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    • 1. 发明申请
    • Sucralose production method
    • 三氯蔗糖生产方法
    • US20080234472A1
    • 2008-09-25
    • US12009455
    • 2008-01-18
    • Duane LeinhosJohn KerrBob JansenSebastien CamborieuxPeter Lloyd-JonesAnthony Baiada
    • Duane LeinhosJohn KerrBob JansenSebastien CamborieuxPeter Lloyd-JonesAnthony Baiada
    • C07H1/00
    • C07H5/02
    • There is provided a method for the production of sucralose from a feed stream resulting from the chlorination of a sucrose-6-acylate in a reaction vehicle, said feed stream comprising a sucralose-6-acylate, the reaction vehicle, and by-products including high molecular weight coloured material, said method comprising: deacylation of the sucralose-6-acylate by treatment with a base to afford sucralose, and, before or after said deacylation, removal of the reaction vehicle and isolation of the sucralose characterised in that immediately before the removal of the reaction vehicle, the reaction stream is subjected to a precipitation step comprising treatment with a metal or ammonium hydroxide and carbon dioxide to form a precipitate of the corresponding metal or ammonium carbonate in which at least a portion of said high molecular weight coloured material is trapped, followed by separation of said precipitate.
    • 提供了从反应载体中的蔗糖-6-酰化物氯化得到的进料流中生产三氯蔗糖的方法,所述进料流包含三氯半乳蔗糖-6-酰化物,反应载体和副产物,包括 所述方法包括:用碱处理三氯半乳蔗糖-6-酰化物脱酰基,得到三氯半乳蔗糖,并且在所述脱酰化之前或之后,除去反应载体和分离三氯半乳蔗糖,其特征在于,紧接在之前 去除反应载体,将反应物流进行沉淀步骤,包括用金属或氢氧化铵和二氧化碳处理以形成相应的金属或碳酸铵的沉淀物,其中至少部分所述高分子量着色 材料被捕获,然后分离所述沉淀物。
    • 8. 发明授权
    • Sucrose inversion process
    • 蔗糖反转过程
    • US08404109B2
    • 2013-03-26
    • US13316278
    • 2011-12-09
    • Robert JansenJohn KerrAnthony Baiada
    • Robert JansenJohn KerrAnthony Baiada
    • B01D17/12C13K3/00B01J14/00
    • C13K3/00C13B20/14
    • A method of inverting sucrose, including (i) determining an initial solids concentration of an aqueous sucrose solution, an initial bed volume of a sucrose inversion resin system, a minimum target inversion percentage, a maximum target inversion percentage, a target maximum hydroxymethylfuran (HMF) concentration, a minimum target pH, or a maximum target pH; (ii) contacting the sucrose inversion resin system with the aqueous sucrose solution under conditions of aqueous solution flow rate and aqueous solution temperature to produce an inverted sucrose solution having an inversion percentage, an HMF concentration, and a pH; (iii) observing an instantaneous inversion percentage, an instantaneous HMF concentration, or an instantaneous pH of the inverted sucrose solution; and, if appropriate; (iv) changing at least one of the aqueous solution flow rate or the aqueous solution temperature to yield a product having a desired inversion percentage, HMF concentration, and/or pH. An apparatus capable of performing the method.
    • 一种反相蔗糖的方法,包括(i)测定蔗糖水溶液的初始固体浓度,蔗糖反转树脂体系的初始床体积,最小目标反转百分比,最大目标反转百分比,目标最大羟甲基呋喃(HMF )浓度,最小目标pH或最大目标pH; (ii)在水溶液流动速率和水溶液温度条件下使蔗糖反转树脂体系与蔗糖溶液水溶液接触,以产生具有倒置百分比,HMF浓度和pH值的倒置蔗糖溶液; (iii)观察反转蔗糖溶液的瞬时反转百分比,瞬时HMF浓度或瞬时pH值; 并酌情; (iv)改变水溶液流速或水溶液温度中的至少一个,得到具有所需转化百分比,HMF浓度和/或pH值的产物。 一种能够执行该方法的装置。
    • 9. 发明授权
    • Sucrose inversion process
    • 蔗糖反转过程
    • US08092609B2
    • 2012-01-10
    • US12025153
    • 2008-02-04
    • Robert JansenJohn KerrAnthony Baiada
    • Robert JansenJohn KerrAnthony Baiada
    • C13K1/08
    • C13K3/00C13B20/14
    • We disclose a method of inverting sucrose, including (i) determining an initial solids concentration of an aqueous sucrose solution (solidsi), an initial bed volume (BVi) 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 (HMFmax), a minimum target pH (pHmin), 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 BVi/hr (ratep) and aqueous solution temperature in ° C. (temperaturep) to produce an inverted sucrose solution having an inversion percentage (invert %product), an HMF concentration (HMFproduct), and a pH (pHproduct); (iii) observing an instantaneous inversion percentage (invert %inst), an instantaneous HMF concentration (HMFinst), or an instantaneous pH (pHinst) of the inverted sucrose solution; and, if invert %inst invert %max, HMFinst>HMFmax, pHinst pHmax; (iv) changing at least one of the aqueous solution flow rate or the aqueous solution temperature such that invert %min≦invert %product≦invert %max, HMFproduct≦HMFmax, or pHmin≦pHproduct≦pHmax. We also disclose a computing apparatus capable of use in performing a method of inverting sucrose.
    • 我们公开了一种蔗糖翻转方法,包括(i)测定蔗糖反应树脂体系的初始固体浓度,蔗糖反转树脂体系的初始床体积(BVi),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(HMF)浓度(HMFmax),最小目标pH(pHmin)或最大目标pH(pHmax)); (ii)在水溶液流速(BVi / hr(速率))和水溶液温度(℃)(℃)下的条件下,将蔗糖反转树脂体系与蔗糖溶液的蔗糖溶液接触,得到反转百分比的倒转蔗糖溶液 转化%产物),HMF浓度(HMF产物)和pH(pH值产物); (iii)观察反转蔗糖溶液的瞬时反转百分率(反转%inst),瞬时HMF浓度(HMFinst)或瞬时pH(pHinst); 并且,如果反转%inst invert%max,HMFinst> HMFmax,pHinst pHmax; (iv)改变水溶液流速或水溶液温度中的至少一个,使得反相%min和nlE反相%max,HMFproduct&NlE; HMFmax或pHmin& NlE; pH值& NlE; pHmax。 我们还公开了一种能够用于执行蔗糖翻转方法的计算装置。