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1384 条记录 (耗时 0.031 秒)

    METHOD AND FOSSIL-FUEL-FIRED POWER PLANT FOR RECOVERING A CONDENSATE
    101.
    发明申请
    METHOD AND FOSSIL-FUEL-FIRED POWER PLANT FOR RECOVERING A CONDENSATE 审中-公开
    用于回收冷凝器的方法和燃料燃料发电厂

    公开(公告)号：US20140150699A1

    公开(公告)日：2014-06-05

    申请号：US14234898

    申请日：2012-07-24

    申请人： Rudiger Schneider ,  Henning Schramm

    发明人： Rudiger Schneider ,  Henning Schramm

    IPC分类号： B01D53/14 ,  B01D53/00 ,  F23J15/02

    CPC分类号： B01D53/1475 ,  B01D53/002 ,  F01K23/10 ,  F23J15/02 ,  Y02C10/06 ,  Y02E20/326

    摘要： A fossil-fuel-fired power plant, having a combustion device, a CO2 separation device, which is arranged downstream of the fossil-fuel-fired power plant, for removing CO2, and a CO2 compressor station, which is arranged downstream of the CO2 separation device and which has a number of compressor stages and coolers for intermediate cooling is provided. The coolers are connected to the CO2 separation device or the fossil-fuel-fired power plant by means of a condensate line in order to recover condensate. A method for carrying out the condensate recovery is also provided.

    摘要翻译： 具有燃烧装置的化石燃料发电厂，设置在化石燃料发电厂下游的CO2分离装置，用于除去CO 2，以及CO 2压缩站，其设置在CO 2的下游 分离装置，其具有多个用于中间冷却的压缩机级和冷却器。 冷却器通过冷凝管线连接到CO2分离装置或化石燃料发电厂，以回收冷凝物。 还提供了一种执行冷凝水回收的方法。

    OXY FUEL BOILER SYSTEM AND A METHOD OF OPERATING THE SAME
    103.
    发明申请
    OXY FUEL BOILER SYSTEM AND A METHOD OF OPERATING THE SAME 有权
    氧燃料锅炉系统及其运行方法

    公开(公告)号：US20140106284A1

    公开(公告)日：2014-04-17

    申请号：US14056055

    申请日：2013-10-17

    申请人： ALSTOM Technology Ltd

    发明人： Olaf STALLMANN

    IPC分类号： F23N3/00 ,  F23J11/00 ,  F23L7/00 ,  F23J15/00

    CPC分类号： F23N3/002 ,  B01D53/002 ,  B01D2256/22 ,  F23J11/00 ,  F23J15/00 ,  F23J15/006 ,  F23J15/06 ,  F23J2215/50 ,  F23J2900/15061 ,  F23L7/007 ,  F23N3/085 ,  Y02C10/04 ,  Y02E20/344

    摘要： The present disclosure relates to a boiler system that includes an oxyfuel boiler in which a stream of oxygen and a fuel are combusted to generate a stream of flue gas. A flue gas condenser condenses the cleaned flue gas. A flue gas compression unit produces a stream of pressurized carbon dioxide rich flue gas. A pressure control system measures and controls the pressure after the flue gas conditioning system to a predetermined set value. A flow control system measures and controls the flow after the flue gas compression unit to a predetermined set value. The present disclosure further relates to a method of operating such a boiler system for an oxy-fuel process as well as to a power plant comprising such a system.

    摘要翻译： 本公开涉及一种锅炉系统，其包括氧燃料锅炉，其中氧气和燃料流燃烧以产生烟道气流。 烟道气冷凝器冷凝清洁的烟气。 烟道气体压缩单元产生一股加压富含二氧化碳的烟道气。 压力控制系统测量并控制烟道气调节系统之后的压力达预定的设定值。 流量控制系统测量并控制烟道气体压缩单元之后的流量达预定设定值。 本公开还涉及一种操作这种用于氧 - 燃料过程的锅炉系统以及包括这种系统的动力装置的方法。

    REDUCING TAR BALLS IN A GASIFICATION SYSTEM
    104.
    发明申请
    REDUCING TAR BALLS IN A GASIFICATION SYSTEM 有权
    减少燃气系统中的塔尔

    公开(公告)号：US20140060327A1

    公开(公告)日：2014-03-06

    申请号：US13898791

    申请日：2013-05-21

    申请人： GRUPO GUASCOR S.L

    发明人： Roberto Gil

    IPC分类号： B01D53/14

    CPC分类号： B01D53/1493 ,  B01D53/002 ,  B01D53/96 ,  B01D2257/702 ,  C10K1/046 ,  C10K1/06

    摘要： A system and method is provided for removing a condensate from a synthetic gas treatment system. The method includes feeding a first fluid stream into a bottom section of a scrubber chamber defined by a scrubber shell of a scrubber. The first fluid stream includes at least one condensable component. A second fluid stream is fed into a top section of the scrubber chamber, such that the second fluid stream flows in the scrubber chamber in a countercurrent flow direction to the first fluid stream. The second fluid stream contacts the first fluid stream causing the at least one condensable component to form the condensate, such that the condensate and the second fluid stream are collected in the bottom section of the scrubber chamber. The method further includes feeding a third fluid stream into the top section of the scrubbing chamber, such that the third fluid stream contacts the condensate and the second fluid stream and forms an emulsion. At least a portion of the emulsion including the condensate flows from the synthetic gas treatment system.

    摘要翻译： 提供一种用于从合成气体处理系统中去除冷凝物的系统和方法。 该方法包括将第一流体流输送到由洗涤器的洗涤器壳限定的洗涤室的底部。 第一流体流包括至少一个可冷凝组分。 第二流体流被供给到洗涤器室的顶部部分中，使得第二流体流在洗涤器室中以与第一流体流逆流的流动方向流动。 第二流体流接触第一流体流，导致至少一个可冷凝组分形成冷凝物，使得冷凝物和第二流体流收集在洗涤器室的底部。 该方法还包括将第三流体流进入洗涤室的顶部部分，使得第三流体流接触冷凝物和第二流体流并形成乳液。 包含冷凝物的乳液的至少一部分从合成气体处理系统流出。

    CONDENSATION-EVAPORATOR NANOPARTICLE CHARGER
    106.
    发明申请
    CONDENSATION-EVAPORATOR NANOPARTICLE CHARGER 有权
    冷凝器 - 蒸发器纳米粒子充电器

    公开(公告)号：US20140029154A1

    公开(公告)日：2014-01-30

    申请号：US14043662

    申请日：2013-10-01

    申请人： Aerosol Dynamics Inc.

    发明人： Susanne Vera Hering ,  Steven Russel Spielman ,  Gregory Stephen Lewis

    IPC分类号： B03C3/38

    CPC分类号： B03C3/38 ,  B01D5/0009 ,  B01D53/002 ,  B01D53/1475 ,  B01D2257/504 ,  G01N15/065 ,  G01N2015/0038 ,  G01N2015/1481

    摘要： A particle charging method and apparatus are provided. An ion source is applied to a particle laden flow. The flow is introduced into a container in a laminar manner. The container has at least a first section, a second section and a third section. The first section includes wetted walls at a first temperature. A second section adjacent to the first section has wetted walls at a second temperature T2 greater than the first temperature T1. A third section adjacent to the second section has dry walls provided at a temperature T3 equal to or greater than T2. Additional water removal and temperature conditioning sections may be provided.

    摘要翻译： 提供了一种粒子充电方法和装置。 将离子源施加到载满颗粒的流。 将流体以层流方式引入容器中。 容器至少具有第一部分，第二部分和第三部分。 第一部分包括第一温度下的湿壁。 与第一部分相邻的第二部分具有大于第一温度T1的第二温度T2的湿壁。 与第二部分相邻的第三部分具有设置在等于或大于T2的温度T3的干壁。 可以提供额外的除水和温度调节部分。

    Heat driven concentrator with alternate condensers
    109.
    发明授权
    Heat driven concentrator with alternate condensers 失效
    带有交替冷凝器的热驱集中器

    公开(公告)号：US08597471B2

    公开(公告)日：2013-12-03

    申请号：US12859729

    申请日：2010-08-19

    申请人： Randall N. Avery ,  Charlie Booth

    发明人： Randall N. Avery ,  Charlie Booth

    IPC分类号： B01D3/00

    CPC分类号： B01D53/261 ,  B01D1/30 ,  B01D1/305 ,  B01D53/002 ,  B01D59/02 ,  B01D59/04 ,  B01D59/08 ,  B01D59/26 ,  B01D59/50 ,  B01D2253/106 ,  B01D2253/108 ,  B01D2257/80 ,  B01D2259/40088 ,  C01B5/02 ,  G21F9/06

    摘要： A method for concentrating contaminated sorbate in a solution which includes contaminated sorbate and clean sorbate is described wherein contaminated sorbate having a freezing point which is higher than the freezing point of the clean sorbate is cooled to a temperature below the freezing point of the contaminated sorbate and above the freezing point of the clean sorbate to concentrate the contaminated sorbate by cycling alternately from a desorption cycle to an adsorption cycle. By maintaining the solution at a temperature between the freezing point of the contaminated sorbate and the freezing point of the clean sorbate, the clean sorbate can be evaporated off.

    摘要翻译： 描述了将污染的山梨酸盐浓缩在包括污染的山梨酸盐和清洁的山梨酸盐的溶液中的方法，其中具有高于清洁山梨酸盐的凝固点的凝固点的污染的山梨酸被冷却到低于污染的山梨酸盐的冰点的温度， 高于清洁山梨酸的凝固点，以通过从解吸循环交替循环到吸附循环来集中污染的山梨酸盐。 通过将溶液保持在被污染的山梨酸盐的凝固点和清洁的山梨酸的凝固点之间的温度下，干净的山梨酸盐可被蒸发掉。

    Method and system for methane separation and purification from a biogas
    110.
    发明授权
    Method and system for methane separation and purification from a biogas 有权
    沼气分离和净化甲烷的方法和系统

    公开(公告)号：US08568512B2

    公开(公告)日：2013-10-29

    申请号：US13097843

    申请日：2011-04-29

    申请人： Stanley M. Siegel ,  Dennis C. Siegel

    发明人： Stanley M. Siegel ,  Dennis C. Siegel

    IPC分类号： B01D53/02 ,  B01D50/00

    CPC分类号： B01D53/75 ,  B01D53/002 ,  B01D53/0476 ,  B01D53/52 ,  B01D2256/245 ,  B01D2257/504 ,  B01D2257/80 ,  B01D2258/05 ,  C10L3/101 ,  C10L3/103 ,  C12M47/18 ,  Y02C20/20 ,  Y02E50/343 ,  Y02P20/59

    摘要： The method and system for methane separation and purification from a biogas includes collecting a raw Biogas gas stream having methane, carbon dioxide, water, sulfur compounds and non-methane organic compound (NMOC) constituents. The Biogas stream is fed into the intake of a liquid sulfur scrubber or a sulfur adsorber unit where the Biogas is separated into a main gas stream routed downstream in the system and a sulfur compounds stream removed from the system. The main gas stream is then processed by an NMOC absorber and further downstream, by an NMOC adsorber. NMOC produced by both NMOC processes is liquefied, removed from the system and stored. Upstream from the NMOC processes, the main gas stream is processed by at least one CO2, N2, O2 gas separation unit that produces a usable product stream of enriched methane gas, and an off-gas stream, which a VPSAU processes for venting and recycling.

    摘要翻译： 从沼气中分离和净化甲烷的方法和系统包括：收集具有甲烷，二氧化碳，水，硫化合物和非甲烷有机化合物（NMOC）成分的生物沼气。 生物气流被送入液体硫洗涤器或硫吸附器单元的入口，其中生物气被分离成在系统中下游的主气流和从体系中除去的硫化合物流。 然后，主要气流由NMOC吸收器和进一步下游的NMOC吸附器处理。 由NMOC工艺生产的NMOC液化，从系统中取出并储存。 在NMOC工艺的上游，主气流由至少一个产生富集甲烷气体的可用产物流的二氧化碳，氮气，二氧化碳气体分离单元和一个废气流进行处理，VPSAU进行排放和循环 。