“块”从配置为SMB的离子排斥系统的循环回路中移位，而不会干扰系统的正常操作。 实际上，将来自SMB的循环回路（17）的甜菜碱浓缩馏分从等体积的水（15）引入环中。 循环回路由此继续而不中断。

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