公开(公告)号：EP3018100B1

公开(公告)日：2018-04-18

申请号：EP13888724.5

申请日：2013-07-05

Applicant: Mitsubishi Heavy Industries, Ltd.

Inventor： UKAI, Nobuyuki ,  OKINO, Susumu ,  EDA, Masayuki ,  KAGAWA, Seiji ,  SUZUKI, Hideo ,  NAKASHOJI, Hiroshi ,  USHIKU, Tetsu ,  YOSHIOKA, Shigeru

IPC: B01D53/50 ,  B01D53/77 ,  B01D53/96 ,  B01D1/16 ,  B01D1/20 ,  C02F1/04 ,  C02F1/12 ,  C02F1/44 ,  C02F103/18

CPC classification number: C02F1/12 ,  B01D1/20 ,  B01D53/501 ,  B01D53/505 ,  B01D53/96 ,  B01D2258/0283 ,  C01F11/464 ,  C01P2004/04 ,  C01P2004/61 ,  C01P2006/80 ,  C01P2006/82 ,  C02F1/048 ,  C02F1/44 ,  C02F2103/18 ,  F23J15/04 ,  F23J2215/20

Abstract: A water treatment system of the present invention for effluent generated in a plant facility includes: a flue gas treatment system 18 that performs treatment of boiler flue gas 12 from a boiler 11; and a spray drying device 23 that includes a spraying unit, which sprays effluent 22 generated, for example, in a cooler 21 of the plant facility, and that performs spray drying using part 12a of the boiler flue gas 12. The water treatment system draws the effluent 22 is discharged into the spray drying device 23 so as to dry the sprayed liquid by the part 12a of the flue gas 12. It is thus not necessary to separately perform treatment of the effluent 22 in an industrial effluent treatment facility and it is possible to eliminate the need of draining the effluent 22 generated in the plant.

公开(公告)号：EP3170547A4

公开(公告)日：2018-01-24

申请号：EP15822300

申请日：2015-07-17

Applicant: MITSUBISHI HITACHI POWER SYS

Inventor： II SHINYA ,  KATAGAWA ATSUSHI ,  ISHIZAKA HIROSHI ,  SHIMAMURA JUN

IPC: B01D53/50 ,  B01D53/80 ,  B01D53/96 ,  C01F11/46 ,  C04B11/02 ,  C04B11/26 ,  C04B28/14 ,  F23J15/04

CPC classification number: B01D53/50 ,  B01D53/501 ,  B01D53/502 ,  B01D53/504 ,  B01D53/80 ,  B01D2251/404 ,  B01D2251/606 ,  B01D2258/0283 ,  C01F11/46 ,  C01F11/464 ,  C04B11/264 ,  F23J15/04 ,  F23J2215/20 ,  F23J2219/50

Abstract: Provided is a method of operating a flue gas desulfurization apparatus, in which gypsum slurry containing gypsum, which is obtained by bringing sulfur oxide contained in flue gas discharged from a combustion device including a boiler into contact with an absorbing solution composed of lime slurry in an absorption tower 1 and then subjecting the same to oxidation, is withdrawn from the absorption tower 1, and said gypsum slurry is supplied into a gypsum slurry tank 6 for supplying the gypsum slurry into dehydration equipment by using a pump 5 or is circulated to the absorption tower 1. In order to reduce the capacity of the pump 5 and thereby conserve pump power, the gypsum slurry is switched to being supplied into the gypsum slurry tank 6 or being circulated to the absorption tower 1 depending on the solid content concentration of the gypsum slurry withdrawn from the absorption tower 1.

公开(公告)号：EP3245334A1

公开(公告)日：2017-11-22

申请号：EP16756003.6

申请日：2016-01-14

Applicant: Imerys USA, Inc.

Inventor： PAYNTER, Christopher ,  STOVALL, Kalena ,  WICKS, Douglas ,  BUTLER-LEE, Gavin ,  GOLBAYANI, Parvin ,  JARVIS, Nigel, Victor ,  PRING, Graham, M. ,  TAYLOR, David ,  PEREZ, Ricardo, M.

IPC: D21H17/67 ,  C09C1/02 ,  C01F11/18

CPC classification number: C01F11/181 ,  B01D53/501 ,  B01D2251/404 ,  B01D2251/606 ,  C01F5/24 ,  C01F5/40 ,  C01F11/182 ,  C01F11/183 ,  C01F11/185 ,  C01F11/464 ,  C01F11/468 ,  C01P2004/03 ,  C01P2004/51 ,  C01P2004/61 ,  C01P2004/62 ,  C01P2006/12 ,  C01P2006/80 ,  C04B14/28 ,  C09C1/021 ,  D21H17/67 ,  D21H17/675

Abstract: A process for treating a sulfurous fluid to form gypsum and magnesium carbonate, whereby the sulfurous fluid is scrubbed with a sequestrating agent to yield a scrubbed fluid, gypsum and magnesium sulfate. The flue gas desulfurized gypsum is isolated from the magnesium sulfate solution by filtration or centrifugation. The magnesium sulfate is reacted with a carbonate salt to produce a magnesium carbonate whereby the reaction conditions are controlled to control the properties of the magnesium carbonate produced.

公开(公告)号：EP3194737A1

公开(公告)日：2017-07-26

申请号：EP15706224.1

申请日：2015-02-23

Applicant: Haldor Topsøe A/S ,  Ecospray Technologies S.r.l.

Inventor： JOHANSEN, Keld ,  ARCHETTI, Maurizio

IPC: F01N3/20 ,  F01N3/023 ,  F01N3/035 ,  F01N5/04 ,  F01N9/00 ,  F01N3/04 ,  F01N13/00 ,  F01N13/08 ,  F01N3/032 ,  B01D46/00 ,  B01D53/14 ,  B01D53/78 ,  F01N3/10

CPC classification number: B01D53/9459 ,  B01D46/0061 ,  B01D46/0068 ,  B01D53/501 ,  B01D53/9409 ,  B01D53/9418 ,  B01D53/944 ,  B01D53/9477 ,  B01D53/9495 ,  B01D2251/2067 ,  B01D2251/304 ,  B01D2251/604 ,  B01D2252/10 ,  B01D2252/1035 ,  B01D2255/1023 ,  B01D2255/20707 ,  B01D2255/20723 ,  B01D2255/20776 ,  B01D2255/9155 ,  B01D2257/302 ,  B01D2257/404 ,  B01D2257/60 ,  B01D2257/702 ,  B01D2258/01 ,  B01D2273/20 ,  B01J21/063 ,  B01J23/22 ,  B01J23/30 ,  B01J23/44 ,  B01J23/6527 ,  B01J35/0006 ,  B01J35/04 ,  F01N3/0232 ,  F01N3/0233 ,  F01N3/032 ,  F01N3/035 ,  F01N3/04 ,  F01N3/106 ,  F01N3/2066 ,  F01N5/04 ,  F01N9/002 ,  F01N13/009 ,  F01N13/0093 ,  F01N13/017 ,  F01N13/087 ,  F01N2340/06 ,  F01N2370/02 ,  F01N2410/04 ,  F01N2550/12 ,  F01N2550/14 ,  F01N2570/04 ,  F01N2590/02 ,  F01N2590/08 ,  Y02A50/2325 ,  Y02T10/16 ,  Y02T10/24 ,  Y02T10/47

Abstract: Method and system for removal of soot, ash and heavy metals, and optionally additionally NOx and SOx being present in exhaust gas from an engine operated on heavy fuel oil.

Abstract translation: 去除烟灰，灰和金属或金属化合物的方法，以及去除处理废气或发动机废气中存在的NOx和SOx。

公开(公告)号：EP3185993A1

公开(公告)日：2017-07-05

申请号：EP15756379.2

申请日：2015-08-13

Applicant: Dürr Systems AG

Inventor： RIEDER, Erhard ,  SCHRÖTER, Martin

IPC: B01D53/86 ,  B01D46/24 ,  B01D53/34

CPC classification number: B01D53/343 ,  B01D46/2407 ,  B01D53/501 ,  B01D53/8603 ,  B01D53/8631 ,  B01D53/8653 ,  B01D53/8659 ,  B01D2251/2062 ,  B01D2251/304 ,  B01D2251/404 ,  B01D2257/2045 ,  B01D2257/2047 ,  B01D2257/302 ,  B01D2257/404 ,  B01D2257/502 ,  B01D2258/0283 ,  B01D2259/65 ,  C01B32/50 ,  Y02P20/129

Abstract: In order to create an energy-efficient treatment device for treating a exhaust stream containing carbon monoxide, the treatment device comprises the following: a conversion device (140) for converting carbon monoxide into carbon dioxide, the energy released in said conversion process being used for supplying a thermal energy source and/or electricity; a purification device (124) for purifying the exhaust stream to be fed to the conversion device.

Abstract translation: 公开了处理废气流的方法和设备。 公开的用于处理含一氧化碳的排气流的示例性处理装置包括将一氧化碳转化成二氧化碳的转化装置，其中转化中释放的能量用于供应热能和/或电能。 该示例处理装置还包括清洁装置，以清洁要提供给转换装置的排气流，其中清洁装置设置在转换装置的入口的上游。

公开(公告)号：EP3170547A1

公开(公告)日：2017-05-24

申请号：EP15822300.8

申请日：2015-07-17

Applicant: Mitsubishi Hitachi Power Systems, Ltd.

Inventor： II, Shinya ,  KATAGAWA, Atsushi ,  ISHIZAKA, Hiroshi ,  SHIMAMURA, Jun

IPC: B01D53/50 ,  C01F11/46

CPC classification number: B01D53/50 ,  B01D53/501 ,  B01D53/502 ,  B01D53/504 ,  B01D53/80 ,  B01D2251/404 ,  B01D2251/606 ,  B01D2258/0283 ,  C01F11/464 ,  C04B11/264 ,  F23J15/04 ,  F23J2215/20 ,  F23J2219/50

Abstract: Provided is a method of operating a flue gas desulfurization apparatus, in which gypsum slurry containing gypsum, which is obtained by bringing sulfur oxide contained in flue gas discharged from a combustion device including a boiler into contact with an absorbing solution composed of lime slurry in an absorption tower 1 and then subjecting the same to oxidation, is withdrawn from the absorption tower 1, and said gypsum slurry is supplied into a gypsum slurry tank 6 for supplying the gypsum slurry into dehydration equipment by using a pump 5 or is circulated to the absorption tower 1. In order to reduce the capacity of the pump 5 and thereby conserve pump power, the gypsum slurry is switched to being supplied into the gypsum slurry tank 6 or being circulated to the absorption tower 1 depending on the solid content concentration of the gypsum slurry withdrawn from the absorption tower 1.

Abstract translation: 本发明提供一种烟气脱硫装置的运转方法，使含有石膏的石膏浆料与由石灰浆料构成的吸收液接触，该石膏浆料是将从包含锅炉的燃烧装置排出的排气中的硫氧化物与 从吸收塔1中取出吸收塔1，然后对其进行氧化处理，然后将所述石膏浆料送入石膏浆液槽6中，用于通过泵5将石膏浆液送入脱水设备或循环至吸收塔 塔1中。为了减小泵5的容量从而节省泵功率，根据石膏的固体含量浓度将石膏浆液切换到石膏浆液罐6中或者循环到吸收塔1中 从吸收塔1排出的浆料。

公开(公告)号：EP3145624A1

公开(公告)日：2017-03-29

申请号：EP15730883.4

申请日：2015-05-21

Applicant: The Babcock & Wilcox Company ,  GEA Process Engineering A/S

Inventor： KLIDAS, Michael ,  REDINGER, Kevin ,  MITCHELL, Joseph III ,  FEENEY, Steven ,  JACOBSEN, Niels ,  BOILESEN, Claus Erik

IPC: B01D53/50 ,  B01D53/73 ,  F23J15/02 ,  F23J15/04

CPC classification number: B01D53/73 ,  B01D53/343 ,  B01D53/50 ,  B01D53/501 ,  B01D53/56 ,  B01D53/8628 ,  B01D2251/404 ,  B01D2257/404 ,  B01D2258/0283 ,  B01D2259/126 ,  F23J15/022 ,  F23J15/04 ,  F23L15/00

Abstract: The present invention relates generally to the field of emission control equipment for boilers, heaters, kilns, or other flue gas-, or combustion gas-, generating devices (e.g., those located at power plants, processing plants, etc.) and, in particular to a new and useful method and apparatus for reducing and/or eliminating various liquid discharges from one or more emission control equipment devices (e.g., one or more wet flue gas desulfurization (WFGD) units). In another embodiment, the method and apparatus of the present invention is designed to reduce and/or eliminate the amount of liquid waste that is discharged from a WFGD unit by subjecting the WFGD liquid waste to one or more drying processes, one or more spray dryer (or spray dry) absorber processes, and/or one or more spray dryer (or spray dry) evaporation processes.

Abstract translation: 本发明涉及基因集会的排放控制设备用于锅炉，加热器，窑，或者其他产生烟道气或燃烧气体的领域中，产生装置（例如，那些位于发电厂，加工厂等），并且在 尤其涉及一种用于从一个或多个排放控制设备装置（例如，一个或多个湿烟道气脱硫（WFGD）单元）减少和/或消除各种液体排泄物一种新的和有用的方法和装置。 在另一个，由WFGD液体废物经受一个或多个干燥过程，一个或多个喷雾干燥器实施例本发明的方法和装置被设计成减少和/或消除的液体废物的量并从WFGD单元排出 （或喷雾干燥）吸收处理，和/或一个或多个喷雾干燥器（或喷雾干燥）蒸发过程。

公开(公告)号：EP3081533A1

公开(公告)日：2016-10-19

申请号：EP16159392.6

申请日：2016-03-09

Applicant: Andritz AG

Inventor： KRAMER, Michael ,  REISSNER, Harald

IPC: C02F1/24 ,  B01D53/64 ,  B04C5/26 ,  C02F1/38

CPC classification number: C02F9/00 ,  B01D53/501 ,  B01D53/64 ,  B01D53/80 ,  B01D2251/404 ,  B01D2257/602 ,  B01D2258/0283 ,  C02F1/24 ,  C02F1/38 ,  C02F1/385 ,  C02F2001/007 ,  C02F2101/20 ,  C02F2103/18 ,  C02F2301/08

Abstract: Den Gegenstand dieser Erfindung bildet ein Verfahren zur Entfernung von Quecksilber aus Wäschersuspensionen (1), die bei einer nassen Rauchgaswäsche anfallen. Die gipshaltige Suspension (1) wird mittels zumindest eines Hydrozyklons (11) eingedickt, wobei der Oberlauf (2, 4) des Hydrozyklons (11) zumindest einem Abwasserzyklon (12) zur Feststoffrückgewinnung zugeführt wird und wobei der Oberlauf (5) des Abwasserzyklons (12) anschließend in einer Abwasserreinigungsanlage (13) behandelt wird. Erfindungsgemäß wird die Quecksilberkonzentration im Oberlauf (5) des Abwasserzyklons (12) erhöht und nur der aufkonzentrierte Abwasserstrom 7 der Abwasserreinigungsanlage 13 zugeführt.

Abstract translation: 一种烟道气脱硫装置中从烟道气中去除汞的方法，其中通过增加洗涤废水中的体积相关汞浓度，减少FGD石膏中的汞浓度，而不增加废水处理厂的尺寸; 将更浓缩的废水流送入废水处理厂。

公开(公告)号：EP2896450A4

公开(公告)日：2016-04-20

申请号：EP13837947

申请日：2013-08-13

Applicant: MITSUBISHI HITACHI POWER SYS

Inventor： NAGAE SHOKO ,  KAGAWA SEIJI ,  NAGAYASU TATSUTO ,  UKAI NOBUYUKI ,  OKAMOTO TAKUYA

IPC: B01D53/34 ,  B01D53/50 ,  B01D53/64 ,  B01D53/75 ,  B01D53/86 ,  C02F1/04 ,  C02F1/26 ,  C02F1/52 ,  C02F1/56 ,  C02F1/68 ,  C02F1/72 ,  C02F9/00 ,  C02F11/12 ,  C02F101/10 ,  C02F101/20 ,  C02F103/18 ,  F23J15/00

CPC classification number: B01D53/64 ,  B01D53/346 ,  B01D53/501 ,  B01D53/502 ,  B01D53/75 ,  B01D53/78 ,  B01D53/8625 ,  B01D53/8631 ,  B01D53/8665 ,  B01D2251/2062 ,  B01D2251/404 ,  B01D2251/50 ,  B01D2255/50 ,  B01D2257/302 ,  B01D2257/404 ,  B01D2257/602 ,  B01D2258/0283 ,  C02F1/04 ,  C02F1/26 ,  C02F1/52 ,  C02F1/5245 ,  C02F1/56 ,  C02F1/683 ,  C02F1/72 ,  C02F9/00 ,  C02F11/123 ,  C02F2101/101 ,  C02F2101/20 ,  C02F2103/18 ,  C02F2209/04 ,  F23J15/006 ,  F23J2215/20 ,  F23J2215/60 ,  F23J2219/40

Abstract: The present invention is a removal system for mercury in the flue gas configured to remove Hg contained in a flue gas flowing from a boiler, and includes: a heat exchanger (AH) 18 configured to execute heat exchange for a flue gas 12 flowing from a boiler 11; a precipitator 19 configured to remove soot dust in the flue gas 12; a wet SOx removal unit 21 configured to remove mercury oxide Hg 2+ in the flue gas by alkali absorbent and desulfurize sulfur oxide in the flue gas; and an HBr compound supply unit 50 configured to supply HBr, namely, a Br compound into a flue gas duct 13 configured to discharge a flue gas from a boiler outlet. Further, enrichment of bromine contained in the alkali absorbent inside the wet SOx removal unit 21 is set to predetermined enrichment or higher. With this configuration, mercury in the flue gas is stabilized in an ionic state of Hg 2+ in gypsum slurry solution discharged from the wet SOx removal unit 21.

公开(公告)号：EP2896448A4

公开(公告)日：2016-04-06

申请号：EP13836486

申请日：2013-08-23

Applicant: MITSUBISHI HEAVY IND LTD

Inventor： ITO MOTOFUMI ,  SUGITA SATORU ,  TSUJIUCHI TATSUYA

IPC: B01D53/50 ,  B01D53/14 ,  B01D53/77 ,  F23J15/00 ,  F23J15/04

CPC classification number: B01D53/1475 ,  B01D53/1406 ,  B01D53/1481 ,  B01D53/501 ,  B01D2251/304 ,  B01D2251/402 ,  B01D2251/404 ,  B01D2251/604 ,  B01D2251/606 ,  B01D2252/2041 ,  B01D2252/20415 ,  B01D2252/20484 ,  B01D2252/20489 ,  B01D2252/20494 ,  B01D2258/0283 ,  Y02A50/2348 ,  Y02A50/2349 ,  Y02C10/06 ,  Y02E20/326

Abstract: A method of using condensed water produced in a desulfurization apparatus includes the steps of: bringing a gas to be treated, containing a sulfur dioxide and a desulfurization absorption liquid, into contact with each other to absorb and eliminate the sulfur dioxide from the gas to be treated; cooling a desulfurized gas obtained by the elimination of the sulfur dioxide to produce condensed water from the desulfurized gas; and washing the desulfurization apparatus with the condensed water. In the step of washing the desulfurization apparatus, an inlet for introducing the gas to be treated into the desulfurization apparatus may be washed with the condensed water, and a mist eliminator for eliminating the desulfurization absorption liquid accompanying the desulfurized gas from the gas may be washed with the condensed water.