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    • 56. 发明申请
    • APPARATUS AND PROCESS FOR GAS PHASE FLUIDISED BED POLYMERISATION REACTION
    • 气相流化床聚合反应的装置和方法
    • WO2010037653A1
    • 2010-04-08
    • PCT/EP2009/062186
    • 2009-09-21
    • INEOS EUROPE LIMITEDDUMAS, ThibaultRAMSAY, Kevin Peter
    • DUMAS, ThibaultRAMSAY, Kevin Peter
    • B01J8/24C08F10/00
    • C08F10/00B01J8/1809B01J8/1872B01J2208/00761B01J2208/00778B01J2208/00991C08F2/34C08F2/01
    • The present invention relates to an apparatus and a process for polymerisation, and, in particular, provides an apparatus for gas phase fluidised bed polymerisation of olefins, which apparatus comprises: A) a first section which is an upright cylindrical section having a diameter, D 1 , and cross- sectional area, A 1 , and B) a second section, provided vertically above the first section and centred about a common vertical axis to the upright cylindrical first section, the base of the second section having a cylindrical cross-section of diameter D 1 and being joined to the top of the first section, and the horizontal cross-sectional area of the second section above its base being greater than the cross-sectional area of the first section, characterised in that: i) D 1 is greater than 4.5 metres, and ii) the second section has a maximum horizontal cross- sectional area, A 2 , which is between 3.2 and 6 times the cross-sectional area, A 1 , of the first section.
    • 本发明涉及一种用于聚合的装置和方法,并且特别地提供了一种用于烯烃的气相流化床聚合的装置,该装置包括:A)第一部分,其是具有直径D1的直立圆柱形部分 横截面积A1和B)第二部分,其垂直设置在第一部分上方并且围绕垂直圆柱形第一部分的共同垂直轴线居中,第二部分的基部具有圆柱形截面直径 D1并且连接到第一部分的顶部,并且第二部分在其基部之上的水平横截面面积大于第一部分的横截面面积,其特征在于:i)D1大于4.5 米,并且ii)第二部分具有最大横截面积A2,其在第一部分的横截面积A1的3.2和6倍之间。
    • 57. 发明申请
    • EXTRUDER AND PROCESS FOR EXTRUDING A POLYMER
    • 挤出机和挤出聚合物的方法
    • WO2009121721A1
    • 2009-10-08
    • PCT/EP2009/053204
    • 2009-03-18
    • INEOS EUROPE LIMITEDPITMAN, Gary Lindsay
    • PITMAN, Gary Lindsay
    • B29C47/10
    • B29C47/10B29C47/0009B29C47/1009B29C47/1027B29C47/385B29C47/6075B29C47/66B29K2101/12
    • The present invention relates to an extruder for a polymer, and a process for extruding a polymer using said extruder. In particular, the present invention provides an extruder comprising: (i) two or more barrel sections (1a, 1b, 1c) arranged sequentially from: (a) an upstream feed barrel section (1a) to which polymer feedstock to be extruded is fed, the upstream feed barrel section containing two or more screws each having a diameter of X; to (b) a downstream barrel section (1c) from which melted polymer is passed to a die and extruded; and (ii) one or more feed ports for feeding polymer feedstock to be extruded into the extruder at its upstream end, characterised in that the total area of the one or more feed ports through which polymer feedstock is introduced is greater than 4*X, and a process for extrusion of polymer comprising feeding a polymer feedstock to the feed port of such an extruder.
    • 本发明涉及一种用于聚合物的挤出机,以及使用所述挤出机挤出聚合物的方法。 特别地,本发明提供了一种挤出机,其包括:(i)两个或更多个筒部分(1a,1b,1c),其从以下顺序排列:(a)上游进料筒部分(1a),待挤出的聚合物原料被供给 上游进料筒部分包含两个或更多个直径为X的螺钉; 到(b)熔融的聚合物通过模头挤出的下游桶部分(1c); 和(ii)一个或多个进料口,用于将聚合物原料输送到其上游端挤出到挤出机中,其特征在于,引入聚合物原料的一个或多个进料口的总面积大于4×X, 以及聚合物的挤出方法,包括将聚合物原料进料到这种挤出机的进料口。
    • 59. 发明申请
    • PROCESS FOR THE PRODUCTION OF ETHANOL AND BUTANOL FROM BIOMASS
    • 从生物量生产乙醇和丁醇的方法
    • WO2009112335A1
    • 2009-09-17
    • PCT/EP2009/051966
    • 2009-02-19
    • INEOS EUROPE LIMITEDBELL, Peter SimpsonBENSTEAD, Stephen John
    • BELL, Peter SimpsonBENSTEAD, Stephen John
    • C12P7/14C12P7/16C12P7/06C12P7/08
    • 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)将生物质原料送至第一次发酵 步骤,b)在所述第一发酵步骤中,使生物质原料在pH低于6.0,温度范围为20至700℃的条件下进行厌氧发酵,以将生物质转化成主要包含乙酸和丁酸的产物 其中乙酸与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步骤分离包含乙酸和丁酸的溶液:(i)将包含乙酸 来自任何残留固体的酸和丁酸和(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所述溶液 包括来自步骤(c)的乙酸和丁酸以形成乙醇和丁醇。