会员体验
专利管家(专利管理)
工作空间(专利管理)
风险监控(情报监控)
数据分析(专利分析)
侵权分析(诉讼无效)
联系我们
交流群
官方交流:
QQ群: 891211   
微信请扫码    >>>
现在联系顾问~
热词
    • 1. 发明授权
    • Method and apparatus for controlling feed of gaseous reaction component
    • 用于控制气态反应组分进料的方法和装置
    • US07381837B2
    • 2008-06-03
    • US10503303
    • 2003-02-26
    • Hidehiko NakajimaYoshiyuki HaranoManabu Yamada
    • Hidehiko NakajimaYoshiyuki HaranoManabu Yamada
    • C07C51/12C07C51/14
    • B01J19/0006B01J4/02B01J10/002B01J2219/00006B01J2219/00065B01J2219/00162B01J2219/00164B01J2219/002B01J2219/00207B01J2219/00216B01J2219/0022B01J2219/00231B01J2219/0024C07C51/12Y02P20/142C07C53/08
    • A method comprises continuously supplying an alcohol to a pressurized reaction system, pressurizing carbon monoxide with a compressor 8 attached to a first feed line 22, for continuously supplying carbon monoxide to the reaction system via a second feed line 23 with a reference flow rate F, and converging excess carbon monoxide in the reaction system in the first feed line via a branched circulation line 24 for allowing to react alcohol with carbon monoxide. The reference flow rate F in the second feed line 23 is a total rate of a reference consumption flow rate Fcs in the reaction and a flow rate F1 in excess rate over a fluctuation consumption flow rate ΔFcv in the reaction system (F=Fcs+F1, F1>ΔFcv). According to the pressure fluctuation of the gaseous phase in the reaction system, the flow rate in the circulation line 24 is controlled to a flow rate Fr=F1−ΔFcv and the feed flow rate in the first feed line 22 is controlled to a flow rate Fsu=Fcs+ΔFcv, for compensating a consumption rate variation in the reaction system with the feed flow rate of carbon monoxide. This ensures discharge inhibition of the gaseous reactant in a liquid phase pressurized reaction system (such as carbonylation reaction system) and effective utilization of the reactant for the reaction.
    • 一种方法包括向加压反应系统连续供应醇,用连接到第一进料管线22的压缩机8加压一氧化碳,用于经由第二进料管线23以参考流量F连续向反应系统供应一氧化碳, 并且通过分支循环管线24在第一进料管线中的反应体系中过量的一氧化碳收敛,以允许醇与一氧化碳反应。 第二进料管线23中的参考流量F是反应中的参考消耗流量Fcs和超过反应体系中的波动消耗流量DeltaFcv的流量F 1的总速率(F = Fcs + F 1,F 1> DeltaFcv)。 根据反应体系中的气相的压力波动,将循环管线24的流量控制为流量Fr = F 1 -DeltaFcv,将第一进料管线22中的进料流量控制为流量 速率Fsu = Fcs +ΔFcv,用于补偿反应体系中一氧化碳进料流量的消耗速率变化。 这确保液相加压反应体系(如羰基化反应体系)中的气态反应物的排放抑制和反应物的有效利用。
    • 2. 发明申请
    • Method and apparatus for controlling feed of gaseous reaction component
    • 用于控制气态反应组分进料的方法和装置
    • US20050154228A1
    • 2005-07-14
    • US10503303
    • 2003-02-26
    • Hidehiko NakajimaYoshiyuki HaranoManabu Yamada
    • Hidehiko NakajimaYoshiyuki HaranoManabu Yamada
    • B01J3/02B01J3/00B01J4/00B01J4/02B01J8/22B01J10/00B01J19/00C07C51/12C07C53/08B01J8/00
    • B01J19/0006B01J4/02B01J10/002B01J2219/00006B01J2219/00065B01J2219/00162B01J2219/00164B01J2219/002B01J2219/00207B01J2219/00216B01J2219/0022B01J2219/00231B01J2219/0024C07C51/12Y02P20/142C07C53/08
    • A method comprises continuously supplying an alcohol to a pressurized reaction system, pressurizing carbon monoxide with a compressor 8 attached to a first feed line 22, for continuously supplying carbon monoxide to the reaction system via a second feed line 23 with a reference flow rate F, and converging excess carbon monoxide in the reaction system in the first feed line via a branched circulation line 24 for allowing to react alcohol with carbon monoxide. The reference flow rate F in the second feed line 23 is a total rate of a reference consumption flow rate Fcs in the reaction and a flow rate F1 in excess rate over a fluctuation consumption flow rate ΔFcv in the reaction system (F=Fcs+F1, F1>ΔFcv). According to the pressure fluctuation of the gaseous phase in the reaction system, the flow rate in the circulation line 24 is controlled to a flow rate Fr=F1−ΔFcv and the feed flow rate in the first feed line 22 is controlled to a flow rate Fsu=Fcs+ΔFcv, for compensating a consumption rate variation in the reaction system with the feed flow rate of carbon monoxide. This ensures discharge inhibition of the gaseous reactant in a liquid phase pressurized reaction system (such as carbonylation reaction system) and effective utilization of the reactant for the reaction.
    • 一种方法包括向加压反应系统连续供应醇,用连接到第一进料管线22的压缩机8加压一氧化碳,用于经由第二进料管线23以参考流量F连续向反应系统供应一氧化碳, 并且通过分支循环管线24在第一进料管线中的反应体系中过量的一氧化碳收敛,以允许醇与一氧化碳反应。 第二供给管线23中的参考流量F是反应中的参考消耗流量Fcs和超过反应系统中的波动消耗流量DeltaFcv的流量F1的总速率(F = Fcs + F1 ,F1> DeltaFcv)。 根据反应体系中的气相的压力波动,将循环管线24中的流量控制为流量Fr = F1-ΔFcv,将第一进料管线22中的进料流量控制为流量 Fsu = Fcs +ΔFcv,用于补偿反应体系中一氧化碳进料流量的消耗速率变化。 这确保液相加压反应体系(如羰基化反应体系)中的气态反应物的排放抑制和反应物的有效利用。
    • 6. 发明授权
    • Imaging apparatus and imaging method
    • 成像设备及成像方法
    • US08319864B2
    • 2012-11-27
    • US12717523
    • 2010-03-04
    • Manabu Yamada
    • Manabu Yamada
    • H04N5/202
    • H04N9/735H04N1/4074H04N1/41H04N5/243
    • An imaging apparatus includes: an image sensor; a pixel output judging processor which judges if a pixel output reaches a saturation level or not; a pixel output compensation processor which performs a compensating operation to compensate a pixel output of a pixel of a specific color which reaches the saturation level; a bit compression convertor which performs a bit compression such that pixel output data, which is once converted from a first bit number to a second bit number, is converted again to the first bit number; a histogram producer which produces a brightness histogram of a photographic subject image; and a calculator which calculates a ratio of the number of pixels of a maximum brightness area to the number of entire pixels from the brightness histogram, wherein the bit compression convertor performs the bit compression based on a bit compression characteristic set on the basis of the ratio of the number of pixels of the maximum brightness area.
    • 一种成像装置,包括:图像传感器; 像素输出判断处理器,其判断像素输出是否达到饱和水平; 像素输出补偿处理器,执行补偿操作以补偿达到饱和水平的特定颜色的像素的像素输出; 执行位压缩的位压缩转换器,使得一旦从第一位数转换为第二位数的像素输出数据被再次转换为第一位数; 产生摄影对象图像的亮度直方图的直方图制作器; 以及计算器,其从所述亮度直方图计算最大亮度区域的像素数与整个像素数的比率,其中所述比特压缩转换器基于基于所述比率设置的比特压缩特性来执行比特压缩 的最大亮度区域的像素数。
    • 7. 发明授权
    • Fluid storage container
    • 流体储存容器
    • US08251500B2
    • 2012-08-28
    • US12617006
    • 2009-11-12
    • Manabu YamadaTakeshi Komaki
    • Manabu YamadaTakeshi Komaki
    • B41J2/175
    • B41J2/17533B41J2/17513B41J2/185B41J29/02Y10T137/0318Y10T137/8593
    • A fluid storage container enables the easy removal of recovered fluid and reuse of the container without incurring the added costs of disassembly and replacing an absorbent material. In one exemplary embodiment, an ink cartridge 17 can have an ink storage unit 45 that stores waste ink, an ink inlet/outlet 55 disposed in a frame part 52 that can be the outside wall of the ink storage unit 45, an ink path 53 of which one end 53a communicates with the ink inlet/outlet 55 and the other end 53b is disposed opening into the ink storage unit, wall parts 54 that divide the ink storage unit 45 into an upper air chamber 61 and a lower fluid chamber 62 that communicate with each other through a communication path 58, and an outside air channel 87, of which one end 87a communicates with the air chamber 61 and the other end 87b enables communication with the outside at a position further from the air chamber 61 than the fluid chamber 62. Other embodiments of fluid storage containers are also disclosed.
    • 流体储存容器能够容易地除去回收的流体和容器的再利用,而不会导致拆卸和更换吸收材料的额外成本。 在一个示例性实施例中,墨盒17可以具有储存废墨的墨水存储单元45,设置在可以作为墨水存储单元45的外壁的框架部分52中的墨水入口/出口55,墨水通道53 其一端53a与墨水入口/出口55连通,另一端53b设置在墨水储存单元的开口处;壁部分54将墨水储存单元45分成上部空气室61和下部流体室62, 通过通信路径58和外部空气通道87,其一端87a与空气室61连通,而另一端87b能够在与空气室61更远的位置处与流体连通 还公开了流体储存容器的其它实施例。