-
公开(公告)号：EP2883594B1
公开(公告)日：2017-11-22
申请号：EP13827456.8
申请日：2013-07-31
发明人： OISHI, Tsuyoshi , NAGAYASU, Hiromitsu , TANAKA, Hiroshi , HIRATA, Takuya , KAMIJO, Takashi , SHIMADA, Daisuke
CPC分类号： B01D53/62 , B01D19/0015 , B01D19/0042 , B01D53/1425 , B01D53/1475 , B01D53/78 , B01D2252/204 , B01D2252/20478 , B01D2257/104 , B01D2258/0283 , C01B32/50 , Y02C10/04 , Y02C10/06 , Y02P20/152
摘要： A CO 2 recovery device is provided with a CO 2 absorber 13 and an absorbent regenerator 14 that regenerates a CO 2 absorbent (rich solution 12A) that absorbs CO 2 . The CO 2 absorber 13 includes a CO 2 absorbing section 13A in which a CO 2 -containing flue gas 11A that contains CO 2 and a CO 2 absorbent 12 that is a basic amine compound absorbent are brought into contact with each other to remove CO 2 , and an aqueous cleaning section 21 in which a decarbonated flue gas 11B, from which CO 2 is removed in the CO 2 absorbing section 13A, and rinsing water 20 are brought into contact with each other to remove an accompanying substance that accompanies the decarbonated flue gas 11B. A lean solution 12B, from which CO 2 is removed in the regenerator 14, is re-used in the absorber 13. The CO 2 recovery device includes a degassing basin 80 which is interposed in a rich solution supply line L 11 that supplies the rich solution 12A from the CO 2 absorber 13 to the absorbent regenerator 14, and which includes a retaining section 82 configured to remove oxygen in the rich solution 12A.
-
公开(公告)号：EP3150270A1
公开(公告)日：2017-04-05
申请号：EP15818919.1
申请日：2015-06-19
CPC分类号： B01D53/1412 , B01D53/1425 , B01D53/1475 , B01D53/18 , B01D53/346 , B01D53/62 , B01D53/78 , B01D2252/20478 , B01D2256/22 , B01D2258/0283 , C01B32/50 , F23J15/04 , F23J2215/50 , F23J2219/40 , Y02A50/2342 , Y02C10/04 , Y02C10/06 , Y02E20/326
摘要： Provided are a CO 2 recovery unit and a CO 2 recovery method which enable stable operation to continue even if an operation condition has changed. This CO 2 recovery unit (1) is equipped with: a CO 2 -absorber (14) that causes CO 2 included in flue gas (11A) to be absorbed into a CO 2 -absorbing solution (13); a CO 2 -regenerator (15) which regenerates the CO 2 -absorbing solution (13) by heating; and a CO 2 recovery amount control unit (111) which calculates a computed target value for the CO 2 recovery amount and a computed target value for the CO 2 recovery rate on the basis of a set value for the CO 2 recovery rate, actual measured values of the CO 2 concentration, gas flow rate, and temperature of the flue gas (11A), and maximum values for the CO 2 recovery amounts in the CO 2 -absorber (14) and the CO 2 -regenerator (15). On the basis of the set value for the CO 2 recovery rate or the computed target value for the CO 2 recovery rate, the CO 2 recovery amount control unit (111) controls: the amount of the CO 2 -absorbing solution (13) supplied to the CO 2 -absorber (14); the amount of the CO 2 -absorbing solution (13) supplied to the CO 2 -regenerator (15); and the amount of saturated steam (S) supplied to a regeneration heater (31) of the CO 2 -regenerator (15).
-
公开(公告)号：EP2883594A1
公开(公告)日：2015-06-17
申请号：EP13827456.8
申请日：2013-07-31
发明人： OISHI, Tsuyoshi , NAGAYASU, Hiromitsu , TANAKA, Hiroshi , HIRATA, Takuya , KAMIJO, Takashi , SHIMADA, Daisuke
CPC分类号： B01D53/62 , B01D19/0015 , B01D19/0042 , B01D53/1425 , B01D53/1475 , B01D53/78 , B01D2252/204 , B01D2252/20478 , B01D2257/104 , B01D2258/0283 , C01B32/50 , Y02C10/04 , Y02C10/06 , Y02P20/152
摘要： A CO 2 recovery device is provided with a CO 2 absorber 13 and an absorbent regenerator 14 that regenerates a CO 2 absorbent (rich solution 12A) that absorbs CO 2 . The CO 2 absorber 13 includes a CO 2 absorbing section 13A in which a CO 2 -containing flue gas 11A that contains CO 2 and a CO 2 absorbent 12 that is a basic amine compound absorbent are brought into contact with each other to remove CO 2 , and an aqueous cleaning section 21 in which a decarbonated flue gas 11B, from which CO 2 is removed in the CO 2 absorbing section 13A, and rinsing water 20 are brought into contact with each other to remove an accompanying substance that accompanies the decarbonated flue gas 11B. A lean solution 12B, from which CO 2 is removed in the regenerator 14, is re-used in the absorber 13. The CO 2 recovery device includes a degassing basin 80 which is interposed in a rich solution supply line L 11 that supplies the rich solution 12A from the CO 2 absorber 13 to the absorbent regenerator 14, and which includes a retaining section 82 configured to remove oxygen in the rich solution 12A.
摘要翻译： CO 2回收装置设置有CO 2吸收器13和吸收再生器14，吸收再生器14再生吸收CO 2的CO 2吸收剂（富溶液12A）。 CO 2吸收器13包括：CO 2吸收部13A，其使含有CO 2的含CO 2废气11A与作为碱性胺系化合物吸收剂的CO 2吸收剂12接触而除去CO 2;以及水溶液清洗部 其中在CO 2吸收部分13A中去除CO 2的脱碳酸化烟气11B与漂洗水20彼此接触以去除伴随脱二氧化碳烟气11B的伴生物质。 在再生器14中从中除去CO 2的贫溶液12B在吸收器13中再利用.CO 2回收装置包括脱气池80，该脱气池插入富溶液供应管线L11中， CO 2吸收器13连接到吸收剂再生器14，并且其包括保持部分82，该保持部分82构造成去除富溶液12A中的氧。
-
公开(公告)号：EP3061516B1
公开(公告)日：2017-11-29
申请号：EP15740962.4
申请日：2015-01-09
发明人： HIRATA, Takuya , TANAKA, Hiroshi , NAGAYASU, Hiromitsu , SORIMACHI, Yoshiki , SHIMADA, Daisuke , OISHI, Tsuyoshi
CPC分类号： B01D53/1475 , B01D53/1412 , B01D53/346 , B01D53/62 , B01D2252/20478 , B01D2258/0283 , C01B32/50 , Y02C10/06 , Y02P20/152
摘要： Provided are: a CO 2 recovery apparatus such that the total operational efficiency and stability of the apparatus can be improved even when the amount of a gas to be treated varies; and a CO 2 recovery process. This CO 2 recovery apparatus (1) is provided with: a CO 2 absorption tower (14) for bringing exhaust gas (11A) into contact with a CO 2 absorbing liquid (13) and thus making the CO 2 absorbing liquid (13) absorb the CO 2 contained in the exhaust gas (11A); a CO 2 absorbing liquid regeneration tower (15) for heating the CO 2 absorbing liquid (13) with steam and thus releasing CO 2 from the CO 2 absorbing liquid (13) and regenerating the CO 2 absorbing liquid (13); a flowmeter (101) for determining the flow rates of the exhaust gas (11A) introduced into the CO 2 absorption tower (14); and a control unit (102) for classifying the flow rates of the exhaust gas (11A) determined by the flowmeter (101) into multiple flow rate ranges, and controlling the flow rate of the CO 2 absorbing liquid (13) supplied to the CO 2 absorption tower (14) and the flow rate of steam supplied to the CO 2 absorbing liquid regeneration tower (15) on the basis of prescribed set load values which have been previously established in accordance with the multiple flow rate ranges.
-
公开(公告)号：EP3187242A1
公开(公告)日：2017-07-05
申请号：EP15819384.7
申请日：2015-06-19
CPC分类号： B01D53/1412 , B01D53/1425 , B01D53/1475 , B01D53/18 , B01D53/346 , B01D53/62 , B01D53/78 , B01D2252/20478 , B01D2256/22 , B01D2258/0283 , F23J15/04 , Y02A50/2342 , Y02C10/04 , Y02C10/06 , Y02E20/326
摘要： Provided are a CO 2 recovery unit and a CO 2 recovery method with which it is possible for a CO 2 recovery amount and/or a CO 2 recovery rate to be controlled with high accuracy towards a target value. This CO 2 recovery unit (1) is characterized by being equipped with: a CO 2 absorber (14) that causes CO 2 included in flue gas (11A) to be absorbed into a CO 2 -absorbing solution (13); a CO 2 -absorbing solution regenerator (15) which, by heating, regenerates the CO 2 -absorbing solution (13) that has absorbed the CO 2 ; a CO 2 recovery rate control unit which measures the CO 2 concentration in the flue gas (11A) and which, on the basis of the CO 2 concentration in the flue gas discharged from the CO 2 -absorbing solution (13) that has absorbed the CO 2 , changes the absorbing solution circulation amount and the amount of saturated steam (S) that is supplied to a regeneration heater (31); and a CO 2 recovery amount control unit which, in accordance with the CO 2 concentration of the flue gas (11A) and the flue gas flow rate, changes the circulation amount of the CO 2 -absorbing solution (13) and the amount of the saturated steam (S) supplied to the regeneration heater (31).
摘要翻译： 本发明提供一种二氧化碳回收装置和二氧化碳回收方法，能够以高精度控制二氧化碳回收量和/或二氧化碳回收率，达到目标值。 该二氧化碳回收装置（1）的特征在于，具备：将吸收烟气（11A）中所含的二氧化碳吸收到二氧化碳吸收液（13）中的二氧化碳吸收器（14）。 CO 2吸收液再生器（15），其通过加热使吸收了CO 2的CO 2吸收液（13）再生; 测量废气（11A）中的二氧化碳浓度并且基于从已吸收二氧化碳的二氧化碳吸收溶液（13）排出的废气中的二氧化碳浓度的二氧化碳回收率控制单元改变 吸收液循环量和供给到再生加热器的饱和蒸汽量（S）。 以及CO2回收量控制单元，其根据烟气（11A）的CO2浓度和烟气流量，改变CO 2吸收溶液（13）的循环量和饱和蒸汽量（ S）提供给再生加热器（31）。
-
公开(公告)号：EP3061516A1
公开(公告)日：2016-08-31
申请号：EP15740962.4
申请日：2015-01-09
发明人： HIRATA, Takuya , TANAKA, Hiroshi , NAGAYASU, Hiromitsu , SORIMACHI, Yoshiki , SHIMADA, Daisuke , OISHI, Tsuyoshi
CPC分类号： B01D53/1475 , B01D53/1412 , B01D53/346 , B01D53/62 , B01D2252/20478 , B01D2258/0283 , C01B32/50 , Y02C10/06 , Y02P20/152
摘要： Provided are: a CO 2 recovery apparatus such that the total operational efficiency and stability of the apparatus can be improved even when the amount of a gas to be treated varies; and a CO 2 recovery process. This CO 2 recovery apparatus (1) is provided with: a CO 2 absorption tower (14) for bringing exhaust gas (11A) into contact with a CO 2 absorbing liquid (13) and thus making the CO 2 absorbing liquid (13) absorb the CO 2 contained in the exhaust gas (11A); a CO 2 absorbing liquid regeneration tower (15) for heating the CO 2 absorbing liquid (13) with steam and thus releasing CO 2 from the CO 2 absorbing liquid (13) and regenerating the CO 2 absorbing liquid (13); a flowmeter (101) for determining the flow rates of the exhaust gas (11A) introduced into the CO 2 absorption tower (14); and a control unit (102) for classifying the flow rates of the exhaust gas (11A) determined by the flowmeter (101) into multiple flow rate ranges, and controlling the flow rate of the CO 2 absorbing liquid (13) supplied to the CO 2 absorption tower (14) and the flow rate of steam supplied to the CO 2 absorbing liquid regeneration tower (15) on the basis of prescribed set load values which have been previously established in accordance with the multiple flow rate ranges.
摘要翻译： 提供一种CO 2回收设备，使得即使当待处理气体的量变化时，设备的总操作效率和稳定性也可以提高; 和二氧化碳回收过程。 该CO 2回收装置（1）具备：使CO 2吸收液（13）与排气（11A）接触而使CO 2吸收液（13）吸收CO 2所含的CO 2的CO 2吸收塔（14） 排气（11A）; CO 2吸收液再生塔（15），其用水蒸气加热CO 2吸收液（13），从CO 2吸收液（13）释放CO 2并使CO 2吸收液（13）再生; 流量计（101），用于确定引入CO2吸收塔（14）的排气（11A）的流量; 和控制单元（102），用于将由流量计（101）确定的排气（11A）的流量分成多个流量范围，并且控制提供给CO 2吸收的CO 2吸收液体（13）的流量 根据预先设定的根据多个流量范围设定的设定负载值，计算供给到二氧化碳吸收液再生塔（15）的蒸汽的流量和流量。
-
7.发明公开
公开(公告)号：EP2998012A1
公开(公告)日：2016-03-23
申请号：EP15743873.0
申请日：2015-01-21
发明人： OKAMOTO, Shinichi , CHIYOMARU, Masaru , TANAKA, Hiroshi , NAGAYASU, Hiromitsu , HIRATA, Takuya , OISHI, Tsuyoshi , SHIMADA, Daisuke
CPC分类号： B01D53/1425 , B01D53/14 , B01D53/1412 , B01D53/1475 , B01D53/1493 , B01D53/30 , B01D53/52 , B01D53/62 , B01D53/77 , B01D2252/204 , B01D2257/504 , B01D2258/0283 , Y02A50/2342 , Y02C10/06
摘要： When CO 2 gas is absorbed from flue gas 11 containing CO 2 as absorbed gas by using an absorbent 12 circulating in an absorber 13 and an absorbent regenerator 14 in a closed system, a first sampling part X at which a lean solution sample 101 is collected in the vicinity of an inlet for a lean solution supply line L 2 in the absorber 13, a second sampling part Y at which a rich solution sample 102 is collected in the vicinity of an outlet for a rich solution supply line L 1 in the absorber 13, and an analyzing device 103 which analyzes the collected lean solution sample 101 and rich solution sample 102 are provided; the lean solution sample 101 at the first sampling part X and the rich solution sample 102 at the second sampling part Y are collected, respectively, in the same time period, and concentrations of CO 2 gas in the lean solution sample 101 and the rich solution sample 102 are measured, and then the gas absorbing and regenerating operation is controlled based on measured results.
摘要翻译： 当通过使用在封闭系统中在吸收器13和吸收剂再生器14中循环的吸收剂12将CO 2气体作为吸收气体从含有CO 2的烟道气11吸收时，收集贫溶液样品101的第一采样部分X 在吸收体13中的贫溶液供给管线L 2的入口附近，在吸收器13内的富溶液供给管线L 1的出口附近收集浓溶液样品102的第二取样部Y 提供了分析收集的贫溶液样品101和富溶液样品102的分析装置103; 分别在同一时间段收集第一取样部X的稀溶液样品101和第二取样部Y的富溶液样品102，稀溶液样品101中的CO 2气体浓度和富溶液 测量样品102，然后基于测量结果控制气体吸收和再生操作。
-
-
-
-
-
-
搜索结果
7 条记录 (耗时 0.013 秒)
