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1. 发明专利

JP2012164456A Heat dissipation plate for secondary battery and method of manufacturing the same, and secondary battery module with heat dissipation plate 审中-公开
标题翻译：用于二次电池的散热板及其制造方法以及具有热释放板的二次电池模块
公开(公告)号：JP2012164456A
公开(公告)日：2012-08-30
申请号：JP2011022488
申请日：2011-02-04
申请人： Furukawa Sky Kk , Kawasaki Heavy Ind Ltd , 古河スカイ株式会社 , 川崎重工業株式会社
发明人： SHIIZAKI SHINJI , NISHIMURA KAZUYA , NONAKA YOSHIHARU , HIRANO TAKASHI , GOMI SHIGERU
IPC分类号： H01M10/60 , H01M10/613 , H01M10/625 , H01M10/647 , H01M10/651 , H01M10/652 , H01M10/653 , H01M10/6551 , H01M10/6555 , H01M10/6557 , H01M10/6561 , H01M10/6563 , H01M10/6567
CPC分类号： Y02E60/12
摘要： PROBLEM TO BE SOLVED: To provide a heat dissipation plate having a simple structure and a high cooling efficiency.SOLUTION: The heat dissipation plate 1 has a contour of rectangular plate, and is provided internally with a plurality of hollow portions 11, and a protrusion 12 in the shape of a triangular plate. The hollow portions 11 are used as passages through which air is distributed as a cooling medium. The protrusion 12 is formed by pressing the heat dissipation plate 1 from the upper surface thereof by means of a triangular cutter, cutting the two sides, and then folding and raising the plate toward the passage 11 around one remaining side. The protrusion 12 is inclined in the direction of air distribution, and raised so that the height of the protrusion 12 is equal to about one half that of the passage. Consequently, the high temperature air near the inner wall of the passage and the low temperature air near the center of the passage are mixed. The air temperature is thereby made uniform and drops below the temperature near the inner wall of the passage.
摘要翻译：要解决的问题：提供一种具有简单结构和高冷却效率的散热板。解决方案：散热板1具有矩形板的轮廓，并且设置有多个中空部分11和三角形板形的突起12。中空部11被用作作为冷却介质分配空气的通道。突起12通过三角形切割器从其上表面按压散热板1而形成，切割两侧，然后在剩余的一侧围绕通道11折叠并升高板。突起12在空气分配方向上倾斜，并且突起部12的高度等于通道的高度的一半。因此，通道内壁附近的高温空气和通道中心附近的低温空气混合。由此使空气温度均匀，并降低到通道内壁附近的温度。版权所有（C）2012，JPO＆INPIT

2. 发明专利

JP2012153761A Method for producing low-grade coal slurry, apparatus for producing low-grade coal slurry, and gasification system of low-grade coal 有权
标题翻译：生产低等级煤浆的方法，生产低等级煤浆的装置和低等级煤的气化系统
公开(公告)号：JP2012153761A
公开(公告)日：2012-08-16
申请号：JP2011012154
申请日：2011-01-24
申请人： Kawasaki Heavy Ind Ltd , 川崎重工業株式会社
发明人： TAKAO SHOICHI , NISHIMURA MOTOHIKO , NONAKA YOSHIHARU , KUMADA NORIHIKO , KIMURA NORIYUKI , MORI SHOICHI
IPC分类号： C10L1/32 , C10J3/46 , C10L9/08
CPC分类号： C10L1/326 , C10J3/506 , C10J2300/0906 , C10J2300/0909 , C10J2300/093 , C10J2300/094
摘要： PROBLEM TO BE SOLVED: To provide a simple method and a simple apparatus for producing low-grade coal slurry that has high slurry concentration and low viscosity and is suitable for gasification by a pressurized gasification furnace, and a gasification system equipped with such a production apparatus.SOLUTION: The method for producing the low-grade coal slurry comprises: a first step of heat-drying coarsely crushed low-grade coal and recovering, as condensed water, steam discharged from the low-grade coal; and a second step of adding the condensed water obtained in the first step and a dispersant to the dry-heated low-grade coal and slurrying the low-grade coal by a wet-crushing method. The apparatus for producing the low-grade coal slurry comprises: a drying apparatus for heat-drying coarsely crushed low-grade coal; a condensed water-recovering apparatus for recovering, as condensed water, steam discharged from the low-grade coal by heat-drying; and a wet-crushing apparatus for slurrying the heat-dried low-grade coal by adding condensed water and a dispersant thereto.
摘要翻译：要解决的问题：提供一种简单的方法和用于生产具有高浆液浓度和低粘度并且适合于通过加压气化炉气化的低等级煤浆的简单方法和装备有这样的气化系统的气化系统一个生产设备。解决方案：低级煤浆的生产方法包括：将粗粉碎的低级煤加热干燥的第一步骤，作为冷凝水回收低品位煤排放的蒸汽; 以及将第一步骤中得到的冷凝水和分散剂加入到干燥低温煤中的第二步骤，并通过湿式破碎法将低等级的煤粉化。用于生产低级煤浆的设备包括：用于对粗粉碎的低等级煤进行加热干燥的干燥装置; 冷凝水回收装置，用于回收通过加热干燥从低级煤排出的蒸汽作为冷凝水; 以及通过向其中加入冷凝水和分散剂使经热处理的低级煤浆料化的湿式破碎装置。版权所有（C）2012，JPO＆INPIT

3. 发明专利

JP2002286218A UNBURNED CHAR BURNER 失效
公开(公告)号：JP2002286218A
公开(公告)日：2002-10-03
申请号：JP2001086483
申请日：2001-03-26
申请人： KAWASAKI HEAVY IND LTD
发明人： YOSHIYAMA TAKASHI , HIROKAWA MASATOSHI , NONAKA YOSHIHARU , FUJIYAMA HIROSHI , FUJITA HIROSHI
IPC分类号： F23G7/00 , F23D1/02 , F23G5/32 , F23G5/44 , F23G5/50
摘要： PROBLEM TO BE SOLVED: To prevent a floor passage from being clogged with foreign matter contained in unburned char, realize a system capable of stable operation over a long period of time, and adjust unburned char and turning force of carrier air. SOLUTION: A fuel burner 12 is provided in an axial direction of a burner body 10, outside of which burner 12 a conveyance flow passage 14 for unburned char and carrier air is formed circumferentially, upstream of which flow passage 14 a turning wind box 20 is provided. A conveyance pipe 22 for unburned char and conveying air is connected tangentially with respect to the turning wind box 20 and is connected, inclined downstream, and is further supported on a rotary bearing in the vicinity of a connection portion with the turning wind box 20 and is made movable to adjust the unburned char and the carrier air.

4. 发明专利

JP2012153760A Method for producing low-grade coal slurry, apparatus for producing low-grade coal slurry, and gasification system of low-grade coal 有权
标题翻译：生产低等级煤浆的方法，生产低等级煤浆的装置和低等级煤的气化系统
公开(公告)号：JP2012153760A
公开(公告)日：2012-08-16
申请号：JP2011012153
申请日：2011-01-24
申请人： Kawasaki Heavy Ind Ltd , 川崎重工業株式会社
发明人： TAKAO SHOICHI , NISHIMURA MOTOHIKO , NONAKA YOSHIHARU , KUMADA NORIHIKO , KIMURA NORIYUKI , MORI SHOICHI
IPC分类号： C10L1/32 , C10J3/46
CPC分类号： C10L1/326 , C10J3/506 , C10J2300/0906 , C10J2300/0909 , C10J2300/093 , C10J2300/094
摘要： PROBLEM TO BE SOLVED: To provide a simple method and a simple apparatus for producing low-grade coal slurry that has high slurry concentration and low viscosity and is suitable for gasification by a pressurized gasification furnace, and a gasification system equipped with such a production apparatus.SOLUTION: The method for producing the low-grade coal slurry comprises: a first step of reforming coarsely crushed low-grade coal at a high temperature under high pressure; and a second step of adding water and a dispersant to the reformed low-grade coal and slurrying the low-grade coal by a wet-crushing method. The apparatus for producing the low-grade coal slurry comprises: a dry-crushing apparatus 1 for dry-crushing low-grade coal; a high-temperature high-pressure kneading apparatus 2 for reforming the dry-crushed low-grade coal; and a wet-crushing apparatus 5 for slurrying the reformed low-grade coal by adding water and a dispersant discharged from the low-grade coal by the reforming treatment.
摘要翻译：要解决的问题：提供一种简单的方法和用于生产具有高浆液浓度和低粘度并且适合于通过加压气化炉气化的低等级煤浆的简单方法和装备有这样的气化系统的气化系统一个生产设备。解决方案：低级煤浆的生产方法包括：在高压下在高压下对粗粉碎的低品位煤进行重整的第一步骤; 第二步是向改性的低档煤中加入水和分散剂，并通过湿式破碎法将低级煤粉化。低级煤浆的制造装置包括：干式破碎低等级煤的破碎装置1; 用于重整干粉碎低等级煤的高温高压捏合装置2; 以及通过重整处理，通过添加水和从低等级煤排出的分散剂来对重整低品位煤进行浆料化的湿式破碎装置5。版权所有（C）2012，JPO＆INPIT

5. 发明专利

JP2010255944A Fuel spray apparatus for gas turbine engine 有权
标题翻译：燃油喷射发动机燃油喷射装置
公开(公告)号：JP2010255944A
公开(公告)日：2010-11-11
申请号：JP2009107440
申请日：2009-04-27
申请人： Kawasaki Heavy Ind Ltd , 川崎重工業株式会社
发明人： OGATA HIDEKI , NONAKA YOSHIHARU , KOBAYASHI MASAYOSHI
IPC分类号： F23R3/28 , F02C7/22 , F23R3/14 , F23R3/34
CPC分类号： F23R3/283 , F23D11/386 , F23D2209/30 , F23D2214/00 , F23D2900/00008 , F23D2900/00018 , F23R3/10 , F23R3/343 , F23R3/50 , Y02T50/675
摘要： PROBLEM TO BE SOLVED: To provide a fuel spray apparatus for a gas turbine engine preventing caulking without increasing the weight of and complicating the apparatus. SOLUTION: The fuel spray apparatus for the gas turbine engine includes: a pilot part 3 for spraying fuel PF to be used for diffusion combustion; a main part 4 provided to surround the pilot part 3 and injecting premixed gas only upon a high load operation; and a shield body 60 constituting a purge air passage PA which takes therein upstream air relative to a fuel injection port 35 of the main part 4 as purge air PA and blows off fuel dripping LF from the fuel injection port 35 toward main air passages 37, 42 of the main part 4. A purge air passage 70 is provided in a position opposite to a main fuel passage 45 communicated with the fuel injection port 35 sandwiching the shield body 60. COPYRIGHT: (C)2011,JPO&INPIT
摘要翻译：要解决的问题：提供一种用于燃气涡轮发动机的燃料喷雾装置，其防止填缝而不增加装置的重量并使其复杂化。解决方案：用于燃气涡轮发动机的燃料喷射装置包括：用于喷射用于扩散燃烧的燃料PF的先导部3; 主要部分4，其设置成围绕引导部3并且仅在高负载操作时喷射预混合气体; 以及构成吹扫空气通路PA的屏蔽体60，其以相对于主体部4的燃料喷射口35为上游的空气作为吹扫空气PA，并且从燃料喷射口35向主空气通路37吹出燃料滴下的LF，吹扫空气通道70设置在与夹着屏蔽体60的燃料喷射口35连通的主燃料通道45相对的位置。（C）2011，JPO＆INPIT

6. 发明专利

JP2013121562A Carbon dioxide-separating equipment 有权
标题翻译：二氧化碳分离设备
公开(公告)号：JP2013121562A
公开(公告)日：2013-06-20
申请号：JP2011270316
申请日：2011-12-09
申请人： Kawasaki Heavy Ind Ltd , 川崎重工業株式会社
发明人： OGINO TOMOYUKI , NONAKA YOSHIHARU , HIROKAWA MASATOSHI , OKUMURA YUJI , SHOJI KIYOTOSHI
IPC分类号： B01D53/04 , B01D53/08 , B01D53/14 , C01B32/50
CPC分类号： B01D53/08 , B01D2252/204 , B01D2253/25 , B01D2257/504 , B01D2257/80 , B01D2258/0283 , B01D2259/4009 , Y02C10/06 , Y02C10/08
摘要： PROBLEM TO BE SOLVED: To provide moving bed CO-separating equipment capable of steady COcollection and to provide CO-separating equipment of high energy efficiency.SOLUTION: The adsorption tower 11, which adsorbs COfrom a gas to be processed, is provided with an adsorbent hopper 10 that supplies a COadsorbent, which is the moving bed. Below the adsorption tower 11, a moving bed regenerating tower 12 for regenerating the COadsorbent after the COadsorption and a moving bed drying tower 13 for drying the COadsorbent after regeneration are provided. Water vapor for desorption generated from the drying tower 13 is supplied to the regenerating tower 12 and COis desorbed from the COadsorbent by condensing the water vapor on the COadsorbent. The COadsorbent that forms the moving bed is thereby re-circulated and used inside the CO-separating equipment 1, and utilization of the energy, which is used for drying the condensed water contained in the COadsorbent, for COdesorption makes the equipment highly energy efficient.
摘要翻译：要解决的问题：提供能够稳定CO 2 集合的移动床CO 2 分离设备，并提供 CO 2 具有高能效的分离设备。解决方案：从待处理气体中吸附CO 2 的吸附塔11设置有供应CO 2 吸附剂，即移动床。在吸附塔11下方，在CO 2 吸附之后再生CO 2 吸附剂的移动床再生塔12和移动提供再生后的用于干燥CO 2 吸附剂的床干燥塔13。从干燥塔13产生的用于解吸的水蒸汽被供应到再生塔12，并且从CO 2 解吸。吸附剂通过在CO 2 吸附剂上冷凝水蒸气。因此，形成移动床的CO 2 吸附剂因此在CO 2分离设备1内再循环使用，用于干燥包含在CO 2 吸附剂中的冷凝水的能量的利用用于CO 2 解吸使得设备高效节能。版权所有（C）2013，JPO＆INPIT

7. 发明专利

JP2012250142A Co2 recovery method and apparatus 有权
标题翻译：二氧化碳回收方法和装置
公开(公告)号：JP2012250142A
公开(公告)日：2012-12-20
申请号：JP2011122535
申请日：2011-05-31
申请人： Kawasaki Heavy Ind Ltd , 川崎重工業株式会社
发明人： OKUMURA YUJI , NONAKA YOSHIHARU , OGINO TOMOYUKI , SHOJI KIYOTOSHI , HIROKAWA MASATOSHI , TAKIGAWA NOBORU , KAMASAWA KAZUTO
IPC分类号： B01D53/62 , B01D53/14 , C01B32/50
CPC分类号： C01B31/20 , B01D53/04 , B01D53/047 , B01D53/62 , B01D2257/504 , B01D2258/0283 , B01D2259/40001 , B01D2259/40054 , B01D2259/40086 , B01D2259/402 , Y02C10/08
摘要： PROBLEM TO BE SOLVED: To provide a CO2 recovery method and apparatus with which desorption and recovery of CO2 from a processed gas discharged out of a power generation plant equipped with a boiler and a steam turbine is carried out with low energy consumption.SOLUTION: Two adsorbent filling tanks 21 and 31, each of which accommodates a CO2 adsorption material installed at a CO2 recovery apparatus 20, perform the adsorption and desorption alternately of CO2 contained in a combustion exhaust gas discharged from a boiler 3. During CO2 desorption, some of the steam discharged through an outlet of a steam turbine 4 of a power generation plant 1 before entering a condenser 6 is separated, sent to a steam compressor 37 to be compressed and heated, then sent to a cooler 29. The steam after compression and heating is cooled to prepare steam for desorption at the cooler 29. The steam prepared at the cooler 29 is supplied to the adsorbent filling tanks 21 or 31 for CO2 desorption. Thereby exhaust steam which has not yet entered the condenser 6 may be used to prepare the steam for desorption.
摘要翻译：要解决的问题：提供一种二氧化碳回收方法和装置，其以低能耗进行从配备有锅炉和蒸汽轮机的发电厂排出的处理气体中的CO 2的解吸和回收。解决方案：两个容纳安装在CO 2回收装置20上的CO 2吸附材料的吸附剂填充槽21和31交替地执行从锅炉3排出的燃烧废气中所含的CO 2的吸附和解吸。二氧化碳脱附时，在进入冷凝器6之前通过发电厂1的蒸汽轮机4的出口排出的一部分蒸汽被分离，送到蒸汽压缩机37进行压缩和加热，然后送至冷却器29。压缩和加热后的蒸汽被冷却以制备用于在冷却器29解吸的蒸汽。在冷却器29处制备的蒸汽被供应到吸附剂填充罐21或31用于CO 2解吸。因此，尚未进入冷凝器6的废气可用于制备用于解吸的蒸汽。版权所有（C）2013，JPO＆INPIT

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