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    • 24. 发明申请
    • BIOREACTOR FOR SYNGAS FERMENTATION
    • 生物反应器用于SYNGAS发酵
    • US20130005010A1
    • 2013-01-03
    • US13471858
    • 2012-05-15
    • Peter Simpson BellChing-Whan Ko
    • Peter Simpson BellChing-Whan Ko
    • C12M1/02C12P7/06C12P1/04
    • A bioreactor is provided that includes a main reactor having a configuration selected from the group consisting of stirred and unstirred tank reactor, trickle bed reactor (TBR), cocurrent contactor (CCC), moving bed bioreactor (MBBR), and a bubble column reactor. The bioreactor also includes a growth reactor continuous with the main reactor and having a configuration selected from the group consisting of stirred and unstirred tank reactor, trickle bed reactor (TBR), cocurrent contactor (CCC), moving bed bioreactor (MBBR), and a bubble column reactor. A method is also provided where acetogenic bacteria are contacted with syngas in a growth fermentor section of a reactor vessel that is continuous with a main fermentor section of a reactor vessel.
    • 提供了一种生物反应器,其包括具有选自搅拌和未搅拌的罐式反应器,滴流床反应器(TBR),并流接触器(CCC),移动床生物反应器(MBBR)和气泡塔型反应器的构型的主反应器。 生物反应器还包括与主反应器连续的生长反应器,并且具有选自搅拌和非搅拌釜反应器,滴流床反应器(TBR),并流接触器(CCC),移动床生物反应器(MBBR)和 泡罩塔反应器。 还提供了一种方法,其中在与反应器容器的主发酵罐部分连续的反应器容器的生长发酵罐部分中,使致生菌与合成气接触。
    • 25. 发明申请
    • Process for the production of ethanol and butanol
    • 生产乙醇和丁醇的方法
    • US20120040427A1
    • 2012-02-16
    • US12736101
    • 2009-02-19
    • Peter Simpson BellStephen John BensteadNeil Turnbull
    • Peter Simpson BellStephen John BensteadNeil Turnbull
    • C12P7/16C12P7/14
    • C12P7/14C12P7/065C12P7/08C12P7/16Y02E50/10Y02E50/17
    • The present invention relates to a process for the production of ethanol and butanol from biomass, and in particular to a process for the production of ethanol and butanol using two separate fermentation steps, said process comprising: a) passing a biomass feedstock to a first fermentation step, b) in said first fermentation step subjecting the biomass feedstock to anaerobic fermentation at a pH below 6.0 and at a temperature in the range 20 to 700° C. and so as to convert the biomass to a product predominantly comprising acetic acid and butyric acid with at least a 2:1 ratio by weight of acetic acid to butyric acid, c) treating the product stream of step (b) to separate a solution comprising the acetic acid and butyric acid by: (i) separating a solution comprising the acetic acid and butyric acid from any residual solids and (ii) separating bacteria and/or pasteurising or sterilising the solution from the first fermentation step, and d) in a second fermentation step fermenting the solution comprising the acetic acid and butyric acid from step (c) to form ethanol and butanol.
    • 本发明涉及从生物质生产乙醇和丁醇的方法,特别涉及使用两个单独的发酵步骤生产乙醇和丁醇的方法,所述方法包括:a)将生物质原料送入第一次发酵 步骤,b)在所述第一发酵步骤中,使生物质原料进行厌氧发酵,pH低于6.0,温度范围为20至700℃,以便将生物质转化成主要包含乙酸和丁酸的产物 酸与乙酸至丁酸的重量比至少为2:1,c)处理步骤(b)的产物流以通过以下方式分离包含乙酸和丁酸的溶液:(i)将包含 任何残留固体的乙酸和丁酸,和(ii)从第一发酵步骤分离细菌和/或将溶液灭菌或灭菌,以及d)在第二发酵步骤中发酵 包含来自步骤(c)的乙酸和丁酸以形成乙醇和丁醇。
    • 26. 发明申请
    • Process
    • 处理
    • US20100330640A1
    • 2010-12-30
    • US12736102
    • 2009-02-19
    • Peter Simpson BellStephen John BensteadNeil Turnbull
    • Peter Simpson BellStephen John BensteadNeil Turnbull
    • C12P7/14
    • C12P7/08C12P7/14Y02E50/17Y02E50/346
    • The present invention relates to a process for the production of ethanol comprising both gasification and fermentation of feedstocks, and, in particular to a process for the production of ethanol comprising: a) passing a biomass feedstock to a first fermentation step wherein it is subjected to anaerobic fermentation at a pH below 6.0 and at a temperature in the range 20 to to convert the biomass to a solution comprising acetic acid as the predominant product, b) passing a gasifiable feedstock to a gasification step wherein it is subjected to gasification to produce a gaseous mixture comprising carbon monoxide and hydrogen, and c) passing the solution comprising acetic acid from step (a) and the gaseous mixture from step (b) to one or more further fermentation steps wherein they are subject to fermentation to produce ethanol.
    • 本发明涉及一种生产乙醇的方法,其包括原料的气化和发酵,特别是涉及一种生产乙醇的方法,包括:a)将生物质原料通过第一发酵步骤,其中其经受 在pH低于6.0且在20℃的温度范围内的厌氧发酵以将生物质转化为包含乙酸作为主要产物的溶液,b)将可气化原料通入气化步骤,其中其进行气化以产生 包含一氧化碳和氢气的气态混合物,和c)将来自步骤(a)的乙酸溶液和来自步骤(b)的气态混合物的溶液通入一个或多个进一步的发酵步骤,其中它们进行发酵以产生乙醇。
    • 27. 发明申请
    • CUTTING TOOLS
    • 切割工具
    • US20090188361A1
    • 2009-07-30
    • US12042438
    • 2008-03-05
    • Peter SimpsonRainer Glauning
    • Peter SimpsonRainer Glauning
    • B26D5/00
    • A01G3/053A01D34/135A01D34/30A01D34/37A01D34/408A01G2003/0461Y10T83/525Y10T83/536
    • The present invention relates to cutting tools, in particular, to control systems for cutters such as vegetation cutters, especially hedge cutters or trimmers (10). Hedge cutters (10) frequently suffer in use from a problem of blocked cutting blades when they encounter a twig or branch whose size or density exceeds the capacity of the blades. We describe a vegetation cutting apparatus (10) having a plurality of cutting blades (11,12), at least one of which blades (11,12) is drivable by means of an electric motor. At least one driven blade (11,12) is movable between two predefined points of maximum travel. The apparatus (10) comprises a control means which causes a change of direction in the movement of the at least one movable blade at a point intermediate the points of maximum travel in response to an event sensed by the control means.
    • 技术领域本发明涉及切割工具,特别涉及用于诸如植被切割器,特别是树篱刀或修剪器(10)的切割器的控制系统。 冲锋刀(10)经常遭受使用中的切割刀片的问题,当它们遇到尺寸或密度超过刀片容量的枝条或枝条​​时。 我们描述具有多个切割刀片(11,12)的植被切割设备(10),其中至少一个刀片(11,12)可以通过电动机驱动。 至少一个从动叶片(11,12)可在两个预定的最大行程点之间移动。 装置(10)包括控制装置,其响应于由控制装置感测到的事件,使至少一个可动刀片在最大行程点之间的点处的移动方向发生变化。