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41. 发明授权

EP3126327B1 IMPROVED AMMONIA REMOVAL FROM REACTOR EFFLUENT 有权
公开(公告)号：EP3126327B1
公开(公告)日：2019-05-22
申请号：EP15715915.3
申请日：2015-03-24
申请人： Ineos Europe AG
发明人： MCDONEL, Timothy Robert , COUCH, Jay Robert , WAGNER, David Rudolph , WACHTENDORF, Paul Trigg
IPC分类号： C07C253/34 , C07C255/08 , C01C1/12 , B01J4/00 , B01J19/00 , F28C1/02 , F28C3/02 , B01J10/00 , B01D53/58 , B01D53/78

42. 发明公开

EP3476461A1 COMPOSITE AMINE ABSORBING SOLUTION, AND DEVICE AND METHOD FOR REMOVING CO2 OR H2S OR BOTH 有权转让
公开(公告)号：EP3476461A1
公开(公告)日：2019-05-01
申请号：EP18748673.3
申请日：2018-01-30
申请人： Mitsubishi Heavy Industries Engineering, Ltd.
发明人： TANAKA, Hiroshi , HIRATA, Takuya , KAMIJO, Takashi , TSUJIUCHI, Tatsuya
IPC分类号： B01D53/14 , B01D53/52 , B01D53/62 , B01D53/78 , C01B17/16 , C01B32/50
摘要： The composite amine absorbing solution according to the present invention absorbs CO 2 or H 2 S or both in a gas, and is obtained by dissolving (1) a linear monoamine, (2) a diamine, and (3) an amide group-containing compound in water. By adopting this composite amine absorbing solution, the composites are interacting in a composite manner, due to an integrated effect of the components, the absorption property of CO 2 or H 2 S or both is favorable, the desorption properties of the CO 2 or H 2 S absorbed when regenerating the absorbing solution become favorable, and the amount of steam from a reboiler 26 used when regenerating the absorbing solution in a CO 2 recovery device 12 can be reduced.

43. 发明授权

EP3178537B1 CO2 RECOVERY DEVICE AND CO2 RECOVERY METHOD 有权转让
公开(公告)号：EP3178537B1
公开(公告)日：2019-04-17
申请号：EP15856351.0
申请日：2015-10-23
申请人： Mitsubishi Heavy Industries Engineering, Ltd.
发明人： TANAKA, Hiroshi , HIRATA, Takuya , YUKUMOTO, Atsuhiro , OISHI, Tsuyoshi , ENDO, Takahiko , TSUJIUCHI, Tatsuya
IPC分类号： B01D53/62 , B01D53/14 , B01D53/73 , B01D53/78 , B01D53/79 , B01D53/96

44. 发明公开

EP3461549A1 DEDUSTING AND DEMISTING APPARATUS FOR WET DESULFURIZATION, AND ELECTROMECHANICAL COUPLING WET DEDUSTING AND DEMISTING APPARATUS 审中-公开
公开(公告)号：EP3461549A1
公开(公告)日：2019-04-03
申请号：EP17825357.1
申请日：2017-07-31
申请人： BEIJING ZHONGNENG NUOTAI ENERGY SAVING AND ENVIRONMENTAL PROTECTION CO., LTD.
发明人： WU, Zhengmin , ZHAO, Yuncai , WANG, Liang
IPC分类号： B01D50/00 , B01D53/78 , B01D45/16 , B01D53/32 , B03C3/02
摘要： Disclosed is a dust and mist removal device for wet desulfurization. The dust and mist removal device for wet desulfurization comprises a multi-stage mechanical dust and mist removal device and a wet electrostatic precipitator; wherein the multi-stage mechanical dust and mist removal device is connected in series to the wet electrostatic precipitator to form an electromechanical wet dust and mist removal unit, the multi-stage mechanical dust and mist removal device is positioned at a lower part the wet electrostatic precipitator, the multi-stage mechanical dust and mist removal device matches with the wet electrostatic precipitator in terms of cross-section shape and size, and the number of electromechanical wet dust and mist removal units arranged in parallel is defined according to a flue gas amount to be treated. According to the present application, the dust and mist removal efficiency is improved, the use is convenient and the cost is low.

45. 发明授权

EP2583740B1 REDUCING-AGENT SUPPLY DEVICE AND AN EXHAUST GAS NITROGEN-REMOVAL SYSTEM USING THE SAME 有权
公开(公告)号：EP2583740B1
公开(公告)日：2018-12-26
申请号：EP11798348.6
申请日：2011-06-20
申请人： Panasia Co., Ltd.
发明人： LEE, Soo-Tae , CHOI, Won-Suk , KANG, Gyeong-Woo
IPC分类号： B01D53/56 , B01D47/06 , B01D53/78 , B01D53/34 , F01N3/20
CPC分类号： B01D53/74 , B01D53/8625 , B01D2251/2062 , F01N3/2066 , F01N2610/00 , F01N2610/02 , F01N2610/1466 , F01N2610/1493 , Y02T10/24
摘要： This invention relates to a reducing agent supply device and an exhaust gas denitrification system using the same. The reducing agent supply device includes a reducing agent supply unit for supplying a reducing agent to a selective supply unit, a water supply unit for supplying water to the selective supply unit, the selective supply unit for selectively supplying any one of the reducing agent and water supplied from the reducing agent supply unit and the water supply unit to a spray unit, and the spray unit for spraying the reducing agent or water supplied from the selective supply unit, wherein the selective supply unit supplies water to the spray unit when the spray unit is blocked due to solidification of the reducing agent which remains behind therein because of a process in which the spray unit continuously sprays the reducing agent or a temporary malfunction of the device, thereby preventing blockage of the spray unit. Also an exhaust gas denitrification system using the device is provided.

46. 发明授权

EP3187242B1 CO2 RECOVERY UNIT AND CO2 RECOVERY METHOD 有权转让
公开(公告)号：EP3187242B1
公开(公告)日：2018-11-21
申请号：EP15819384.7
申请日：2015-06-19
申请人： Mitsubishi Heavy Industries Engineering, Ltd.
发明人： NAKAGAWA, Yosuke , SHIMADA, Daisuke , TSUJIUCHI, Tatsuya
IPC分类号： B01D53/14 , B01D53/62 , C01B32/50 , B01D53/78 , F23J15/04
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 , 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).

47. 发明授权

EP3124095B1 CONTROL OF CARBONYL SULFIDE WITH SODIUM BOROHYDRIDE IN CAUSTIC TOWERS FOR PETROLEUM/PETROCHEMICAL PROCESSES 有权转让
公开(公告)号：EP3124095B1
公开(公告)日：2018-09-26
申请号：EP16181860.4
申请日：2016-07-29
申请人： Baker Hughes, a GE company, LLC
发明人： MO, Hua , METZLER, Roger D.
IPC分类号： B01D53/48 , B01D53/78
CPC分类号： B01D53/485 , B01D53/78 , B01D2251/108 , B01D2251/304 , B01D2257/308
摘要： Sodium borohydride (NaBH 4 ) may be used to removing carbonyl sulfide (COS) from a process stream containing it. The method involves contacting the process stream with an amount of effective of NaBH 4 to react with the COS to form reaction products that may be removed by a process of washing away the reaction product by an aqueous basic compound and/or the reaction product having a higher boiling point than carbonyl sulfide which permits trapping the reaction product, such as in a caustic tower.

48. 发明授权

EP1872054B1 REDUCING MERCURY EMISSIONS FROM THE BURNING OF COAL 有权
公开(公告)号：EP1872054B1
公开(公告)日：2018-09-05
申请号：EP05738526.2
申请日：2005-04-21
申请人： Nox II International, Ltd.
发明人： COMRIE, Douglas C.
IPC分类号： C10L10/02 , F23J15/02 , F23J15/04 , B01D53/04 , B01D53/78 , B01J20/12 , B01D53/64 , F23J7/00 , F23K1/00 , F23J15/00 , B01D53/48 , B01D53/30 , C10L9/10 , B01J20/04 , B01J20/06 , B01J20/16
CPC分类号： F23J7/00 , B01D53/04 , B01D53/30 , B01D53/485 , B01D53/64 , B01D53/78 , B01D2253/104 , B01D2253/11 , B01D2257/30 , B01D2257/602 , B01J20/041 , B01J20/043 , B01J20/046 , B01J20/06 , B01J20/12 , B01J20/16 , B01J2220/42 , C10L9/10 , C10L10/00 , C10L10/02 , F23J15/00 , F23J15/025 , F23J15/04 , F23K1/00 , F23K2201/505 , Y10S423/05
摘要： Sorbent compositions containing halogen and either nitrates or nitrites are added to coal to mitigate the release of mercury and/or other harmful elements into the environment during combustion of coal containing natural levels of mercury.

49. 发明授权

EP3099399B1 METHOD FOR REMOVING GASEOUS ELEMENTARY MERCURY FROM A STREAM OF GAS 有权转让
公开(公告)号：EP3099399B1
公开(公告)日：2018-08-22
申请号：EP15708248.8
申请日：2015-01-27
申请人： Outotec (Finland) Oy
发明人： ALLGULIN, Torkel
IPC分类号： B01D53/14 , B01D53/78 , B01D53/04 , B01D53/64
CPC分类号： B01D53/64 , B01D53/04 , B01D53/1493 , B01D53/78 , B01D2252/30 , B01D2253/102 , B01D2253/112 , B01D2257/602
摘要： The invention relates to a method and to an arrangement for removing gaseous elementary mercury from a stream of gas and to an arrangement for carrying out the method. The arrangement comprises a first washing tower (2) for receiving a stream of gas, a second washing tower (6) for receiving a stream of once processed gas (5) from the first washing tower (2), and a third washing tower (9) for receiving a stream of twice processed gas (23) from the second washing tower (6) and configured for discharging a stream of cleaned gas (12).

50. 发明公开

EP3359281A1 METHOD AND PLANT FOR CO2 CAPTURE 有权
公开(公告)号：EP3359281A1
公开(公告)日：2018-08-15
申请号：EP16762779.3
申请日：2016-09-06
申请人： Capsol-Eop AS
发明人： HAMRIN, Stellan
IPC分类号： B01D53/18 , B01D53/62 , B01D53/78 , F23J15/04 , B01D53/96
摘要： A method and plant for capturing CO2 from a CO2 containing exhaust gas (1), where the exhaust gas is compressed (10) and thereafter cooled (13, 15, 22) before the exhaust gas is introduced into an absorber (30), where the exhaust gas is brought in counter-current flow with an aqueous CO2 absorbent solution (49), to give a lean exhaust gas (31) that is withdrawn from the absorber (30), reheated 22, 13) against incoming compressed exhaust gas, and thereafter expanded (34) and released into the atmosphere (4), where the aqueous CO2 absorbent solution is an aqueous potassium carbonate solution, and that the steam and CO2 withdrawn from the regenerator (40) is cooled in a direct contact cooler (61) by counter-current flow of cooling water (62), to generate a gaseous flow (70) of cooled CO2 and steam that is withdrawn for compression and drying of the CO2, and a liquid flow (64) of cooling water and condensed steam that is withdrawn and flashed (80), to give a cooled liquid phase (84) that is recycled as cooling water for the direct contact cooler (61) for the withdrawn CO2 and steam, and a gaseous phase (81) that is compressed (82) and thus heated, and introduced into the regenerator (40) as stripping steam (83).

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