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1. 发明授权

US08828130B2 Exhaust gas treatment system equipped with carbon dioxide removal device 有权
标题翻译：废气处理系统配有二氧化碳去除装置
公开(公告)号：US08828130B2
公开(公告)日：2014-09-09
申请号：US13581920
申请日：2010-03-03
申请人： Jun Shimamura , Toshio Katsube , Shigehito Takamoto , Masaharu Kuramoto , Naoki Oda
发明人： Jun Shimamura , Toshio Katsube , Shigehito Takamoto , Masaharu Kuramoto , Naoki Oda
IPC分类号： B01D53/14 , F23J15/06 , F23J15/00 , F23J15/04
CPC分类号： F23J15/006 , B01D53/1475 , B01D2257/504 , B01D2258/0283 , F23J15/04 , F23J15/06 , F23J2215/10 , F23J2215/20 , F23J2215/50 , F23J2219/40 , Y02A50/2342 , Y02C10/04 , Y02C10/06 , Y02E20/326 , Y02E20/346 , Y02E20/363
摘要： An object of the present invention is to solve these problems and to provide a exhaust gas treatment system which prevents formation of deposits in a main duct and a flue, on and after the point where the exhaust gases converge, after the removal of CO2 and reduces labor required for maintenance such as cleaning, and thus enabling a long-term operation. Disclosed is an exhaust gas treatment system equipped with a carbon dioxide removal device, comprising a main duct 6 through which an exhaust gas, after treating an exhaust gas from a boiler 1 by a wet desulfurization device, passes; a diverging duct 40 configured to diverge some of an exhaust gas flow from the main duct; an CO2 removal device 20 configured to absorb and remove carbon dioxide (CO2) in the diverged exhaust gas by an amine absorbent; and a return duct 42 configured to converge the exhaust gas, from which CO2 has been removed by the CO2 removal device, with an exhaust gas that has not yet been diverged, wherein the return duct 42, before the point where the exhaust gases converge, is provided with heating means 8 configured to vaporize mist of the amine absorbent in the exhaust gas after convergence.
摘要翻译：本发明的目的是解决这些问题，并且提供一种排气处理系统，其在去除CO 2之后，在废气收敛点之后，在主管道和烟道中形成沉积物，并且减少维修所需的劳动力，如清洁，从而实现长期运行。公开了一种配备有二氧化碳去除装置的废气处理系统，其包括主管道6，通过湿式脱硫装置处理来自锅炉1的废气后的废气通过该主管道6; 发散管道40，其构造成使来自主管道的一些排气流分散; 被配置为通过胺吸收剂吸收和去除分散的废气中的二氧化碳（CO 2）的二氧化碳去除装置20; 以及回流管42，其被配置成会聚已经由二氧化碳去除装置除去CO 2的废气与尚未分流的废气，其中返回管42在废气会聚之前，设置有加热装置8，其被配置为在收敛之后蒸发废气中的胺吸收剂的雾。

2. 发明授权

US08741245B2 Carbon dioxide-absorbing solution and method of recovering carbon dioxide 有权
标题翻译：二氧化碳吸收溶液和回收二氧化碳的方法
公开(公告)号：US08741245B2
公开(公告)日：2014-06-03
申请号：US13519264
申请日：2009-12-28
申请人： Koichi Yokoyama , Eiji Miyamoto , Hirofumi Kikkawa , Shigehito Takamoto , Toshio Katsube , Naoki Oda , Jun Shimamura , Masaharu Kuramoto
发明人： Koichi Yokoyama , Eiji Miyamoto , Hirofumi Kikkawa , Shigehito Takamoto , Toshio Katsube , Naoki Oda , Jun Shimamura , Masaharu Kuramoto
IPC分类号： B01D53/62
CPC分类号： B01D53/1475 , B01D53/1493 , B01D53/62 , B01D2252/20405 , B01D2252/20421 , B01D2252/20426 , B01D2252/20473 , B01D2252/20484 , B01D2252/205 , B01D2252/2056 , B01D2252/504 , B01D2257/504 , Y02A50/2342 , Y02C10/06
摘要： A method of recovering carbon dioxide, includes bringing gas to be processed containing carbon dioxide (CO2) and oxygen into contact with the CO2-absorbing solution in an absorption column to form a CO2-rich solution; circulating the solution in a regeneration column to thermally release and recover CO2 and recirculating the absorbing solution as a CO2-poor solution inside the absorption column; and performing heat exchange between the solution being delivered from the absorption column to the regeneration column and the solution recirculated from the regeneration column to the absorption column, wherein an alkanolamine aqueous solution containing a silicone oil and/or an organosulfur compound is added to the solution inside the absorption column and/or the solution recirculated from the regeneration column to the absorption column to adjust the composition of the absorbing solution inside the absorption column.
摘要翻译：回收二氧化碳的方法包括使含有二氧化碳（CO 2）和氧的待处理气体与吸收塔中的CO 2吸收溶液接触以形成富CO 2溶液; 将溶液循环在再生塔中以热释放和回收CO 2并将吸收溶液作为不透水的溶液循环到吸收塔内; 并且在从吸收塔输送到再生塔的溶液和从再生塔再循环到吸收塔的溶液之间进行热交换，其中将含有硅油和/或有机硫化合物的链烷醇胺水溶液加入到溶液中在吸收塔内和/或从再生塔再循环到吸收塔的溶液中，以调节吸收塔内吸收溶液的组成。

3. 发明申请

US20120308469A1 CARBON DIOXIDE-ABSORBING SOLUTION AND METHOD OF RECOVERING CARBON DIOXIDE 有权
标题翻译：二氧化碳吸收解决方案和二氧化碳回收方法
公开(公告)号：US20120308469A1
公开(公告)日：2012-12-06
申请号：US13519264
申请日：2009-12-28
申请人： Koichi Yokoyama , Eiji Miyamoto , Hirofumi Kikkawa , Shigehito Takamoto , Toshio Katsube , Naoki Oda , Jun Shimamura , Masaharu Kuramoto
发明人： Koichi Yokoyama , Eiji Miyamoto , Hirofumi Kikkawa , Shigehito Takamoto , Toshio Katsube , Naoki Oda , Jun Shimamura , Masaharu Kuramoto
IPC分类号： C01B31/20 , C09K3/00
CPC分类号： B01D53/1475 , B01D53/1493 , B01D53/62 , B01D2252/20405 , B01D2252/20421 , B01D2252/20426 , B01D2252/20473 , B01D2252/20484 , B01D2252/205 , B01D2252/2056 , B01D2252/504 , B01D2257/504 , Y02A50/2342 , Y02C10/06
摘要： A method of recovering carbon dioxide, including bringing gas to be processed containing carbon dioxide (CO2) and oxygen into contact with the CO2-absorbing solution according to Claim 1 in an absorption column to form a CO2-rich solution; subsequently circulating the solution in a regeneration column to thermally release and recover CO2 and recirculating the absorbing solution as a CO2-poor solution inside the absorption column; and performing heat exchange between the solution being delivered from the absorption column to the regeneration column and the solution recirculated from the regeneration column to the absorption column, wherein an alkanolamine aqueous solution containing a silicone oil and/or an organosulfur compound represented by the Formula (A) or (B) is added to the solution inside the absorption column and/or the solution recirculated from the regeneration column to the absorption column to adjust the composition of the absorbing solution inside the absorption column so as to include the alkanolamine in an amount of 30% by weight or more and 60% by weight or less, the organosulfur compound in an amount of 0.01% by weight or more and 2% by weight or less, and the silicone oil in an amount of 5 ppm by weight or more and 100 ppm by weight or less.
摘要翻译：一种回收二氧化碳的方法，包括使含有二氧化碳（CO 2）和氧气的待处理气体与吸收塔中的根据权利要求1的吸收CO 2的溶液接触以形成富CO 2溶液; 随后将溶液循环在再生塔中以热释放并回收CO 2并将吸收溶液作为不透水的溶液再循环到吸收塔内; 并且在从吸收塔输送到再生塔的溶液和从再生塔再循环到吸收塔的溶液之间进行热交换，其中含有由式（（将A）或（B）添加到吸收塔内的溶液和/或从再生塔再循环到吸收塔的溶液中以调节吸收塔内部的吸收溶液的组成，从而将链烷醇胺的量为30重量％以上且60重量％以下，有机硫化合物的含量为0.01重量％以上2重量％以下，硅油为5重量ppm以上和100重量ppm以下。

4. 发明申请

US20120325092A1 EXHAUST GAS TREATMENT SYSTEM EQUIPPED WITH CARBON DIOXIDE REMOVAL DEVICE 有权
标题翻译：废气处理系统配有二氧化碳去除装置
公开(公告)号：US20120325092A1
公开(公告)日：2012-12-27
申请号：US13581920
申请日：2010-03-03
申请人： Jun Shimamura , Toshio Katsube , Shigehito Takamoto , Masaharu Kuramoto , Naoki Oda
发明人： Jun Shimamura , Toshio Katsube , Shigehito Takamoto , Masaharu Kuramoto , Naoki Oda
IPC分类号： B01D53/62
CPC分类号： F23J15/006 , B01D53/1475 , B01D2257/504 , B01D2258/0283 , F23J15/04 , F23J15/06 , F23J2215/10 , F23J2215/20 , F23J2215/50 , F23J2219/40 , Y02A50/2342 , Y02C10/04 , Y02C10/06 , Y02E20/326 , Y02E20/346 , Y02E20/363
摘要： An object of the present invention is to solve these problems and to provide a exhaust gas treatment system which prevents formation of deposits in a main duct and a flue, on and after the point where the exhaust gases converge, after the removal of CO2 and reduces labor required for maintenance such as cleaning, and thus enabling a long-term operation. Disclosed is an exhaust gas treatment system equipped with a carbon dioxide removal device, comprising a main duct 6 through which an exhaust gas, after treating an exhaust gas from a boiler 1 by a wet desulfurization device, passes; a diverging duct 40 configured to diverge some of an exhaust gas flow from the main duct; an CO2 removal device 20 configured to absorb and remove carbon dioxide (CO2) in the diverged exhaust gas by an amine absorbent; and a return duct 42 configured to converge the exhaust gas, from which CO2 has been removed by the CO2 removal device, with an exhaust gas that has not yet been diverged, wherein the return duct 42, before the point where the exhaust gases converge, is provided with heating means 8 configured to vaporize mist of the amine absorbent in the exhaust gas after convergence.
摘要翻译：本发明的目的是解决这些问题，并且提供一种排气处理系统，其在去除CO 2之后，在废气收敛点之后，在主管道和烟道中形成沉积物，并且减少维修所需的劳动力，如清洁，从而实现长期运行。公开了一种配备有二氧化碳去除装置的废气处理系统，其包括主管道6，通过湿式脱硫装置处理来自锅炉1的废气后的废气通过该主管道6; 发散管道40，其构造成使来自主管道的一些排气流分散; 被配置为通过胺吸收剂吸收和去除分散的废气中的二氧化碳（CO 2）的二氧化碳去除装置20; 以及回流管42，其被配置成会聚已经由二氧化碳去除装置除去CO 2的废气与尚未分流的废气，其中返回管42在废气会聚之前，设置有加热装置8，其被配置为在收敛之后蒸发废气中的胺吸收剂的雾。

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