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    Dry carbon dioxide capturing device with multistage supply structure
    3.
    发明公开
    Dry carbon dioxide capturing device with multistage supply structure 有权
    Trockenkohlenstoffdioxid-Aufnahmevorrichtung mit mehrstufiger Versorgungsstruktur

    公开(公告)号：EP2596848A1

    公开(公告)日：2013-05-29

    申请号：EP12189244.2

    申请日：2012-10-19

    申请人： Korea Institute of Energy Research

    发明人： Yi, Chang-Keun ,  Park, Young Cheol ,  Jo, Sung-Ho ,  Jin, Gyoung Tae ,  Shun, Dowon ,  Bae, Dal-Hee ,  Park, Jaehyeon ,  Ryu, Ho-Jung ,  Lee, Seung-Yong ,  Moon, Jong-Ho ,  Lee, Dong-Ho

    IPC分类号： B01D53/12 ,  B01D53/62

    CPC分类号： B01D53/12 ,  B01D53/62 ,  B01D53/83 ,  B01D2251/304 ,  B01D2251/306 ,  B01D2257/504 ,  B01D2259/128 ,  B01D2259/4009 ,  Y02A50/2342 ,  Y02C10/04 ,  Y02C10/06 ,  Y02C10/08

    摘要： Disclosed is a dry carbon dioxide capturing device which can improve sorption efficiency by supplying sorbent for absorbing carbon dioxide or exhaust gas containing carbon dioxide to a recovery reactor in multistages at various heights. The dry carbon dioxide (CO 2 ) capturing device with multistage supply structure comprises a recovery reactor 102 to recover CO 2 by contacting a solid sorbent with exhaust gas; a recovery cyclone 110 connected to the recovery reactor 102 to discharge a gas while separating the CO 2 -captured solid sorbent only; a regenerator 114 connected to the recovery cyclone 110 to receive the CO 2 -captured solid sorbent and separate CO 2 captured in the solid sorbent; and a pretreatment reactor 122 connected to the regenerator 114 for cooling the solid sorbent free from CO 2 wherein at least one of the exhaust gas supply line and the sorbent supply line has two or more arranged according to the height of the recovery reactor 102.

    摘要翻译： 公开了一种干式二氧化碳捕获装置，其可以通过在各种高度的多级供应用于将回收反应器中的二氧化碳或含二氧化碳的废气提供给吸收剂来提高吸附效率。 具有多级供应结构的干二氧化碳（CO 2）捕获装置包括回收反应器102，以通过使固体吸附剂与废气接触来回收CO 2; 回收旋风器110，其连接到回收反应器102以排出气体，同时仅分离CO 2捕集的固体吸附剂; 连接到回收旋风分离器110以接收捕获在固体吸附剂中的CO 2捕获的固体吸附剂和分离的CO 2的再生器114; 以及连接到再生器114以用于冷却不含CO 2的固体吸附剂的预处理反应器122，其中废气供应管线和吸附剂供应管线中的至少一个根据回收反应器102的高度布置有两个或更多个。

    Dry carbon dioxide capturing device with improved energy efficiency
    4.
    发明公开
    Dry carbon dioxide capturing device with improved energy efficiency 审中-公开
    Trocken-AdsorptionsvorrichutungfürKohlendioxid miterhöhterEnergieeffizienz

    公开(公告)号：EP2581128A1

    公开(公告)日：2013-04-17

    申请号：EP12184861.8

    申请日：2012-09-18

    申请人： Korea institute of energy research

    发明人： Yi, Chang-Keun ,  Park, Young-Cheol ,  Jo, Sung-Ho ,  Jin, Gyong-Tae ,  Shun, Dowon ,  Bae, Dal-Hee ,  Park, Jaehyeon ,  Lee, Seung-Yong ,  Moon, Jong-Ho ,  Ryo, Ho-Jung ,  Lee, Dong-Ho

    IPC分类号： B01D53/12

    CPC分类号： B01D53/10 ,  B01D53/12 ,  B01D53/1475 ,  B01D53/62 ,  B01D2257/504 ,  B01D2259/4009 ,  Y02A50/2342 ,  Y02C10/04 ,  Y02C10/06 ,  Y02C10/08

    摘要： Disclosed is a dry CO 2 capturing device with improved energy efficiency, which utilizes a difference in temperature between a regeneration operation of isolating CO 2 from an sorbent containing CO 2 absorbed therein and a pre-treatment operation of allowing H 2 O to be adsorbed to CO 2 . The dry carbon dioxide (CO 2 ) capturing device, includes a recovery reactor for recovering CO 2 , a recovery cyclone for discharging a gas while separating the CO 2 -captured solid sorbent only, a regenerator for receiving the CO 2 -captured solid sorbent and separating CO 2 captured in the solid sorbent, and a pre-treatment reactor for cooling the solid sorbent free from CO 2 , wherein a first heat exchanger is provided between the recovery cyclone and the regenerator to pass the CO 2 -captured solid sorbent therethrough, and a second heat exchanger is provided between the pre-treatment reactor and the regenerator to pass the solid sorbent free from CO 2 therethrough. The first and second heat exchanger include a first and second heat exchange jacket mounted thereon which are connected to each other in a closed loop state.

    摘要翻译： 公开了一种具有提高的能量效率的干式CO 2捕获装置，其利用从吸收其中含有CO 2的吸附剂分离CO 2的再生操作和允许H 2 O被吸附的预处理操作之间的温度差异 CO 2。 干二氧化碳（CO 2）捕获装置包括用于回收CO 2的回收反应器，用于仅分离仅吸收CO 2的固体吸附剂排出气体的回收旋风分离器，用于接收CO 2捕获的固体吸附剂的再生器， 分离固体吸附剂中捕获的CO 2和用于冷却不含CO 2的固体吸附剂的预处理反应器，其中在回收旋风分离器和再生器之间提供第一热交换器以使CO 2捕获的固体吸附剂通过其中， 并且在预处理反应器和再生器之间设置第二热交换器以使固体吸附剂通过其中不含CO 2。 第一和第二热交换器包括安装在其上的第一和第二热交换套管，其以闭环状态彼此连接。

    Dry carbon dioxide capturing device using multi sorbents
    6.
    发明公开
    Dry carbon dioxide capturing device using multi sorbents 有权
    采用多吸附剂的干式二氧化碳捕集装置

    公开(公告)号：EP2604326A1

    公开(公告)日：2013-06-19

    申请号：EP12193224.8

    申请日：2012-11-19

    申请人： Korea Institute of Energy Research

    发明人： Yi, Chang-Keun ,  Park, Young Cheol ,  Jo, Sung-Ho ,  Jin, Gyoung Tae ,  Shun, Dowon ,  Bae, Dal-Hee ,  Park, Jaehyeon ,  Ryu, Ho-Jung ,  Lee, Seung-Yong ,  Moon, Jong-Ho ,  Lee, Dong-Ho

    IPC分类号： B01D53/10

    CPC分类号： B01D53/06 ,  B01D53/10 ,  B01D2253/112 ,  B01D2257/504 ,  Y02C10/04 ,  Y02C10/08

    摘要： Disclosed is a dry CO 2 capturing device using multi sorbents so as to maintain the sorption rate for exhaust gas containing CO 2 . The dry carbon dioxide (CO 2 ) capturing device comprises at least two dry carbon dioxide (CO 2 ) capturing parts comprising: a first and second recovery reactors 104 and 105 to recover CO 2 by contacting a solid sorbent with exhaust gas; a first and second recovery cyclones 106 and 122 connected to the recovery reactors; a first and second regenerators 110 and 126 connected to the recovery cyclones; and a first and second pre-treatment reactors 116 and 132 connected to the regenerators through sorbent supply lines. The first and second dry carbon dioxide (CO 2 ) capturing parts are connected to each other so as to feed an isolated gas, which is separated with the solid sorbent in the first recovery cyclone 106 of the first dry CO 2 capturing part, to the second dry CO 2 capturing part through the exhaust gas supply line, and different solid sorbents are used in the first and second CO 2 capturing parts.

    摘要翻译： 公开了使用多吸附剂的干式二氧化碳捕获装置，以维持含有二氧化碳的排气的吸附速率。 干燥的二氧化碳（CO 2）捕集装置包括至少两个干燥的二氧化碳（CO 2）捕集部分，其包括：第一和第二回收反应器104和105，其通过使固体吸附剂与废气接触来回收CO 2; 连接到回收反应器的第一和第二回收旋流器106和122; 连接到回收旋风器的第一再生器110和第二再生器126; 以及通过吸附剂供应管线连接到再生器的第一和第二预处理反应器116和132。 第一和第二干燥二氧化碳（CO 2）捕获部件彼此连接以便将在第一干燥CO 2捕获部件的第一回收旋风器106中与固体吸附剂分离的分离气体供给到第二干燥 通过废气供应管线的CO 2捕集部分，并且在第一和第二CO 2捕集部分中使用不同的固体吸附剂。

    Exhaust gas treating apparatus and treating method for carbon dioxide capture process
    7.
    发明公开
    Exhaust gas treating apparatus and treating method for carbon dioxide capture process 审中-公开
    Abgasbehandlungsvorrichtung und BehandlungsverfahrenfürKohlendioxidabscheidungsverfahren

    公开(公告)号：EP2489423A1

    公开(公告)日：2012-08-22

    申请号：EP12152829.3

    申请日：2012-01-27

    申请人： Korea Institute of Energy Research

    发明人： Lee, Hyung-Keun ,  Choi, Won-Kil ,  Jo, Hang-Dae ,  Yi, Chang-Keun ,  Jo, Sung-Ho ,  Park, Young-Cheol

    IPC分类号： B01D53/60 ,  B01D53/64 ,  B01D53/75 ,  F23J15/00

    CPC分类号： B01D53/60 ,  B01D53/1475 ,  B01D53/64 ,  B01D53/75 ,  B01D2251/108 ,  B01D2251/30 ,  B01D2258/0283 ,  F23J15/003 ,  F23J15/006 ,  F23J2215/20 ,  F23J2215/50 ,  F23J2219/40 ,  F23J2900/15061 ,  Y02A50/2342 ,  Y02C10/04 ,  Y02C10/06 ,  Y02E20/326

    摘要： Disclosed are an exhaust gas treating apparatus and a treating method for a carbon dioxide capture process, in which harmful substances remaining in the exhaust gas discharged from the conventional flue-gas desulfurization process are additionally removed for efficient performance of the carbon dioxide capture process. According to the exhaust gas treating apparatus for a carbon dioxide capture process, it has the effects of minimizing the installation space of desulfurization equipment and reducing the process cost. In addition, by keeping the contaminants contained in the gas introduced in the carbon dioxide capture equipment below a proper level, absorption performance can be improved as degradation of the absorbent used in the carbon dioxide capture process is prevented. After all, it has an advantage of preventing the pollution by the exhaust gas discharged into the atmosphere.

    摘要翻译： 本发明公开了一种二氧化碳捕集方法的废气处理装置和处理方法，其中除去常规烟道气脱硫方法排出的废气中残存的有害物质，以有效地进行二氧化碳捕获处理。 根据用于二氧化碳捕集过程的废气处理装置，其具有使脱硫设备的安装空间最小化并降低工艺成本的效果。 此外，通过将引入到二氧化碳捕获装置中的气体中所含的污染物保持在适当的水平以下，可以改善吸收性能，因为可以防止二氧化碳捕获过程中使用的吸收剂的降解。 毕竟，具有防止排放到大气中的排气污染的优点。

    High-temperature and high-pressure system for desulfurisation and dehalogenation of gas
    10.
    发明公开
    High-temperature and high-pressure system for desulfurisation and dehalogenation of gas 有权
    Hochtemperatur- und Hochdrucksystem zur Entschwefelung und Enthalogenierung von Gas

    公开(公告)号：EP2614876A2

    公开(公告)日：2013-07-17

    申请号：EP13150666.9

    申请日：2013-01-09

    申请人： Korea Institute of Energy Research

    发明人： Yi, Chang-Keun ,  Park, Young Cheol ,  Jo, Sung-Ho ,  Ryu, Ho-Jung ,  Jin, Gyoung Tae ,  Shun, Dowon ,  Bae, Dal-Hee ,  Park, Jaehyeon ,  Lee, Seung-Yong ,  Moon, Jong-ho ,  Lee, Dong-Ho

    IPC分类号： B01D53/50 ,  B01D53/68 ,  B01D53/75

    CPC分类号： B01D53/508 ,  B01D53/685 ,  B01D53/75 ,  B01D53/83 ,  B01D2251/306 ,  B01D2251/602 ,  B01D2251/606 ,  Y02C10/04 ,  Y02C10/06

    摘要： Disclosed is a system for purifying high-temperature high-pressure contaminated gas which includes a dehalogenation process for removing halogen compounds from a raw gas by recycling a dry carbon dioxide sorbent that has been exhausted by repeated removing of carbon dioxide. The system 10 includes a desulfurization apparatus 200 which removes sulfur compounds from a raw gas; and a dehalogenation apparatus 100 which is disposed at a front or rear of the desulfurization apparatus 200 to remove halogen compounds. The dehalogenation apparatus 100 includes dehalogenation reactors 104 and 108 into which a dry carbon dioxide sorbent is introduced, and dehalogenation cyclones 106 and 110 which separate the dry carbon dioxide sorbents from a mixture of a dehalogenation gas and the dry carbon dioxide sorbents discharged from the dehalogenation reactor 100 and discharges only the dehalogenation gas.

    摘要翻译： 公开了一种用于净化高温高压污染气体的系统，其包括通过再循环通过反复去除二氧化碳而排出的干二氧化碳吸附剂从原料气体中除去卤素化合物的脱卤方法。 系统10包括从原料气体中除去硫化合物的脱硫装置200; 以及脱硫装置100，其设置在脱硫装置200的前方或后方，以除去卤素化合物。 脱卤装置100包括引入干燥二氧化碳吸附剂的脱卤反应器104和108，以及将脱二氧化碳吸附剂与脱卤气体和从脱卤化合物排出的干二氧化碳吸附剂的混合物分离的脱卤旋风器106和110 反应器100并仅排出脱卤气体。