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1. 发明专利

JP2015031204A 海流発電設備及び海流発電設備の係留方法有权
标题翻译：海洋电流发电设备及其运行方法
公开(公告)号：JP2015031204A
公开(公告)日：2015-02-16
申请号：JP2013161292
申请日：2013-08-02
申请人：三菱重工業株式会社 , Mitsubishi Heavy Ind Ltd
发明人： IIJIMA MASAKI , NAKATANI HIROKI , KAHATA TATSUO
IPC分类号： F03B13/26
CPC分类号： F03B17/061 , F03B13/264 , F05B2240/911 , F05B2240/917 , F05B2240/97 , Y02E10/28 , Y02P70/527
摘要：【課題】海流の速い場所で高発電量を得ることができ、海流発電装置を係留するために新設する係留設備の規模や、海流発電装置で発生した電力の送電設備の規模を低減することが可能な海流発電設備及び海流発電設備の係留方法を提供することを目的とする。【解決手段】海流発電設備1は、海流によって回転する翼4、及び、翼4の回転力によって発電する発電機を有する、海中に浮遊して設置される海流発電装置2と、一端が海流発電装置2に接続され、他端が海底20に対して固定又は係留された石油又は天然ガス生産用プラットフォーム10に接続される係留ワイヤ3とを備える。【選択図】図1
摘要翻译：要解决的问题：提供一种能够在具有快速洋流的位置获得高发电能力的海洋电力发电设备和系泊方法，并且减少新建的用于将洋流放电的系泊设备的规模发电装置和用于传输由海洋电力发电设备产生的电力的电力传输设备。解决方案：海洋电力发电设备1包括：海洋电力发电装置2，其具有由洋流旋转的叶片4和发电机通过叶片4的旋转产生电力并悬浮在海水中; 以及一个系泊绳3，其一端连接到洋流发电装置2，另一端连接到平台10，用于油或天然气的生产，固定或锚固到海底20。

2. 发明专利

JP2014084265A Saturator and natural gas modification therewith 有权
标题翻译：饱和度和天然气改性剂
公开(公告)号：JP2014084265A
公开(公告)日：2014-05-12
申请号：JP2012236672
申请日：2012-10-26
申请人： Mitsubishi Heavy Ind Ltd , 三菱重工業株式会社
发明人： IIJIMA MASAKI , MATSUZAWA MASATO
IPC分类号： C01B3/38
CPC分类号： F16L53/002 , B01J19/24 , C01B3/34 , C01B3/384 , C01B2203/0233 , C01B2203/0805 , C01B2203/0811 , C01B2203/1058 , C01B2203/1241 , C01B2203/1276 , F16L53/32 , Y10T137/6579
摘要： PROBLEM TO BE SOLVED: To provide a saturator capable of more efficiently recovering heat from a heat source so as to be utilized and adding water vapor into a fluid to the maximum, and a natural gas modification system provided therewith.SOLUTION: In the saturator 20 comprising; a circulation passage through which a first fluid circulates at the inside;a first heat exchange part 22 of performing heat exchange between the first fluid and a second fluid; a second heat exchange part 23 of performing heat exchange between the first fluid after the passage of the first heat exchange part 22 and a third fluid; a humidification part 26, in the upstream side of the first fluid of the first heat exchange part 22 and the second heat exchange part 23, adding water to the first fluid; and a transportation passage 25 of transporting the third fluid after the heat exchange to the upstream side of the first heat exchange part 22 from the second heat exchange part 23, and flowing the same into the circulation passage as the first fluid; the first fluid is heated and humidified in the first heat exchange part 22, the second fluid is cooled and is exhausted to the outside of the system, the first fluid is heated and humidified to a saturation vapor pressure in the second heat exchange part 23 so as to be exhausted to the outside of the system, and the third fluid is cooled.
摘要翻译：要解决的问题：提供一种能够更有效地从热源回收热量以便最大程度地利用并将水蒸气加入到流体中的饱和器以及由其提供的天然气改性系统。解决方案：在饱和器20 包括; 第一流体在内部循环通过的循环通道;在第一流体和第二流体之间进行热交换的第一热交换部22; 在第一热交换部22通过后的第一流体与第三流体之间进行热交换的第二热交换部23; 加湿部26，在第一热交换部22的第一流体和第二热交换部23的上游侧，向第一流体添加水; 以及将热交换后的第三流体从第二热交换部23输送到第一热交换部22的上游侧并将其作为第一流体流入循环通道的输送路25; 第一流体在第一热交换部22中被加热和加湿，第二流体被冷却并排出到系统的外部，第一流体被加热并加湿到第二热交换部23中的饱和蒸汽压，因此被排出到系统的外部，并且第三流体被冷却。

3. 发明专利

JP2011005368A Co2 recovering apparatus and method 审中-公开
标题翻译：二氧化碳回收装置和方法
公开(公告)号：JP2011005368A
公开(公告)日：2011-01-13
申请号：JP2009149032
申请日：2009-06-23
申请人： Kansai Electric Power Co Inc:The , Mitsubishi Heavy Ind Ltd , 三菱重工業株式会社 , 関西電力株式会社
发明人： IIJIMA MASAKI , TANAKA YUJI , SORIMACHI MIKI , TATSUMI MASAHIKO , YAGI YASUYUKI , OGURA KOKI
IPC分类号： B01D53/62 , B01D53/14 , C01B32/50
CPC分类号： Y02A50/2342 , Y02P20/152
摘要： PROBLEM TO BE SOLVED: To provide a COrecovering apparatus and method, wherein operation with less regeneration energy to be consumed when an absorbing liquid is regenerated can be conducted when a constant recovery rate is maintained.SOLUTION: The COrecovering apparatus includes: a COabsorption column 16 in which flue gas 12 containing COis brought into contact with a COabsorbing liquid 15 to remove COcontained in the flue gas 12; and a regeneration column 18 in which COcontained in a rich solution 17, in which COis absorbed in the COabsorption column 16, is removed to regenerate the rich solution, and is constituted so that a lean solution being the COabsorbing liquid 15, from which COis removed in the regeneration column 18, is reused in the COabsorption column 16, and further includes a control means for detecting the temperature of the flue gas to be introduced into the COabsorption column 16, decreasing or increasing a circulation rate of the COabsorbing liquid 15 according to a change in the detected temperature, and adjusting the amount of steam to be supplied to the regeneration column 18 according to the amount of the COabsorbing liquid 15 to be circulated.
摘要翻译：要解决的问题：提供一种COrecovering装置和方法，其中当保持恒定的回收率时，可以进行在再生吸收液体时消耗的再生能量较少的操作。解决方案：COrecovering装置包括：CO吸收塔16 其中含有COIS的烟道气12与CO吸收液体15接触以除去烟道气12中的CO; 在CO吸收塔16中吸收CO 2的富含溶液17中的CO被还原的再生塔18被除去以再生富溶液，并且构成为使得作为除去CO 2的吸收液15的贫溶液在再生塔18中重新使用在CO吸收塔16中，并且还包括控制装置，用于检测引入到CO吸收塔16中的烟道气的温度，根据下述方式减少或提高吸收液15的循环速度检测温度的变化，以及根据待循环的吸收液15的量调节供给至再生塔18的蒸汽量。

4. 发明专利

JP2010207686A Apparatus and method for treating exhaust gas 有权
标题翻译：用于处理排气的装置和方法
公开(公告)号：JP2010207686A
公开(公告)日：2010-09-24
申请号：JP2009055291
申请日：2009-03-09
申请人： Mitsubishi Heavy Ind Ltd , 三菱重工業株式会社
发明人： IIJIMA MASAKI
IPC分类号： B01D53/62 , C01B32/50
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： PROBLEM TO BE SOLVED: To provide an apparatus and a method for treating exhaust gas which can steadily and stably suck into a CO 2 recovering device a nearly whole amount of exhaust gas exhausted to the atmosphere from a stack in a simple structure while minimizing the air sucked from the atmosphere. SOLUTION: A first apparatus 10A for treating exhaust gas includes the stack 15 discharging to the outside the exhaust gas 12 exhausted from a boiler 21, a blower 13 installed downstream of the stack 15 to take in the exhaust gas 12, and the CO 2 recovering device 22 recovering the CO 2 in the exhaust gas 12 taken in by the blower 13, and a flow-passage forming means 23A forming a meandering flow passage where the exhaust gas 12 and the air 17 flow is installed inside the stack 15 as a restricting means which suppresses the discharge of the exhaust gas 12 from the stack 15 to the outside and which restricts the inflow of the air 17 to the inside of the stack 15. COPYRIGHT: (C)2010,JPO&INPIT
摘要翻译：要解决的问题：为了提供一种能够稳定和稳定地吸入CO 2 回收装置的废气处理装置和方法，从废气中排出的几乎全部废气排放到大气中一个简单结构的堆栈，同时最大限度地减少从大气吸入的空气。解决方案：用于处理废气的第一装置10A包括从锅炉21排出的排气12向外部排出的堆15，安装在堆15的下游以吸入废气12的鼓风机13，以及回收装置22回收由鼓风机13吸入的废气12中的CO 2 ，以及形成曲折流动通道的流路形成装置23A，废气12和空气17流被安装在堆叠15内作为限制装置，其限制排气12从堆15排放到外部并限制空气17流入堆15的内部。版权所有（C）2010，JPO＆INPIT

5. 发明专利

JP2008126154A Treatment method and treatment apparatus of exhaust gas 有权
标题翻译：排气处理方法及处理装置
公开(公告)号：JP2008126154A
公开(公告)日：2008-06-05
申请号：JP2006314860
申请日：2006-11-21
申请人： Kansai Electric Power Co Inc:The , Mitsubishi Heavy Ind Ltd , 三菱重工業株式会社 , 関西電力株式会社
发明人： HIRATA TAKUYA , TANAKA YUJI , TAKASHINA TORU , IIJIMA MASAKI , MIMURA TOMIO , YAGI YASUYUKI , ISHIDA KAZUO
IPC分类号： B01D53/50 , B01D53/34 , B01D53/62 , B01D53/77
CPC分类号： Y02A50/2342 , Y02C10/04
摘要： PROBLEM TO BE SOLVED: To suppress an increase of operation cost in a treatment method and a treatment apparatus of an exhaust gas by reliably removing sulfur oxide from the exhaust gas and decreasing the sulfur oxide accumulated in a decarbonation absorption solution. SOLUTION: The treatment apparatus comprises a high-power desulfurization gas cooling treatment apparatus 12 for removing sulfur oxide by bringing an exhaust gas into contact with a basic absorption solution and at the same time cooling the exhaust gas, a decarbonation treatment apparatus 13 for removing carbon dioxide from the exhaust gas treated by the high-power desulfurization and cooling treatment, and a water supply line 93 as an absorption solution dilution means for supplying diluting water to the basic absorption solution to be used in the high-power desulfurization gas cooling treatment apparatus 12. COPYRIGHT: (C)2008,JPO&INPIT
摘要翻译：解决方案：通过从废气中可靠地除去硫氧化物并减少积聚在脱碳吸收溶液中的硫氧化物，来抑制废气处理方法和处理装置中的操作成本的增加。解决方案：处理装置包括用于通过使废气与碱性吸收溶液接触并同时冷却废气来除去硫氧化物的大功率脱硫气体冷却处理装置12，脱碳处理装置13 用于从通过高功率脱硫和冷却处理处理的废气中除去二氧化碳，以及作为用于向用于大功率脱硫气体的碱性吸收溶液供给稀释水的吸收溶液稀释装置的供水管线93 冷却处理设备12.版权所有（C）2008，JPO＆INPIT

6. 发明专利

JP2007284272A Apparatus and method for recovering co2 有权
标题翻译：用于回收二氧化碳的装置和方法
公开(公告)号：JP2007284272A
公开(公告)日：2007-11-01
申请号：JP2006111302
申请日：2006-04-13
申请人： Kansai Electric Power Co Inc:The , Mitsubishi Heavy Ind Ltd , 三菱重工業株式会社 , 関西電力株式会社
发明人： TANAKA YUJI , TAKASHINA TORU , HIRATA TAKUYA , IIJIMA MASAKI , MIMURA TOMIO , YAGI YASUYUKI
IPC分类号： C01B32/50 , B01D53/14 , B01D53/62
CPC分类号： Y02A50/2342 , Y02C10/06 , Y02P20/152
摘要： PROBLEM TO BE SOLVED: To provide an apparatus and method for recovering CO 2 by which the discharge amount of a CO 2 absorption liquid entrained by exhaust gas freed of CO 2 is reduced and the recovery efficiency of the CO 2 absorption liquid is further enhanced. SOLUTION: The apparatus for recovering CO 2 includes: an absorption tower in which CO 2 -containing exhaust gas is brought into contact with a CO 2 absorption liquid to remove the CO 2 ; and a regeneration tower in which a rich solution containing absorbed CO 2 is regenerated, wherein a lean solution freed of CO 2 in the regeneration tower is reused in the absorption tower. The absorption tower comprises: a CO 2 recovery section in which CO 2 in exhaust gas is absorbed in the CO 2 absorption liquid; a washing section in which gas freed of CO 2 is cooled and CO 2 absorption liquid entrained by the gas is recovered; a circulation line for directly circulating condensed water containing the CO 2 absorption liquid condensed in the washing section from the top of the washing section; and a surplus condensed water supply line for supplying a surplus of the condensed water containing the CO 2 absorption liquid to a lean solution supply pipe for supplying the lean solution from the regeneration tower to the absorption tower. COPYRIGHT: (C)2008,JPO&INPIT
摘要翻译：要解决的问题：提供一种用于回收CO 2 的装置和方法，通过该装置和方法，释放出CO的废气所夹带的CO 2 吸收液体的排出量 2 降低，并且进一步提高CO 2 SB吸收液的回收效率。解决方案：用于回收CO 2 的装置包括：使CO 2 的废气与CO 2 接触的吸收塔， / SB>吸收液以除去CO 2 ; 再生再生塔，其中含有吸收的CO 2 的富溶液再生，其中在再生塔中不含CO 2 SB的稀溶液再次用于吸收塔中。吸收塔包括：排气中的CO 2 CO吸收液体中的CO 2 回收段; 回收其中除去CO 2 的气体的清洗部分，并且回收由气体夹带的CO 2 吸收液体; 用于直接循环冷凝水的循环管线，所述冷凝水含有从洗涤部分的顶部在洗涤部分中冷凝的CO 2 SB吸收液; 以及剩余的冷凝水供给管线，用于将含有CO 2 SBS吸收液体的剩余的冷凝水供给到用于将稀溶液从再生塔供给到吸收塔的稀溶液供给管。版权所有（C）2008，JPO＆INPIT

7. 发明专利

JP2006159163A Method for separating methane isotope from high pressure gaseous starting material and separating apparatus therefor 审中-公开
标题翻译：从高压气体起动材料分离甲烷同位素的方法及其分离装置
公开(公告)号：JP2006159163A
公开(公告)日：2006-06-22
申请号：JP2004358858
申请日：2004-12-10
申请人： Mitsubishi Heavy Ind Ltd , Tokyo Electric Power Co Inc:The , 三菱重工業株式会社 , 東京電力株式会社
发明人： YASUTAKE AKINORI , ASAKAWA HARUMA , IIJIMA MASAKI , KARASAWA SHINJI , YOSHIDA SATOYUKI , IZUMI JUN
IPC分类号： B01D59/26 , B01D53/04 , C07C7/12 , C07C9/04
摘要： PROBLEM TO BE SOLVED: To provide a separating method and a separating apparatus capable of compactly separating and concentrating a methane isotope.
SOLUTION: A high-pressure source gas is contacted with an adsorption system comprising a selective adsorbent selectively adsorbing
12 CH
4 among methane isotopes therein, so as to adsorb
12 CH
4 on the selective adsorbent. Further, the gas other than
12 CH
4 is made to flow, so as to be recovered, and the selective adsorbent is led to a pressure lower than that at the time of the adsorption, thus
12 CH
4 -enriched gas is desorbed, and the selective adsorbent is regenerated. In this way, the methane isotope can be efficiently separated.
COPYRIGHT: (C)2006,JPO&NCIPI
摘要翻译：要解决的问题：提供能够紧密分离和浓缩甲烷同位素的分离方法和分离装置。解决方案：将高压源气体与包含选择性吸附剂的吸附系统接触，所述吸附系统选择性地吸附其中的甲烷同位素中的 CH 4 SP> 12 CH 4 。此外，除了 12 CH 4 之外的气体流动以便回收，并且选择性吸附剂被引导到低于因此吸附，因此富含气体的 12 CH 4 气体被解吸，并且选择性吸附剂被再生。以这种方式，可以有效地分离甲烷同位素。版权所有（C）2006，JPO＆NCIPI

8. 发明专利

JP2005349299A Freshwater production apparatus 审中-公开
标题翻译：水泥生产设备
公开(公告)号：JP2005349299A
公开(公告)日：2005-12-22
申请号：JP2004172380
申请日：2004-06-10
申请人： Mitsubishi Heavy Ind Ltd , 三菱重工業株式会社
发明人： OGURA KAZUMASA , IIJIMA MASAKI
IPC分类号： C02F1/04 , B01D1/14 , B01D1/16 , B01D5/00 , C02F1/12 , C02F1/16 , C02F1/26
CPC分类号： C02F1/16 , B01D1/14 , B01D1/16 , B01D5/003 , C02F1/12 , C02F1/265 , C02F2103/08 , Y02A20/128
摘要： PROBLEM TO BE SOLVED: To provide a small-scaled freshwater production apparatus at a low cost.
SOLUTION: The freshwater production apparatus using exhaust combustion gas 11 and seawater 12 comprises a sprinkler 15 which sprays the seawater 12 onto the exhaust combustion gas 11 to evaporate water in the seawater and to humidify and cool the exhaust combustion gas to a saturation temperature, and a freshwater recovery device 17 which cools the humidified and cooled exhaust combustion gas 16 to condense and recover freshwater. Water in the exhaust combustion gas is recovered together with the water in the seawater to efficiently produce the freshwater.
COPYRIGHT: (C)2006,JPO&NCIPI
摘要翻译：要解决的问题：以低成本提供小型淡水生产设备。解决方案：使用排气燃烧气体11和海水12的淡水生产设备包括喷洒器15，其将海水12喷射到排气燃烧气体11上以蒸发海水中的水并且将排气燃烧气体加湿并且冷却至饱和温度和淡水回收装置17，其冷却加湿和冷却的废气燃烧气体16以冷凝和回收淡水。排气燃烧气体中的水与海水中的水一起回收以有效地产生淡水。版权所有（C）2006，JPO＆NCIPI

9. 发明专利

JPH11270355A FULL FIRED HEAT RECOVERY THERMAL ELECTRIC POWER GENERATING EQUIPMENT 失效
公开(公告)号：JPH11270355A
公开(公告)日：1999-10-05
申请号：JP7153798
申请日：1998-03-20
申请人： MITSUBISHI HEAVY IND LTD
发明人： KANBARA MASAMICHI , OTA KAZUHIRO , IIJIMA MASAKI , SHIBATA MASATOSHI
IPC分类号： F02C7/22 , C10G9/00 , F23C6/04
摘要： PROBLEM TO BE SOLVED: To improve the power generating efficiency while obtaining various fuel with a supply of the only heavy fuel oil and while operating an equipment as a combined electric power generating equipment by providing a heavy fuel oil decomposing unit, a gas turbine, and a boiler for receiving the exhaust gas from the gas turbine and while burning the heavy oil as a fuel. SOLUTION: This power generating equipment includes a heavy fuel oil decomposing unit including a heavy fuel oil heating and decomposing device 1, a gas turbine 2 and a boiler 3 as main equipment. The heavy fuel oil is heated for decomposition by the heavy fuel oil heating and decomposing device 1 so as to obtain the decomposed material including three components of heavy oil, light oil and light gas. The gas turbine 2 rotates a turbine while burning the light oil from the heavy fuel oil decomposing unit. Since oxygen is left in the exhaust gas from the gas turbine 2, the left oxygen is fed to the boiler 3 so as to be used as the combustion air with the recovery of the waste heat. The boiler 3 burns the heavy fuel oil, the heavy oil or the heavy fuel oil from the heavy fuel oil decomposing unit and the heavy oil from the heavy fuel oil decomposing unit as a fuel. The light gas can operate the heavy fuel oil decomposing device 1.

10. 发明专利

JPH11137960A METHOD FOR CONTROL LIQUID CARBON DIOXIDE ABSORBENT AND DEVICE THEREFOR 失效
公开(公告)号：JPH11137960A
公开(公告)日：1999-05-25
申请号：JP32390597
申请日：1997-11-11
申请人： KANSAI ELECTRIC POWER CO , MITSUBISHI HEAVY IND LTD
发明人： MIMURA TOMIO , SATSUMI SHICHIROU , IIJIMA MASAKI , MITSUOKA SHIGEAKI , TANAKA YUJI , IWAKI KAN
IPC分类号： B01D53/34 , B01D53/14 , B01D53/62
摘要： PROBLEM TO BE SOLVED: To provide the method and device for keeping the amt. and concn. of a liq. absorbent constant in a decarbonation equipment to stabilize decarbonation and especially their continuous method and device. SOLUTION: In the decarbonation equipment having an absorption tower having an amine recovery part and a regeneration tower, a discharged absorbent storage tank 13, a feed absorbent storage tank 12, an amine-contg. water storage tank 6, a level gage 17 furnished at a liq. level measurable part, the continuous densitometer 20 and flowmeter 16 provided to an absorbent feed line to the absorption tower, a flow control valve 24 furnished to a discharged absorbent discharge line, a flow control valve 24 provided to a concd. absorbent feed line and a flow control valve 19 furnished to a regulating amine-contg. water feed line are provided, and an opening degree of the flow control valve 19, flow control valve 22 and flow control valve 24 is controlled based on the values of the level gage 17, densitometer 20 and flowmeter 16 to keep the amt. of the absorbent in the system and the amine concn. and flow rate of the absorbent to be supplied to the absorption tower respectively at the specified value.

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