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    • 5. 发明申请
    • GRAIN WET MILLING PROCESS FOR PRODUCING ETHANOL
    • 用于生产乙醇的颗粒磨细工艺
    • WO2006119206A3
    • 2007-01-11
    • PCT/US2006016661
    • 2006-05-02
    • TATE & LYLE INGREDIENTSJANSEN ROBERTKERR JOHNFARLEY EDWARDWALKER GORDONCAMBORIEUX SEBASTIEN
    • JANSEN ROBERTKERR JOHNFARLEY EDWARDWALKER GORDONCAMBORIEUX SEBASTIEN
    • A23L7/10C12P7/10C12R1/865
    • C12P7/06Y02E50/16Y02E50/17
    • Whole grain, such as wheat, barley, rye, and/or rice, can be processed by (a) steeping the grain in aqueous liquid to produce softened grain, (b) milling the softened grain to produce milled grain, (c) liquefying the milled grain by contacting it with amylase and heating it to a temperature of at least about 50°C, producing a liquefied material, (d) at least partially saccharifying the liquefied material by contacting it with amyloglucosidase at a temperature of at least about 50°C, producing a first saccharified material, and (e) separating fiber and germ from the first saccharified material, producing a screened material that is substantially free of fiber and germ. The process also includes the steps of (f) further saccharifying and fermenting the screened material with a microorganism that produces ethanol, thereby producing a broth that comprises ethanol, soluble protein, and insoluble protein, and (g) separating ethanol from the broth. A protein-rich product can be recovered from the broth that comprises both gluten from the grain and microorganism from the fermenting step.
    • 可以通过(a)在水性液体中浸渍谷物以产生软化的谷物,(b)研磨软化的谷物以产生碾磨的谷物,(c)液化(例如,麦粒,大麦,黑麦和/或米) 研磨的颗粒通过使其与淀粉酶接触并将其加热至至少约50℃的温度,产生液化材料,(d)至少部分地使液化材料与淀粉葡糖苷酶接触,其中所述液化物质与至少约50℃的温度 产生第一糖化材料,和(e)从第一糖化物质分离纤维和胚芽,产生基本上不含纤维和细菌的筛选材料。 该方法还包括以下步骤:(f)用生产乙醇的微生物进一步对筛选的材料进行糖化和发酵,从而产生包含乙醇,可溶性蛋白质和不溶性蛋白质的肉汤,和(g)从肉汤中分离乙醇。 富含蛋白质的产物可以从含有谷物的谷蛋白和发酵步骤的微生物的肉汤中回收。
    • 6. 发明申请
    • IMPROVED SUCROSE INVERSION PROCESS
    • 改进的SUCROSE反转过程
    • WO2008097878A2
    • 2008-08-14
    • PCT/US2008052877
    • 2008-02-04
    • TATE & LYLE INGREDIENTSJANSEN ROBERTKERR JOHNBAIADA ANTHONY
    • JANSEN ROBERTKERR JOHNBAIADA ANTHONY
    • C13B20/14C13K3/00C13B35/06
    • C13K3/00C13B20/14
    • 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
    • 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
    • 7. 发明申请
    • GRAIN WET MILLING PROCESS FOR PRODUCING DEXTROSE
    • 用于生产甜味剂的谷物湿法生产工艺
    • WO2006119217A2
    • 2006-11-09
    • PCT/US2006016679
    • 2006-05-02
    • TATE & LYLE INGREDIENTSJANSEN ROBERTKERR JOHNFARLEY EDWARDWALKER GORDONCAMBORIEUX SEBASTEIN
    • JANSEN ROBERTKERR JOHNFARLEY EDWARDWALKER GORDONCAMBORIEUX SEBASTEIN
    • A23J1/12A23J3/18A23J3/34A23K1/14C13B20/14C13K1/08
    • C12Y302/00A23J1/125A23J3/18A23K10/30A23K20/179A23K50/80A23L7/104A23L29/35C13B20/142C13K1/08Y02A40/818
    • Whole grain, such as wheat, barley, rye, and/or rice, can be processed by (a) steeping the grain or at least partially dehulled grain in an aqueous liquid to produce softened grain, (b) milling the softened grain to produce milled grain, (c) liquefying the milled grain by contacting it with amylase and heating it to a temperature of at least about 5O°C, producing a liquefied material, (d) at least partially saccharifying the liquefied material by contacting it with amyloglucosidase at a temperature of at least about 5O°C, producing a first saccharified material, and (e) separating fiber and germ from the first saccharified material, producing a screened material that is substantially free of fiber and wheat germ. The process also includes the steps of (f) further saccharifying the screened material by contacting it with amyloglucosidase at a temperature of at least about 5O°C, producing a second saccharified material, (g) membrane filtering the second saccharified material, producing a permeate that comprises primarily dextrose and other soluble components and a retentate that comprises insoluble protein, and (h) purifying the permeate by chromatographic separation, producing a purified dextrose stream. The chromatographic separation can also produce a raffinate, and the process can further include the steps of (i) combining the retentate from the membrane filtration and the raffinate from the chromatographic separation to form a fermentation medium, (j) fermenting the fermentation medium aerobically with a microorganism, (k) separating a protein product that comprises insoluble protein and microorganism from the medium, and (1) drying the protein product.
    • 可以通过(a)在水性液体中浸渍颗粒或至少部分脱壳的颗粒以产生软化的颗粒,(b)研磨软化的颗粒以产生(例如,小麦,大麦,黑麦和/或米) 磨碎的谷物,(c)通过使其与淀粉酶接触并将其加热至至少约50℃的温度来液化碾磨的谷粒,产生液化物质,(d)至少部分地使液化物质与淀粉葡糖苷酶接触, 至少约50℃的温度,产生第一糖化物质,和(e)从第一糖化物质分离纤维和胚芽,产生基本上不含纤维和小麦胚芽的筛选材料。 该方法还包括以下步骤:(f)通过使筛选的材料与淀粉葡糖苷酶在至少约50℃的温度下接触进一步糖化,产生第二糖化物质,(g)膜过滤第二糖化物质,产生渗透物 其主要包括葡萄糖和其他可溶性组分以及包含不溶性蛋白质的渗余物,和(h)通过色谱分离纯化渗透物,产生纯化的葡萄糖流。 色谱分离还可以产生萃余液,并且该方法还可以包括以下步骤:(i)将来自膜过滤的残留物和来自色谱分离的萃余液组合以形成发酵培养基,(j)有氧地发酵发酵培养基, 微生物,(k)从培养基中分离含有不溶性蛋白质和微生物的蛋白质产物,(1)干燥蛋白质产物。
    • 8. 发明申请
    • CORN WET MILLING PROCESS
    • 玉米湿磨工艺
    • WO2007015741A3
    • 2007-12-06
    • PCT/US2006027296
    • 2006-07-14
    • TATE & LYLE INGREDIENTSJANSEN ROBERTSASS DAVIDWALKER GORDONLUTZ ERIC
    • JANSEN ROBERTSASS DAVIDWALKER GORDONLUTZ ERIC
    • A23L1/105A23J1/12A23K1/00A23L1/308C13K1/06C13K1/08
    • A23K20/163A23J1/12A23K10/37A23L7/104A23L29/35A23L33/22Y02P60/877
    • A corn wet-milling process comprises steeping corn kernels in an aqueous liquid, which produces softened corn; milling the softened corn in a first mill, which produces a first milled corn; separating germ from the first milled corn, thereby producing a germ-depleted first milled corn; milling the germ-depleted first milled corn in a second mill, producing a second milled corn; separating the second milled corn into a first starch/protein portion that comprises starch and protein and a first fiber portion that comprises fiber, starch, and protein; milling the first fiber portion in a third mill, which produces a milled fiber material that comprises fiber, starch, ' and protein; separating at least some of the starch and protein in the milled fiber material from the fiber therein, producing a second fiber portion that comprises fiber and starch and a second starch/protein portion that comprises starch and protein; and contacting the second fiber portion with at least one enzyme to convert at least some of the starch therein to dextrose. The converted material is screened using one or more screens to separate the fiber from the liquor. The liquor can be fermented to ethanol, or refined to dextrose. The fiber can be pressed and dried as an animal feed.
    • 玉米湿磨工艺包括将玉米粒浸渍在水性液体中,其产生软化的玉米; 在第一磨机中磨碎软化的玉米,其产生第一磨碎的玉米; 从第一个研磨的玉米中分离胚芽,由此产生消耗细菌的第一个研磨的玉米; 在第二研磨机中研磨消毒的第一研磨玉米,产生第二研磨玉米; 将第二研磨玉米分离成包含淀粉和蛋白质的第一淀粉/蛋白质部分和包含纤维,淀粉和蛋白质的第一纤维部分; 在第三研磨机中研磨第一纤维部分,其产生包含纤维,淀粉和蛋白质的研磨纤维材料; 将碾磨的纤维材料中的至少一些淀粉和蛋白质与其中的纤维分离,产生包含纤维和淀粉的第二纤维部分和包含淀粉和蛋白质的第二淀粉/蛋白质部分; 和使第二纤维部分与至少一种酶接触以将其中的至少一些淀粉转化为右旋糖。 使用一个或多个筛网筛选转化的材料以从液体中分离纤维。 酒可以发酵成乙醇,或精制成右旋糖。 纤维可以作为动物饲料压制和干燥。
    • 9. 发明申请
    • CORN WET MILLING PROCESS
    • WO2009094418A3
    • 2010-04-01
    • PCT/US2009031652
    • 2009-01-22
    • TATE AND LYLE INGREDIENTS AMERJANSEN ROBERTKERR JOHNJONES PETER-LLOYDTANNER RICHARD
    • JANSEN ROBERTKERR JOHNJONES PETER-LLOYDTANNER RICHARD
    • C08B30/04C12P7/08C12P19/20C13K1/06
    • C13K1/06C08B30/044C12P7/06C12P19/14Y02E50/17
    • A corn wet-milling process comprises steeping corn kernels in an aqueous liquid, which produces softened corn; milling the softened corn in a first mill, which produces a first milled corn; separating germ from the first milled corn, thereby producing a germ-depleted first milled corn; milling the germ-depleted first milled corn in a second mill, producing a second milled corn; separating the second milled corn into a first starch/protein portion that comprises starch and protein and a first fiber portion that comprises fiber, starch, and protein; milling the first fiber portion in a third mill, which produces a milled fiber material that comprises fiber, starch, and protein; separating at least some of the starch and protein in the milled fiber material from the fiber therein, producing a second fiber portion that comprises fiber and starch and a second starch/protein portion that comprises starch and protein; and contacting the second fiber portion with at least one enzyme to convert at least some of the starch therein to dextrose. The converted material is screened using one or more screens to separate the fiber from the liquor. The liquor can be fermented to ethanol, or refined to dextrose. The fiber can be pressed and dried as an animal feed.
    • 玉米湿法研磨方法包括在含水液体中浸泡玉米粒,产生软化的玉米; 在第一磨机中研磨软化的玉米,其生产第一研磨的玉米; 将胚芽与第一磨碎的玉米分离,从而产生一种无菌的第一磨碎的玉米; 在第二磨机中研磨灭菌的第一批玉米,生产第二批玉米; 将第二研磨的玉米分离成包含淀粉和蛋白质的第一淀粉/蛋白质部分和包含纤维,淀粉和蛋白质的第一纤维部分; 在第三磨机中研磨第一纤维部分,其产生包含纤维,淀粉和蛋白质的研磨纤维材料; 将磨碎的纤维材料中的至少一些淀粉和蛋白质与其中的纤维分离,产生包含纤维和淀粉的第二纤维部分和包含淀粉和蛋白质的第二淀粉/蛋白质部分; 以及使所述第二纤维部分与至少一种酶接触以将其中的至少一些淀粉转化成葡萄糖。 使用一个或多个筛网筛选转化的材料以将纤维与液体分离。 酒可以发酵成乙醇,或精制成葡萄糖。 纤维可以作为动物饲料被压制和干燥。
    • 10. 发明申请
    • IMPROVED PROCESS FOR EFFICIENT ENERGY RECOVERY FROM BIOMASS
    • 改进生物质能源回收方法
    • WO2009020740A3
    • 2010-11-18
    • PCT/US2008070067
    • 2008-07-15
    • TATE AND LYLE INGREDIENTS AMERGANGA RAYMOND CIMIG GREGMCBURNEY BLAKEJANSEN ROBERTKERR JOHNREUST STEVEN J
    • GANGA RAYMOND CIMIG GREGMCBURNEY BLAKEJANSEN ROBERTKERR JOHNREUST STEVEN J
    • F23G5/12F23G5/46F23G7/10F23J7/00
    • F23G7/10F23G5/12F23G5/46F23G2202/106F23G2206/20F23G2900/00001F23G2900/7012F23J7/00
    • A method for extracting energy from biomass depleted of at least some carbohydrate, at least some oil, or both by a) introducing the biomass into a vertically elongated combustion chamber having i) at least one suspension burner at the top of the combustion chamber which is capable of projecting a flame down the axis of the combustion chamber, ii) a heat transfer apparatus having at least a portion of a heat collection surface located radially from the flame and below the burner, and iii) an exhaust opening located below the flame and below at least a portion of the heat collection surface; b) combusting the biomass to yield a mixture containing hot flue gas and molten ash above the exhaust opening; c) transferring heat from the hot flue gas to at least a portion of the heat collection surface substantially by radiation prior to any substantial contact of ash to a surface of the combustion chamber, to yield a mixture containing warm flue gas and non-molten ash and having a lower molten ash content than the mixture yielded by the combusting step; and d) cooling the warm flue gas with cold gas, to yield a mixture containing cool flue gas and non-molten ash and having a lower molten ash content than the mixture yielded by the transferring step.
    • 一种用于从生物量中提取能量的方法,该方法是通过以下步骤从至少一些碳水化合物,至少一些油或两者中消耗的能量:a)将生物质引入垂直细长的燃烧室,所述燃烧室具有:i)在燃烧室顶部的至少一个悬浮燃烧器, 能够沿着燃烧室的轴线向下突出火焰,ii)传热装置,其具有位于燃烧器的径向与火焰之下的集热表面的至少一部分,以及iii)位于火焰下方的排气口, 在集热面的至少一部分的下方; b)燃烧生物质以产生在排气口上方含有热烟道气和熔融灰渣的混合物; c)在灰分与燃烧室的任何实质接触之前,基本上通过辐射将热量从热烟道气传递到至少一部分集热表面,以产生含有热烟气和非熔融灰的混合物 并且具有比通过燃烧步骤产生的混合物更低的熔融灰分含量; 和d)用冷气体冷却暖烟道气,得到含有冷烟道气和非熔融灰分的混合物,其熔融灰分含量低于转移步骤产生的混合物。