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    • 31. 发明申请
    • AN AIRCRAFT INTERNAL WING AND DESIGN
    • WO2003059736A3
    • 2003-07-24
    • PCT/US2003/000985
    • 2003-01-14
    • CARR, Robert, Jonathan
    • B64C3/10
    • An aircraft (12) comprising three wings located on either side of the fuselage (14). The forward wing (22) has a downward angle with a curved top and bottom surface. The upper wing (24) is located towards the rear of the aircraft and above the forward wing (22). The lower wing (26) is located below the upper wing (24) and slightly forward and located to the rear and below of the forward wing. The outer ends of all three wings come into contact at one point. The forward wing (22) uses the Coanda effect to increase the airflow across the top surface of the bottom wing. One embodiment of the aircraft has two turbines (58), shaft-coupled to a power source, located on either side of the forward end of the fuselage. Each engine (58) has part of its thrust (63) diverted through and directed by a plenum disposed internal of the Coanda toward both sides of the fuselage so that an equal amount of thrust (63)flows through the duct (65) and over the wings on either side of the fuselage (14).
    • 32. 发明申请
    • LOW-SHEAR CENTRIFUGE FEEDING SYSTEM
    • 低剪切中心送料系统
    • WO1997016256A1
    • 1997-05-09
    • PCT/US1996017703
    • 1996-11-01
    • CARR SEPARATIONS, INC.CARR, Robert, B.
    • CARR SEPARATIONS, INC.
    • B04B09/12
    • B04B1/00B04B11/06B04B15/08
    • A centrifugal separator comprises a bowl (200) rotatable about a vertically disposed axis including a feed cone assembly located at the closed conical lower end having a conical outer wall (212) and a cusp-shaped hub (214). An annular channel (216) is located between the conical outer wall (212) and the hub (214). A feed pipe (218) includes a feed outlet (224) which fits within the annular channel (216). In another embodiment, the bowl (100) includes an open lower end (102) and a closed upper end (104). An inverted feed cone (108) is positioned at the upper end (104) and includes a rounded cusp-shaped diverter (122) and an annular channel (132). A feed pipe (134) includes a feed applicator (138) which is positioned coaxially with an adjacent to the cusp-shaped diverter (122). The feed applicator (138) is sized and shaped to closely follow the contours of the cusp-shaped diverter (122). A vacuum (180) within a predetermined range is applied within the bowl to reduce power consumption and foaming.
    • 离心分离器包括可围绕竖直设置的轴线旋转的碗状物(200),包括位于封闭锥形下端的进料锥体组件,该进料锥形组件具有锥形外壁(212)和尖形轮毂(214)。 环形通道(216)位于锥形外壁(212)和轮毂(214)之间。 进料管(218)包括装配在环形通道(216)内的进料出口(224)。 在另一个实施例中,碗(100)包括敞开的下端(102)和封闭的上端(104)。 倒置进料锥(108)位于上端(104)处,并且包括圆形的尖头形分流器(122)和环形通道(132)。 进料管(134)包括与邻近尖头形转向器(122)同轴定位的进料施加器(138)。 进料施加器(138)的尺寸和形状被设计成紧密地跟随尖头形分流器(122)的轮廓。 在碗内施加预定范围内的真空(180)以降低功率消耗和发泡。
    • 33. 发明申请
    • SOLIDS SCRAPING ASSEMBLY FOR A CENTRIFUGE
    • 用于中心的固体切割装置
    • WO1997015400A1
    • 1997-05-01
    • PCT/US1996017701
    • 1996-10-24
    • CARR SEPARATIONS, INC.CARR, Robert, B.
    • CARR SEPARATIONS, INC.
    • B04B11/08
    • B04B11/08B04B2011/086B04B2011/088
    • A scraper assembly (32) for removing the collected solids component (50) of a feed material from an interior wall surface (28) of a centrifugal separator bowl (18) comprises a supporting shaft (34) positioned within the bowl (18) along a vertically disposed longitudinal axis. The supporting shaft (34) is pivotal between a stowed position and an operational position. At least two longitudinally spaced scraper blades (36) are attached to the supporting shaft (34) along the longitudinal axis and are adapted to contact the solids component (50) when the support shaft (34) is in the operational position. An upper scraper blade (36) is angularly offset with respect to the lower scraper blade (36) along the longitudinal axis so that any collected solids component (50) removed by the upper scraper blade (36) may freely drop clear of the lower scraper blade (36).
    • 用于从离心分离器碗(18)的内壁表面(28)去除进料的收集的固体成分(50)的刮刀组件(32)包括沿着碗(18)内定位的支撑轴(34) 垂直设置的纵向轴线。 支撑轴(34)在收起位置和操作位置之间枢转。 至少两个纵向间隔的刮刀(36)沿着纵向轴线附接到支撑轴(34),并且当支撑轴(34)处于操作位置时适于接触固体部件(50)。 上刮刀(36)相对于下刮刀(36)沿着纵向轴线成角度地偏移,使得由上刮刀(36)移除的任何收集的固体部件(50)可以自由地从下刮刀 刀片(36)。
    • 35. 发明申请
    • PROCESS FOR MODULATING THE CONCENTRATION OF DISSOLVED GASES IN LIQUID MEDIA
    • 调节液体中溶解气体浓度的方法
    • WO1994001530A1
    • 1994-01-20
    • PCT/GB1993001392
    • 1993-07-02
    • PUBLIC HEALTH LABORATORY SERVICE BOARDCARR, Robert, Jeffrey, GeddesTINSLEY, Anne
    • PUBLIC HEALTH LABORATORY SERVICE BOARD
    • C12M03/02
    • C12N5/0025C02F3/025C12M41/14C12M41/32C12N2500/02Y02W10/15
    • A process is provided for modulating the concentration of dissolved gases in liquid media, especially liquid media which are associated with biological materials e.g. aqueous culture media for cells, and waste products such as polluted water and sewage which are characterised by the presence of microorganisms. The process utilises a liquid transfer medium to effect the desired modulation and selecting physical properties of the liquid transfer medium and the manner in which the transfer medium is manipulated to facilitate the transfer of gases. The transfer medium (132) is transferred between zones (112, 114) operated at different temperatures in which the transfer medium exists respectively in the liquid and the gaseous states, gas dissolves in the transfer medium in a zone (114) where the transfer medium is in the liquid state and separation of gas from the transfer medium takes place in a separate zone (112).
    • 提供了一种方法,用于调节液体介质中的溶解气体的浓度,特别是与生物材料相关的液体介质。 用于细胞的水性培养基和以微生物存在为特征的废水和污水等废物。 该方法利用液体转移介质来实现所需的调节和选择液体转移介质的物理性能以及操作转印介质以便于气体转移的方式。 转移介质(132)在不同温度下操作的区域(112,114)之间转移,其中转移介质分别存在于液体和气体状态中,气体在区域(114)中溶解在转移介质中,其中转印介质 处于液体状态,并且气体与转移介质的分离发生在单独的区域(112)中。
    • 36. 发明申请
    • EXAMINATION OF OBJECTS OF MACROMOLECULAR SIZE
    • 检测大分子大小的物体
    • WO1991004507A1
    • 1991-04-04
    • PCT/GB1990001407
    • 1990-09-12
    • CARR, Robert, Jeffrey, GeddesCLARKE, David, JohnATKINSON, Anthony
    • G02B21/00
    • G02B21/0004G01N15/1434
    • In a method and apparatus for examining samples comprising individual objects (28) of macromolecular or similar size, or smaller, an instrument element (14) comprises a substrate (16) overlaid with a thin film layer (18) of a material that is electrically conductive and/or at last partly optically opaque. A discontinuity comprising an aperture (26) or an asperity is formed in or on the element (14) in a known location, and the sample (28) is brought to this discontinuity so that it is not necessary to search for the sample by scanning. Energy (e.g. electrical energy or light) is applied to the element (14) and, with the latter and the sample in intimate association, e.g. with the sample inside the aperture (26), changes in the radiation from the sample site resulting from the presence of the sample are detected.
    • 在用于检查包括大分子或相似尺寸或更小尺寸的单个物体(28)的样品的方法和装置中,仪器元件(14)包括覆盖有电薄膜层(18)的衬底(18),所述衬底 导电和/或最后部分光学不透明。 在已知位置处,在元件(14)中或其上形成包括孔(26)或凹凸的不连续性,并且样品(28)被带到该不连续处,使得不需要通过扫描来搜索样品 。 能量(例如电能或光)被施加到元件(14),并且与后者和样品紧密结合,例如, 样品在孔(26)内部,检测到样品存在导致样品位置辐射的变化。
    • 39. 发明申请
    • PROCESS FOR PRODUCTION OF METHYLENE-BRIDGED POLYPHENYL POLYAMINES
    • 制备亚甲基多胺聚苯胺的方法
    • WO2010072504A1
    • 2010-07-01
    • PCT/EP2009/065863
    • 2009-11-26
    • HUNTSMAN INTERNATIONAL LLCMITCHELL, Christopher, JohnCORMA CANOS, AvelinoCARR, Robert, HenryBOTELLA ASUNCION, Pablo
    • MITCHELL, Christopher, JohnCORMA CANOS, AvelinoCARR, Robert, HenryBOTELLA ASUNCION, Pablo
    • C07C209/60C07C209/78
    • C07C209/60C07C209/78C07C211/50
    • A process for providing methylene-bridged polyphenyl polyamines from aniline and formaldehyde according to the invention comprises the subsequent steps of a) condensing aniline and formaldehyde, providing a condensate, the molar ratio of aniline to formaldehyde being chosen in the range of 2 to 3.5; b) reacting, in a first catalytic reaction step, at a reaction temperature within the range of about 30°C to about 100°C, said condensate over a solid catalyst being chosen from the group consisting of clays, silicates, silica-aluminas and ion exchange resins, whereby an intermediate mixture is provided, the intermediate mixture comprising amino benzyl amines; c) converting, in a subsequent catalytic reaction step, at a temperature within the range of about 70°C to about 250°C, the reaction temperature in said subsequent catalytic reaction step is higher than the reaction temperature in said first catalytic reaction step, said intermediate mixture into methylene-bridged polyphenyl polyamines in presence of a subsequent solid catalyst being chosen from the group consisting of zeolites, delaminated zeolites and ordered mesoporous materials, thereby providing said methylene-bridged polyphenyl polyamines.
    • 根据本发明的由苯胺和甲醛提供亚甲基桥接的聚苯胺的方法包括以下步骤:a)使苯胺和甲醛缩合,提供缩合物,苯胺与甲醛的摩尔比选择在2至3.5的范围内; b)在第一催化反应步骤中,在约30℃至约100℃范围内的反应温度下使所述缩合物在固体催化剂上选自粘土,硅酸盐,二氧化硅 - 氧化铝和 离子交换树脂,由此提供中间体混合物,所述中间体混合物包含氨基苄基胺; c)在随后的催化反应步骤中,在约70℃至约250℃的温度范围内,将所述后续催化反应步骤中的反应温度高于所述第一催化反应步骤中的反应温度, 所述中间体混合物在随后的固体催化剂存在下,选自沸石,脱层沸石和有序介孔材料,从而提供所述亚甲基桥接的聚苯胺。
    • 40. 发明申请
    • PROCESS FOR THE PRODUCTION OF DI- AND POLYAMINES OF THE DIPHENYLMETHANE SERIES
    • 生产二苯乙烯系列二 - 和多聚酰胺的方法
    • WO2009037088A1
    • 2009-03-26
    • PCT/EP2008/061350
    • 2008-08-28
    • HUNTSMAN INTERNATIONAL LLCCARR, RobertKOOLE, Johannes LodewijkVAN DER BORDEN, Willem
    • CARR, RobertKOOLE, Johannes LodewijkVAN DER BORDEN, Willem
    • C07C209/78C07C209/86C07C211/50C07C263/10C08G18/76C08G73/02
    • C07C209/78C07C263/10C08G12/08C08G73/0266C07C211/50C07C265/14
    • Process for the production of di- and poly( diamino diphenyl methane) comprising the steps of (a) reacting aniline and formaldehyde in the presence of an acid catalyst to produce a reaction mixture containing di- and poly amines; (b) neutralising the reaction mixture containing di- and poly amines; (c) separating the neutralised reaction mixture into an organic phase containing di- and polyamines and an aqueous phase; (d) further treating the organic phase separated off in step (c) by (d1) washing with water followed by (d2) separating the washed mixture into an organic phase and an aqueous phase and (d3) further fractionation of the organic phase to produce purified di- and polyamines on the one hand and aniline/water on the other hand; (e) further treating the aqueous phase separated off in step (c) by (el) washing with aniline followed by (e2) separating the washed mixture into an aqueous phase and an organic phase and (e3) further treatment of the aqueous phase to remove the aniline thereby leaving an effluent stream; wherein phase separation in step (c) and/or step (d2) is facilitated by using any of the following methods either on its own or in combination with one or more of the other methods: (A) removal of some of the aromatic amine from the neutralised reaction mixture obtained in step (b) or the organic phase separated in step (c); (B) addition of di- and poly amine to the organic phase separated in step (c); (C) return of some of the organic phase obtained in step (d2) or (d3) to the washed mixture in step (d1).
    • 包括以下步骤的制备二 - 和二(二氨基二苯基甲烷)的方法:(a)在酸催化剂存在下使苯胺和甲醛反应以产生含有二胺和多胺的反应混合物; (b)中和含有二胺和多胺的反应混合物; (c)将中和的反应混合物分离成含有二胺和多胺及水相的有机相; (d)通过(d1)用水洗涤进一步处理在步骤(c)中分离的有机相,然后用(d2)将洗涤的混合物分离成有机相和水相,和(d3)将有机相进一步分级分离成 另一方面,一方面产生纯化的二胺和多胺,另一方面生产苯胺/水; (e)通过(e)用苯胺洗涤进一步处理在步骤(c)中分离的水相,然后(e2)将洗涤的混合物分离成水相和有机相,和(e3)将水相进一步处理 除去苯胺,从而留下流出物流; 其中步骤(c)和/或步骤(d2)中的相分离通过使用任何以下方法自身或与一种或多种其它方法组合来促进:(A)除去一些芳族胺 从步骤(b)中获得的中和反应混合物或步骤(c)中分离的有机相中获得; (B)在步骤(c)中分离的有机相中加入二胺和多胺; (C)在步骤(d1)中将步骤(d2)或(d3)中获得的一些有机相返回到洗涤的混合物中。