System for recovering carbon dioxide from flue gas
    42.
    发明授权
    System for recovering carbon dioxide from flue gas 有权
    烟气回收二氧化碳的系统

    公开(公告)号:US08535428B2

    公开(公告)日:2013-09-17

    申请号:US13003682

    申请日:2009-01-26

    IPC分类号: B01D53/14

    摘要: To include an absorber (1006) that brings CO2 absorbent that absorbs CO2 contained in flue gas (1002) into contact with the flue gas to remove CO2 from the flue gas, a regenerator (1008) that strips CO2 from CO2 absorbent (rich solution), which is fed from the absorber through a first feed line L1 and has absorbed CO2, to regenerate CO2 absorbent, thereby acquiring regenerated CO2 absorbent (lean solution) (1009), falling film reboilers (1101-1 and 1101-2) that draw off CO2 absorbent (amine solution) (1033) from near the bottom of the regenerator and reheats regenerated CO2 absorbent via steam (1031), a first liquid-vapor separator (1103) that separates the CO2 absorbent reheated by the falling film reboilers into regenerated CO2 absorbent in which CO2 has been removed and vapor containing CO2, and a second feed line L2 for supplying the separated regenerated CO2 absorbent to the absorber.

    摘要翻译: 为了包括吸收器(1006),其将吸收烟道气(1002)中包含的CO 2的CO 2吸收剂与烟道气接触以从烟道气中除去CO 2;再生器(1008),其从CO 2吸收剂(富溶液) ,其从吸收器通过第一进料管线L1进料并吸收CO 2,以再生CO 2吸收剂,从而获得再生的CO 2吸收剂(贫溶液)(1009),下拉膜再沸器(1101-1和1101-2) 从再生器底部附近排出CO 2吸收剂(胺溶液)(1033),并通过蒸汽(1031)再加热再生的CO 2吸收剂,第一液 - 气分离器(1103)将由降膜再沸器再加热的CO 2吸收剂分离成再生 已经除去CO 2的CO 2吸收剂和含有CO 2的蒸气,以及用于将分离的再生CO 2吸收剂供给到吸收器的第二供给管线L2。

    SYSTEM FOR RECOVERING CARBON DIOXIDE FROM FLUE GAS
    43.
    发明申请
    SYSTEM FOR RECOVERING CARBON DIOXIDE FROM FLUE GAS 有权
    从燃气回收二氧化碳的系统

    公开(公告)号:US20110107916A1

    公开(公告)日:2011-05-12

    申请号:US13003682

    申请日:2009-01-26

    IPC分类号: B01D53/18 B01D53/62

    摘要: To include an absorber (1006) that brings CO2 absorbent that absorbs CO2 contained in flue gas (1002) into contact with the flue gas to remove CO2 from the flue gas, a regenerator (1008) that strips CO2 from CO2 absorbent (rich solution), which is fed from the absorber through a first feed line L1 and has absorbed CO2, to regenerate CO2 absorbent, thereby acquiring regenerated CO2 absorbent (lean solution) (1009), falling film reboilers (1101-1 and 1101-2) that draw off CO2 absorbent (amine solution) (1033) from near the bottom of the regenerator and reheats regenerated CO2 absorbent via steam (1031), a first liquid-vapor separator (1103) that separates the CO2 absorbent reheated by the falling film reboilers into regenerated CO2 absorbent in which CO2 has been removed and vapor containing CO2, and a second feed line L2 for supplying the separated regenerated CO2 absorbent to the absorber.

    摘要翻译: 为了包括吸收器(1006),其将吸收烟道气(1002)中包含的CO 2的CO 2吸收剂与烟道气接触以从烟道气中除去CO 2;再生器(1008),其从CO 2吸收剂(富溶液) ,其从吸收器通过第一进料管线L1进料并吸收CO 2,以再生CO 2吸收剂,从而获得再生的CO 2吸收剂(贫溶液)(1009),下拉膜再沸器(1101-1和1101-2) 从再生器底部附近排出CO 2吸收剂(胺溶液)(1033),并通过蒸汽(1031)再加热再生的CO 2吸收剂,第一液 - 气分离器(1103)将由降膜再沸器再加热的CO 2吸收剂分离成再生 已经除去CO 2的CO 2吸收剂和含有CO 2的蒸气,以及用于将分离的再生CO 2吸收剂供给到吸收器的第二供给管线L2。

    Amine recovery method and apparatus and decarbonation apparatus having same
    44.
    发明授权
    Amine recovery method and apparatus and decarbonation apparatus having same 有权
    胺回收方法及装置及其脱碳装置

    公开(公告)号:US06784320B2

    公开(公告)日:2004-08-31

    申请号:US10168975

    申请日:2002-08-13

    IPC分类号: C07C20982

    摘要: In a decarbonation process for removing carbon dioxide from a carbon dioxide-containing gas with the use of an amine compound-containing absorbing solution, an amine compound accompanying a decarbonated exhaust gas is efficiently recovered in the following manner: A water washing section is constituted in two stages, a first-stage water washing section 64 and a second-stage water washing section 65. In these water washing sections, recovery of the amine compound accompanying the decarbonated exhaust gas is performed sequentially. Regeneration tower refluxed water is supplied as washing water to the second-stage water washing section 65. Washing water is withdrawn from the second-stage water washing section 65 and supplied to the first-stage water washing section 64. Demisters 83, 84 and 85 are provided at outlets of a carbon dioxide absorption section 73, the first-stage water washing section 64 and the second-stage water washing section 65. An absorbing solution mist and a washing water mist accompanying the decarbonated exhaust gas are removed by these demisters.

    摘要翻译: 在使用含有胺化合物的吸收溶液从含二氧化碳气体中除去二氧化碳的脱碳过程中,伴随脱碳酸废气的胺化合物以下列方式被有效地回收:水洗部分 两级,第一级水洗部64和第二级水洗部65.在这些水洗部中,依次进行伴随脱碳废气的胺化合物的回收。 再生塔回流水作为洗涤水供给到第二级水洗部65.洗涤水从第二级水洗部65取出并供给至第一级水洗部64.除雾器83,84,85 设置在二氧化碳吸收部73,第一级水洗部64和第二级水洗部65的出口。通过这些除雾器除去吸附溶液雾和伴随脱碳废气的洗涤水雾。

    Amine recovery apparatus and decarbonation apparatus having same
    45.
    发明授权
    Amine recovery apparatus and decarbonation apparatus having same 有权
    胺回收装置及其脱碳装置

    公开(公告)号:US07316737B2

    公开(公告)日:2008-01-08

    申请号:US10700504

    申请日:2003-11-05

    IPC分类号: B01D53/14 B01D53/62 B01D53/78

    摘要: An amine recovery apparatus includes a carbon dioxide absorption section and plural water washing sections. The carbon dioxide absorption section brings the exhaust gas into vapor-liquid contact with an absorbing solution containing an amine compound and produces decarbonated exhaust gas. The water washing sections bring the decarbonated exhaust gas into vapor-liquid contact with washing water and sequentially recover the amine compound accompanying the decarbonated exhaust gas, while the decarbonated exhaust gas passes through the water washing sections in sequence from inlet portions to outlet portions thereof, respectively. The water washing sections have plural liquid reservoirs provided at the inlet portions of the water washing sections, respectively, and the liquid reservoirs reserve the washing water which is transported to the outlet portions of the water washing sections and supplied to the water washing sections, respectively.

    摘要翻译: 胺回收装置包括二氧化碳吸收部和多个水洗部。 二氧化碳吸收部使废气与含有胺化合物的吸收溶液气液接触,产生脱碳废气。 水洗部分使脱碳废气与洗涤水气液接触,并依次回收伴随脱碳废气的胺化合物,同时脱碳废气依次从其入口部分到出口部分通过水洗部分, 分别。 水洗部分分别设置在水洗部分的入口部分处的多个液体储存器,液体储存器储存被输送到水洗部分的出口部分并分别供应到水洗部分的洗涤水 。

    Transmission system, transmission device, packet loss ratio measurement method, and packet loss ratio measurement program
    48.
    发明授权
    Transmission system, transmission device, packet loss ratio measurement method, and packet loss ratio measurement program 有权
    传输系统,传输设备,丢包率测量方法和丢包率测量程序

    公开(公告)号:US09264332B2

    公开(公告)日:2016-02-16

    申请号:US14129075

    申请日:2012-06-12

    摘要: In a transmission system capable of measuring packet loss ratio between arbitrary devices upon a transmission path without increasing bandwidth of an OAM frame band, a plurality of transmission devices which have been disposed upon a transmission path are provided with a frame analysis unit which receives data frames so as to analyze the type of the data frames, a count processing unit which stores the number of received frames included in the data frames into storage module provided beforehand, an output line end portion which outputs the data frames, and an OAM processing unit which calculates the packet loss ratio in the transmission path using the number of received frames. The frame analysis unit has a function which, if the data frames are OAM frames, copies the data frames and the OAM processing unit has a function which calculates the packet loss ratio using the copied OAM frames.

    摘要翻译: 在能够测量传输路径上的任意设备之间的分组丢失率而不增加OAM帧频带宽的传输系统中,设置在传输路径上的多个传输设备设置有帧分析单元,其接收数据帧 为了分析数据帧的类型,将数据帧中包含的接收帧的数量存储在预先提供的存储模块中的计数处理单元,输出数据帧的输出线路端部分和OAM处理单元, 使用接收帧的数量来计算传输路径中的丢包率。 帧分析单元具有这样的功能:如果数据帧是OAM帧,则复制数据帧,并且OAM处理单元具有使用复制的OAM帧来计算分组丢失率的功能。

    Substrate processing apparatus and substrate processing method
    49.
    发明授权
    Substrate processing apparatus and substrate processing method 有权
    基板加工装置及基板处理方法

    公开(公告)号:US09070549B2

    公开(公告)日:2015-06-30

    申请号:US12680799

    申请日:2008-09-22

    IPC分类号: B08B5/02 H01L21/02 H01L21/67

    CPC分类号: H01L21/02052 H01L21/67028

    摘要: A drying gas is supplied into a drying chamber in a substantially horizontal direction, an obliquely downward direction descendent from the substantially horizontal direction, or a vertically downward direction under a state where a wafer is immersed in a cleaning liquid in a cleaning tank. The wafer is moved from the cleaning tank into the drying chamber, with the drying gas being supplied into the drying chamber. At this time, the supply of the drying gas into the drying chamber is stopped, under a condition where a part of the wafer is immersed in the cleaning liquid stored in the cleaning tank. After the movement of the wafer into the drying chamber has been finished, a drying gas is supplied into the drying chamber in an obliquely upward direction ascendant from the substantially horizontal direction or a vertically upward direction.

    摘要翻译: 在将晶片浸入清洗槽中的清洗液体的状态下,将干燥气体从大致水平方向或垂直向下方向向大致水平方向,倾斜向下方向供给到干燥室。 将晶片从清洁槽移动到干燥室中,其中干燥气体被供应到干燥室中。 此时,在将晶片的一部分浸渍在存储在清洗槽中的清洗液中的状态下,将干燥气体供给到干燥室内停止。 在将晶片移动到干燥室中之后,干燥气体从大致水平方向或垂直向上方向上升的斜上方向供给干燥室。