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1. 发明授权

US08728423B2 Method and apparatus for flue gas treatment 有权
标题翻译：烟气处理方法和装置
公开(公告)号：US08728423B2
公开(公告)日：2014-05-20
申请号：US12098639
申请日：2008-04-07
申请人： Masaki Iijima , Hasham Mukadam , Ronald M. Weiner
发明人： Masaki Iijima , Hasham Mukadam , Ronald M. Weiner
IPC分类号： B01D53/62 , C01B31/20
CPC分类号： F01N5/02 , F01K23/10 , F22B1/1815 , F22B1/1861 , F23J2215/50 , Y02E20/326 , Y02P20/13 , Y02T10/16
摘要： A method for flue gas treatment includes branching part of a flue gas stream emitted from a gas turbine from an upstream side or a downstream side of an exhaust heat recovery boiler and subjecting the branched part to combustion with a fuel in an auxiliary boiler so as to increase carbon dioxide concentration in the branched part prior to recombining the flue gas stream from the auxiliary boiler with the remaining part of the flue gas stream from the gas turbine to form a combined flue gas stream having a carbon dioxide concentration for efficient recovery in a carbon dioxide recovery apparatus.
摘要翻译：烟道气处理方法包括从燃气轮机从排气热回收锅炉的上游侧或下游侧排出的烟道气的一部分，并使分支部分与辅助锅炉中的燃料一起燃烧，以便在将来自辅助锅炉的烟道气流与来自燃气轮机的烟道气流的剩余部分重新组合之前，增加分支部分中的二氧化碳浓度以形成具有二氧化碳浓度以在碳中有效回收的组合烟气流二氧化碳回收装置。

2. 发明授权

US09284856B2 Gas turbine combined cycle power plant with distillation unit to distill a light oil fraction 有权
$Gas turbine combined cycle power plant with distillation unit to distill a light oil fraction$
标题翻译：燃气轮机联合循环发电厂与蒸馏单元馏出轻油馏分
公开(公告)号：US09284856B2
公开(公告)日：2016-03-15
申请号：US13496904
申请日：2009-12-18
申请人： Masaki Iijima , Toyoaki Komori , Ryotaro Kanai , Takeo Araki
发明人： Masaki Iijima , Toyoaki Komori , Ryotaro Kanai , Takeo Araki
IPC分类号： F01K23/10 , F01K23/06 , C10G7/06 , B01D3/10 , F01K7/16
CPC分类号： F01K23/10 , B01D3/10 , C10G7/06 , F01K7/16 , F01K23/064 , Y02E20/16
摘要： The present invention is a gas turbine combined cycle power plant which generates electricity by fueling a gas turbine with crude oil or heavy oil and which is provided with a vacuum distillation unit which distills and extracts a light oil fraction from crude oil or heavy oil by keeping the interior thereof in an environment which lowers a boiling point of crude oil or heavy oil, and the vacuum distillation unit is provided with heaters which heat distillation materials by using low pressure steam and medium pressure steam generated in a gas turbine combined cycle.
摘要翻译：本发明是一种燃气轮机联合循环发电厂，其通过用原油或重油加油燃气轮机而发电，并且设有真空蒸馏单元，其通过保持从原油或重油中提取和提取轻质油馏分其内部在降低原油或重油的沸点的环境中，真空蒸馏单元设置有通过使用在燃气轮机联合循环中产生的低压蒸汽和中压蒸汽来加热蒸馏材料的加热器。

3. 发明授权

US09233336B2 Carbon dioxide recovery system and method 有权
标题翻译：二氧化碳回收系统及方法
公开(公告)号：US09233336B2
公开(公告)日：2016-01-12
申请号：US13338408
申请日：2011-12-28
申请人： Masaki Iijima
发明人： Masaki Iijima
IPC分类号： F01K23/06 , B63H11/12 , F02K9/50 , F03C1/00 , B01D53/14 , B01D53/56 , C01B17/16 , C01B31/20 , F23J15/00 , F01K7/06 , F01K19/00 , B01D53/62
CPC分类号： B01D53/1425 , B01D53/1475 , B01D53/62 , B01D2257/504 , B01D2258/0283 , B01D2259/65 , F01K7/06 , F01K19/00 , F23J15/006 , F23J2215/50 , F23J2219/40 , Y02A50/2342 , Y02C10/04 , Y02C10/06 , Y02E20/326
摘要： A carbon dioxide recovery system includes a high-pressure 11, a boiler 15, a carbon dioxide recovery unit 24 that includes a carbon dioxide absorber 21 that absorbs and reduces carbon dioxide in flue gas G emitted from the boiler 15 using a carbon dioxide absorbent and an absorbent regenerator 23 that regenerates a carbon dioxide absorbent having absorbed the carbon dioxide using a regenerating superheater 22 to obtain a regenerated carbon dioxide absorbent, a high-temperature and high-pressure steam extraction line L11 that extracts the high-temperature and high-pressure steam 14 from the boiler 15 before the steam is introduced into the high-pressure turbine 11, an auxiliary turbine 32 that recovers power with the high-temperature and high-pressure steam 14, and a steam supply line L12 that supplies emission steam 33 emitted from the auxiliary turbine 32 to the regenerating superheater 22 to be used as a heat source.
摘要翻译：二氧化碳回收系统包括高压11，锅炉15，二氧化碳回收单元24，二氧化碳回收单元24包括二氧化碳吸收器21，二氧化碳吸收器21使用二氧化碳吸收剂吸收和还原从锅炉15排出的烟道气G中的二氧化碳，吸收剂再生器23，其使用再生过热器22再生吸收了二氧化碳的二氧化碳吸收剂，以获得再生二氧化碳吸收剂;高温高压蒸汽提取管线L11，其提取高温高压在将蒸汽引入高压涡轮机11之前，来自锅炉15的蒸汽14，用高温高压蒸汽14回收动力的辅助涡轮机32和排出的排出蒸气33的蒸汽供给管路L12 从辅助涡轮32到再生过热器22，用作热源。

4. 发明申请

US20130206010A1 CO2 RECOVERY SYSTEM 审中-公开
标题翻译：二氧化碳回收系统
公开(公告)号：US20130206010A1
公开(公告)日：2013-08-15
申请号：US13879304
申请日：2011-07-27
申请人： Masaki Iijima , Yasuyuki Yagi , Kazuhiko Kaibara
发明人： Masaki Iijima , Yasuyuki Yagi , Kazuhiko Kaibara
IPC分类号： B01D53/14
CPC分类号： B01D53/1425 , B01D53/1475 , B01D2259/65 , Y02C10/04 , Y02C10/06 , Y02E20/326
摘要： A CO2 recovery system according to the present invention includes: a CO2 absorber that brings a cooled CO2-containing exhaust gas into contact with a CO2-absorbent that absorbs CO2, thereby removing the CO2 from the exhaust gas; an absorbent regenerator that releases CO2 from a CO2-absorbent that has absorbed CO2 (rich solution), thereby regenerating the absorbent; and a lean solution temperature-reduction unit that recovers heat from a lean solution discharged from the absorbent regenerator.
摘要翻译：根据本发明的CO 2回收系统包括：CO 2吸收器，其使冷却的含CO 2废气与吸收CO 2的CO 2吸收剂接触，从而从排气中除去CO 2; 吸收性再生器，其从吸收了二氧化碳（富溶液）的二氧化碳吸收剂中释放二氧化碳，从而再生吸收剂; 以及从吸收式再生器排出的贫溶液中回收热量的贫溶液温度降低单元。

5. 发明申请

US20120269690A1 CARBON DIOXIDE RECOVERY SYSTEM 有权
标题翻译：二氧化碳回收系统
公开(公告)号：US20120269690A1
公开(公告)日：2012-10-25
申请号：US13357929
申请日：2012-01-25
申请人： Masaki Iijima , Koji Kadono , Kazuhiko Kaibara
发明人： Masaki Iijima , Koji Kadono , Kazuhiko Kaibara
IPC分类号： B01D53/62
CPC分类号： B01D53/1475 , B01D53/1418 , B01D53/1425 , B01D2252/204 , B01D2258/0283 , B01D2259/816 , Y02A50/2342 , Y02C10/06
摘要： A carbon dioxide recovery system includes a carbon dioxide absorption tower for absorbing carbon dioxide in combustion exhaust gas into an absorbing solution by bringing the combustion exhaust gas into contact with the absorbing solution that absorbs carbon dioxide; a dissolved oxygen removing device that uses at least one device of a device for blowing bubbling gas into the rich absorbing solution into which carbon dioxide has been absorbed, a device for applying ultrasonic oscillation, and a device for heating the rich absorbing solution; a bubble removing device that turns the rich absorbing solution in the carbon dioxide absorption tower into a swirling flow or agitates the rich absorbing solution; and a regeneration tower that regenerates the absorbing solution by releasing carbon dioxide from the absorbing solution from which oxygen has been removed by the dissolved oxygen removing device and the bubble removing device and obtains carbon dioxide gas.
摘要翻译：二氧化碳回收系统包括：二氧化碳吸收塔，用于通过使燃烧废气与吸收二氧化碳的吸收溶液接触，将燃烧废气中的二氧化碳吸收到吸收溶液中; 溶解氧去除装置，其使用至少一个装置，用于将吸入气体的气体吹送到已被吸收了二氧化碳的富吸收溶液中，用于施加超声波振荡的装置和用于加热富吸收溶液的装置; 将二氧化碳吸收塔中的富吸收溶液转化为旋流或搅拌富吸收溶液的气泡去除装置; 以及再生塔，其通过从溶解氧去除装置和气泡除去装置除去氧的吸收溶液中释放二氧化碳而再生吸收溶液，并获得二氧化碳气体。

6. 发明申请

US20120255442A1 AIR POLLUTION CONTROL APPARATUS AND AIR POLLUTION CONTROL METHOD 有权
标题翻译：空气污染控制装置和空气污染控制方法
公开(公告)号：US20120255442A1
公开(公告)日：2012-10-11
申请号：US13474460
申请日：2012-05-17
申请人： Masaki Iijima
发明人： Masaki Iijima
IPC分类号： B01D45/06
CPC分类号： F23L17/005 , B01D53/346 , B01D53/62 , B01D2257/504 , F23J15/006 , F23J2215/50 , F23J2217/20 , F23L11/00 , F23L13/06 , Y02C10/04 , Y02E20/326 , Y10T137/4643 , Y10T137/86212
摘要： An air pollution control apparatus according to an embodiment of the present invention includes: a stack that discharges flue gas discharged from a boiler outside; a blower that is provided downstream of the stack and draws in the flue gas; and a CO2 recovering apparatus that recovers CO2 in the flue gas drawn in by the blower. The stack includes a controlling unit that suppresses release of the flue gas outside from the stack and suppresses inflow of atmosphere to the stack, and the controlling unit is a channel forming unit that forms a serpentine channel through which the flue gas and the atmosphere in the stack flow.
摘要翻译：根据本发明实施例的空气污染控制装置包括：排出从锅炉外部排出的烟道气的堆; 提供在烟囱下游并吸入烟道气的鼓风机; 以及CO 2回收装置，其回收由鼓风机吸入的烟道气中的CO 2。该堆叠包括控制单元，该控制单元抑制烟道气从堆叠中的释放，并抑制气氛向堆叠的流入，并且控制单元是形成蛇形通道的通道形成单元，通过该通道形成单元，烟道气体和堆流。

7. 发明申请

US20120222394A1 AIR POLLUTION CONTROL APPARATUS AND AIR POLLUTION CONTROL METHOD 有权
公开(公告)号：US20120222394A1
公开(公告)日：2012-09-06
申请号：US13474440
申请日：2012-05-17
申请人： Masaki Iijima
发明人： Masaki Iijima
IPC分类号： B01D45/08
CPC分类号： F23L17/005 , B01D53/346 , B01D53/62 , B01D2257/504 , F23J15/006 , F23J2215/50 , F23J2217/20 , F23L11/00 , F23L13/06 , Y02C10/04 , Y02E20/326 , Y10T137/4643 , Y10T137/86212
摘要： An air pollution control apparatus according to an embodiment of the present invention includes: a stack that discharges flue gas discharged from a boiler outside; a blower that is provided downstream of the stack and draws in the flue gas; and a CO2 recovering apparatus that recovers CO2 in the flue gas drawn in by the blower. The stack includes a controlling unit that suppresses release of the flue gas outside from the stack and suppresses inflow of atmosphere to the stack, and the controlling unit is a channel forming unit that forms a serpentine channel through which the flue gas and the atmosphere in the stack flow.

8. 发明授权

US08231719B2 Absorbent liquid, and apparatus and method for removing CO2 or H2S from gas with use of absorbent liquid 有权
标题翻译：吸收液体，以及使用吸收液体从气体中除去CO 2或H 2 S的装置和方法
公开(公告)号：US08231719B2
公开(公告)日：2012-07-31
申请号：US12308086
申请日：2006-06-12
申请人： Ryuji Yoshiyama , Masazumi Tanoura , Noriko Watari , Shuuji Fujii , Yukihiko Inoue , Mitsuru Sakano , Tarou Ichihara , Masaki Iijima , Tomio Mimura , Yasuyuki Yagi , Kouki Ogura
发明人： Ryuji Yoshiyama , Masazumi Tanoura , Noriko Watari , Shuuji Fujii , Yukihiko Inoue , Mitsuru Sakano , Tarou Ichihara , Masaki Iijima , Tomio Mimura , Yasuyuki Yagi , Kouki Ogura
IPC分类号： B01D53/14
CPC分类号： B01D53/1462 , B01D53/1493 , Y02C10/04 , Y02C10/06
摘要： An absorbent liquid according to the present invention is an absorbent liquid for absorbing CO2 or H2S or both from gas, in which the absorbent liquid includes an alkanolamine as a first compound component, and a second component including a nitrogen-containing compound having in a molecule thereof two members or more selected from a primary nitrogen, a secondary nitrogen, and a tertiary nitrogen or a nitrogen-containing compound having in a molecule thereof all of primary, secondary, and tertiary nitrogens. The absorbent liquid has an excellent absorption capacity performance and an excellent absorption reaction heat performance, as compared to an aqueous solution containing solely an alkanolamine and a nitrogen-containing compound in the same concentration in terms of wt %, and can recover CO2 or H2S or both from gas with smaller energy.
摘要翻译：根据本发明的吸收液体是用于从气体吸收CO 2或H 2 S或两者的吸收液体，其中吸收剂液体包括作为第一化合物组分的链烷醇胺，和包含分子中的含氮化合物的第二组分其中选自初级氮，次氮和叔氮或含有一分，分子中的一级，二级和次级氮的含氮化合物的两个或更多个成员。与仅含有以wt％计相同浓度的链烷醇胺和含氮化合物的水溶液相比，吸收液体具有优异的吸收能力性能和优异的吸收反应热性能，并且可以回收CO 2或H 2 S或两者都来自具有较小能量的气体。

9. 发明授权

US08016919B2 CO2 recovery system and solid-particles removing method for use in the same 有权
标题翻译：二氧化碳回收系统和固体颗粒去除方法用于其中
公开(公告)号：US08016919B2
公开(公告)日：2011-09-13
申请号：US12022468
申请日：2008-01-30
申请人： Masaki Iijima , Takashi Kamijo
发明人： Masaki Iijima , Takashi Kamijo
IPC分类号： B01D53/14
CPC分类号： B01D53/73 , B01D53/1425 , B01D53/1475 , B01D53/62 , Y02C10/04 , Y02C10/06 , Y02P20/152
摘要： A solution contained in a regeneration tower is supplied to a filtering unit. The filter unit filters out solid particles contained in the solution. A washing unit washes out with backwash water solid particles filtered out by the filter unit. An evaporating unit receives the backwash water containing the solid particles, and heats received backwash water thereby obtaining solid-particles concentrated backwash water.
摘要翻译：包含在再生塔中的溶液被提供给过滤单元。过滤器单元过滤掉溶液中包含的固体颗粒。用洗涤水清洗洗涤单元，过滤单元过滤出的反冲洗水固体颗粒。蒸发单元接收含有固体颗粒的回洗水，并加热接收反冲洗水，从而获得固体颗粒集中的反冲洗水。

10. 发明申请

US20110113965A1 CO2 RECOVERY SYSTEM AND METHOD 有权
标题翻译：二氧化碳回收系统和方法
公开(公告)号：US20110113965A1
公开(公告)日：2011-05-19
申请号：US13013419
申请日：2011-01-25
申请人： Masaki Iijima , Takashi Kamijo , Takahito Yonekawa , Tomio Mimura , Yasuyuki Yagi
发明人： Masaki Iijima , Takashi Kamijo , Takahito Yonekawa , Tomio Mimura , Yasuyuki Yagi
IPC分类号： B01D53/14
CPC分类号： B01D53/14 , B01D53/1406 , B01D53/1425 , B01D53/1475 , B01D53/62 , B01D2258/0283 , B01D2259/65 , Y02A50/2342 , Y02C10/04 , Y02C10/06
摘要： A CO2 recovery system includes an absorption tower and a regeneration tower. CO2 rich solution is produced in the absorption tower by absorbing CO2 from CO2-containing gas. The CO2 rich solution is conveyed to the regeneration tower where lean solution is produced from the rich solution by removing CO2. A regeneration heater heats lean solution that accumulates near a bottom portion of the regeneration tower with saturated steam thereby producing steam condensate from the saturated steam. A steam-condensate heat exchanger heats the rich solution conveyed from the absorption tower to the regeneration tower with the steam condensate.
摘要翻译： CO2回收系统包括吸收塔和再生塔。通过从含CO 2的气体吸收CO 2在吸收塔中产生富CO 2溶液。将富含二氧化碳的溶液输送到再生塔，通过除去CO 2从富溶液中产生贫溶液。再生加热器用饱和蒸汽加热在再生塔的底部附近积聚的贫溶液，从而产生来自饱和蒸汽的蒸汽冷凝物。蒸汽冷凝热交换器将从吸收塔输送的富溶液与蒸汽冷凝物加热到再生塔。

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