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    • 61. 发明申请
    • MECHANICAL SEAL DEVICE AND PROCESSING APPARATUS
    • 机械密封装置和加工装置
    • US20120127825A1
    • 2012-05-24
    • US13261089
    • 2010-07-22
    • Takeshi KojimaShinichi Yamagami
    • Takeshi KojimaShinichi Yamagami
    • F16J15/34B01F7/00
    • F16J15/3484B01F7/18F16J15/40
    • A mechanical seal device in which, between a processing equipment which performs processing under a sterile condition and a rotary shaft used with its one end inserted in the processing equipment from an atmosphere side, seal parts are disposed outside the processing equipment at least at two places along a length direction of the rotary shaft from the processing equipment side toward the atmosphere side seals the rotary shaft, and when the inside of the processing equipment and the seal parts are sterilized, the atmosphere-side seal part is also easily and surely sterilized similarly to the other seal part. An airtight area is provided on an atmosphere side of an atmosphere-side seal part so that an area communicating with the atmosphere-side seal part is kept airtight all along a circumferential direction of a rotary shaft, and sterilizing gas supplied to a sealing fluid supplied area, which is an area between the rotary shaft and a device main body of the mechanical seal device, in order to sterilize the seal parts is retained in the airtight area.
    • 一种机械密封装置,其特征在于,在无菌状态下进行处理的处理设备与从气氛侧插入到处理设备中的一端使用的旋转轴之间,至少在两处设置在处理设备外部 沿着旋转轴的长度方向从加工设备侧向大气侧密封旋转轴,并且当处理设备的内部和密封部件被灭菌时,气氛侧密封部也容易且可靠地灭菌 到另一个密封部分。 在大气侧密封部的气氛侧设置有气密区域,使得与大气侧密封部连通的区域沿着旋转轴的圆周方向保持气密,并且供给到供给的密封流体的消毒气体 作为机械密封装置的旋转轴和装置主体之间的区域,为了对密封部进行消毒,保持在气密区域。
    • 62. 发明申请
    • PROCESS FOR RECOVERY OF CARBON DIOXIDE FROM A FLUID STREAM, IN PARTICULAR FROM SYNGAS
    • 从流体流中回收二氧化碳的方法,特别是从SYNGAS
    • US20120067059A1
    • 2012-03-22
    • US13322125
    • 2010-05-25
    • Torsten KatzGeorg SiederKoji Tanaka
    • Torsten KatzGeorg SiederKoji Tanaka
    • F02C6/18C01B3/22C01C1/04B01D53/14
    • C10K1/08Y02C10/06Y02E20/16Y02E20/18Y02E20/185
    • A process for removing carbon dioxide from a fluid comprises the steps of: (a) treating the fluid by bringing it into countercurrent contact with a liquid absorbent in a first absorption zone and thereafter in a second absorption zone to absorb at least part of the carbon dioxide contained in the fluid into the absorbent; (b) depressurizing the loaded absorbent to release a first stream of carbon dioxide and yield a partially regenerated absorbent; (c) recycling a first stream of the partially regenerated absorbent into the first absorption zone; (d) heating a second stream of the partially regenerated absorbent to release a second stream of carbon dioxide and yield a regenerated absorbent; (e) recycling the regenerated absorbent into the second absorption zone; (f) condensing water vapour entrained in the second stream of carbon dioxide by cooling the second stream of carbon dioxide and transferring at least part of the heat recovered to the partially regenerated absorbent by indirect heat exchange. The invention provides a two-stage carbon dioxide recovery process wherein the overall energy required for carbon dioxide recovery is reduced and/or wherein at least part of the carbon dioxide is recovered at a pressure higher than atmospheric pressure so as to reduce the energy required for compression of the carbon dioxide, e.g., for sequestration. Also disclosed is a plant for removing carbon dioxide from a fluid.
    • 从流体中除去二氧化碳的方法包括以下步骤:(a)通过使流体与第一吸收区中的液体吸收剂逆流接触,然后在第二吸收区中以吸收至少部分碳 包含在流体中的二氧化碳变成吸收剂; (b)减压负载的吸收剂以释放第一流二氧化碳并产生部分再生的吸收剂; (c)将部分再生的吸收剂的第一流再循环到第一吸收区中; (d)加热部分再生的吸收剂的第二料流以释放第二二氧化碳流并产生再生的吸收剂; (e)将再生的吸收剂再循环到第二吸收区; (f)通过冷却第二二氧化碳流将夹带在第二二氧化碳流中的水蒸汽冷凝,并通过间接热交换将至少部分回收的热量转移到部分再生的吸收剂中。 本发明提供二阶段二氧化碳回收方法,其中减少二氧化碳回收所需的总能量和/或其中至少部分二氧化碳在高于大气压的压力下回收,以便减少二氧化碳回收所需的能量 压缩二氧化碳,例如用于封存。 还公开了一种用于从流体中除去二氧化碳的设备。
    • 64. 发明申请
    • CONTACTOR
    • 联系人
    • US20110210457A1
    • 2011-09-01
    • US12673441
    • 2008-08-13
    • Takashi Nakayama
    • Takashi Nakayama
    • B01F3/04B01D3/16B01D53/18
    • B01D3/32B01D3/141B01D3/24B01D11/043B01D53/18B01J8/22B01J2208/00247B01J2208/00274B01J2208/00283B01J2208/00787B01J2208/0084
    • [Technical Problem] A contactor is provided which is capable of making fluids of two phases contact each other under a good dispersion state and which can be easily multi-staged.[Means for Solving the Problems] The inside of a contactor 1 is divided into a plurality of cells 22, 32 by partition walls (a vertical wall 10, horizontal walls 21, 31) and the respective cells 22, 32 become countercurrent contacting spaces of an upflow fluid flowing up in the contactor 1 and a downflow fluid flowing down in the contactor 1. A downflow fluid injection hole 52 provided in the vertical wall 10 of each stage makes the downflow fluid blocked by the partition wall and residing inject into the neighboring cells 22, 32 of a lower stage side, while an upflow fluid flow-in port 51 provided in an upper side of the injection hole 2 makes an upflow fluid from the cells 22, 32 of the lower stage side flow in.
    • 技术问题提供一种接触器,其能够使两相流体在良好的分散状态下彼此接触并且可以容易地多级。 (解决问题的手段)接触器1的内部通过分隔壁(垂直壁10,水平壁21,31)被分成多个单元22,32,并且各单元22,32成为逆流接触空间 在接触器1中向上流动的向上流动的流体和在接触器1中向下流动的向下流动的流体。设置在每一级的垂直壁10中的下流流体注入孔52使得下流流体被分隔壁阻塞并且驻留在邻近的 下部侧的电池22,32同时设置在喷射孔2的上侧的向上流动的流入口51使来自下段侧的电池22,32的向上流体流入。
    • 66. 发明申请
    • Crude treatment system
    • 原油处理系统
    • US20110168523A1
    • 2011-07-14
    • US12927887
    • 2010-11-29
    • Naoaki Sawai
    • Naoaki Sawai
    • C10G31/06
    • C10G75/00C10G7/00C10G7/10
    • [Task] To provide a crude treatment system capable of treating crude containing a comparatively large content of a corrosive material.[Means for Resolution] A primary distillation tower 11 fractionates first crude into a target fraction. A secondary distillation tower 21 which fractionates second crude having a corrosive material content greater than that of the first crude into a light fraction of which the content of the corrosive material is an amount not causing corrosion in the primary distillation tower 11 and a heavy fraction as the remainder thereof. Also, a light fraction supply line supplies the light fraction from the secondary distillation tower 21 to the primary distillation tower 11 so as to treat the light fraction in the primary distillation tower 11. Here, the secondary distillation tower 21 and the supply line for supplying second crude to the secondary distillation tower 21 are made from a material having corrosion resistance with respect to the corrosive material under circumstances in which the secondary distillation tower 21 and the supply line contact with the second crude and the heavy fraction.
    • [任务]提供能够处理含有比较大量的腐蚀性物质的粗品的粗制处理体系。 [解决方法]初级蒸馏塔11将第一粗品分馏成目标馏分。 二级蒸馏塔21,其将具有大于第一粗品的腐蚀性物质含量的第二粗品分馏成轻馏分,其中腐蚀性物质的含量是不会在一级蒸馏塔11中引起腐蚀的量,重馏分如 其余部分。 此外,轻馏分供给管将来自二次蒸馏塔21的轻馏分提供给一次蒸馏塔11,以处理一级蒸馏塔11中的轻馏分。这里,二次塔塔21和供给管 在二级蒸馏塔21和供给管线与第二原油和重馏分接触的情况下,第二原油至二级蒸馏塔21由具有相对于腐蚀性材料的耐腐蚀性的材料制成。
    • 70. 发明申请
    • METHOD FOR TREATING WASTE WATER CONTAINING NITRATE ION
    • 用于处理含有硝酸盐的废水的方法
    • US20090145858A1
    • 2009-06-11
    • US11719505
    • 2005-11-17
    • Shigeru MiharaHirofumi ItoMikio HiranoTakashi Kato
    • Shigeru MiharaHirofumi ItoMikio HiranoTakashi Kato
    • C02F1/70B01J23/89B01J35/08
    • C02F1/70B01J21/18B01J23/8926B01J35/08C02F1/66C02F1/68C02F1/705C02F2101/163
    • A method for treating waste water containing nitrate ion which comprises supplying raw waste water from a tube (2), formalin from a tube (3) and an aqueous alkaline solution from a tube (4) to a mixing vessel (1), while agitating with an agitator (5), so the resultant mixture has a pH of 7 or higher, transferring the mixture from an outlet pipe (6) to a catalyst bed (9) through a tube (8) by a pump (7), and discharging the treated fluid drained from the catalyst bed (9) to the outside of the system through pipe (11), wherein the catalyst bed (9) is provided within a jacket (10), through which a liquid such as water flows, for the temperature control, and is packed with a support type catalyst comprising spherical type activated carbon and Pd—Cu supported thereon. The type of reactor containing the support type catalyst in the catalyst bed (9) may be a fluidized bed or a fixed bed. The above method can be suitably used for reducing nitrate ion to nitrogen by the use of formalin as a reducing agent at a low treating cost and with a low selectivity of ammonia as a by-product.
    • 一种用于处理废水的含硝酸根离子,其包括从管(2),福尔马林从管(3)和从一个管(4)到混合容器(1)的碱性水溶液供给原废水,同时进行搅拌的方法 有搅拌器(5),因此所得到的混合物的pH为7或更高,将混合物从出口管(6)通过管(8),通过泵(7)转移到一个催化剂床(9),和 放电通过管(11)从所述催化剂床(9)排出到系统外的处理过的流体,其中所述催化剂床(9)的夹套(10)内,通过该液体,例如水的流动,​​对于 温度控制,并且填充有支撑型催化剂,其包含球形活性炭和负载在其上的Pd-Cu。 含在催化剂床(9)的负载型催化剂的反应器类型可以是流化床或固定床。 上述方法可以适当地使用了通过使用福尔马林作为以低处理成本还原剂还原硝酸根离子为氮和与氨的选择性低,为副产物。