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1. 发明专利

JP2010276259A Drying device and drying method for water-containing solid fuel 有权
标题翻译：用于含水固体燃料的干燥装置和干燥方法
公开(公告)号：JP2010276259A
公开(公告)日：2010-12-09
申请号：JP2009128513
申请日：2009-05-28
申请人： Mitsubishi Heavy Ind Ltd , Univ Of Tokyo , 三菱重工業株式会社 , 国立大学法人東京大学
发明人： YOKOHAMA KATSUHIKO , KOSAKA KENICHIRO , MATSUMOTO KEIGO , KAWAMOTO NOBORU , YAMAGUCHI HIROKI , KINOSHITA MASAAKI , OURA KOJI , TSUTSUMI ATSUSHI , KANEKO SHOZO , MOCHIZUKI KAZUHIRO , FUSHIMI CHIHIRO , KANSHA YASUKI
IPC分类号： F26B21/04 , C10L5/40 , F26B3/08
CPC分类号： F23K1/04 , C10L9/08 , F23K2201/20 , F26B23/004 , Y02B30/52 , Y02E50/30 , Y02P70/405
摘要： PROBLEM TO BE SOLVED: To provide a drying device for water-containing solid fuel capable of effectively using sensible heat and latent heat of a heating medium for drying etc. and enabling efficient drying while reducing energy consumption. SOLUTION: The drying device 10 for drying the water-containing solid fuel includes: a dryer 20 for inputting scavenging gas to inside of a drying container 21 having a heat transfer pipe 22 arranged therein; a dust collector 13 for removing particulates from mixed gas fluid including the particulates made to flow out from the drying container 21; a compressor 30 for compressing mixed gas fluid including steam; a steam heat exchanger 31 for preheating low-pressure mixed gas fluid by high pressure mixed gas fluid compressed by the compressor 30; and a gas liquid separator 14 using the high-pressure mixed gas fluid as drying gas passing through the heat transfer pipe 22 and releasing heat and performing gas liquid separation of the water-containing scavenging gas including condensation water of steam generated by the heat release and made to flow out from the heat transfer pipe 22. By using the latent heat and sensible heat of the mixed gas fluid, the water-containing solid fuel is heated and dried within the drying container 21. COPYRIGHT: (C)2011,JPO&INPIT
摘要翻译：要解决的问题：提供一种能够有效地利用加热介质的显热和潜热进行干燥等的含水固体燃料的干燥装置，并且能够在降低能量消耗的同时进行有效的干燥。用于干燥含水固体燃料的干燥装置10包括：干燥器20，用于将清除气体输入到具有布置在其中的传热管22的干燥容器21的内部; 用于从包括从干燥容器21流出的微粒的混合气体流体中除去微粒的集尘器13; 用于压缩包括蒸汽的混合气体流体的压缩机30; 用于通过由压缩机30压缩的高压混合气体流体预热低压混合气体流体的蒸汽热交换器31; 以及气液分离器14，其使用高压混合气体流体作为干燥气体，通过传热管22，并释放热量，并对包含由热释放产生的蒸汽的冷凝水和含水清除气体进行气液分离，使其从传热管22流出。通过使用混合气体流体的潜热和显热，将含水固体燃料在干燥容器21内加热干燥。版权所有（C）2011 ，JPO＆INPIT

2. 发明专利

JP2013078294A Apparatus and method for producing ethanol 审中-公开
标题翻译：装置和方法生产乙醇
公开(公告)号：JP2013078294A
公开(公告)日：2013-05-02
申请号：JP2011221133
申请日：2011-10-05
申请人： Nippon Steel & Sumikin Engineering Co Ltd , 新日鉄住金エンジニアリング株式会社 , Ns Plant Designing Corp , Nsプラント設計株式会社 , Univ Of Tokyo , 国立大学法人東京大学
发明人： KIUCHI TAKAFUMI , HIDAKA RYOTA , ISHIBASHI YOICHI , MITARAI SHIGERU , HARADA KOJI , KANSHA YASUKI , TSUTSUMI ATSUSHI
IPC分类号： C12M1/00 , B01D3/00 , B01D3/14 , B09B3/00 , C12M1/02 , C12P7/06
CPC分类号： Y02E50/17
摘要： PROBLEM TO BE SOLVED: To provide an apparatus and method for producing ethanol in which energy required to circulate and use an enzyme is reduced compared to before.SOLUTION: In the ethanol production apparatus including a distillation tower 11 into which an ethanol-fermented liquid produced by fermentation of a biomass raw material is introduced and in which the ethanol-fermented liquid is distilled to distill ethanol vapor, and a rectification tower 12 for rectifying the ethanol vapor to produce ethanol from the biomass raw material, the ethanol vapor distilled from the distillation tower 11 is directly introduced into the rectification tower 12.
摘要翻译：待解决的问题：提供一种生产乙醇的装置和方法，其中循环和使用酶所需的能量比以前减少。解决方案：在包括通过引入生物质原料发酵生产的乙醇发酵液体并蒸馏乙醇发酵液体以蒸馏乙醇蒸气的蒸馏塔11的乙醇制备装置中，以及精馏塔12用于将乙醇蒸汽精馏从生物质原料中生产乙醇，从蒸馏塔11蒸馏的乙醇蒸汽直接引入精馏塔12.版权所有（C）2013，JPO＆INPIT

3. 发明专利

JP2010036057A Separation process module, integration separation process module, large scale integration separation process module 有权
标题翻译：分离过程模块，集成分离过程模块，大规模集成分离过程模块
公开(公告)号：JP2010036057A
公开(公告)日：2010-02-18
申请号：JP2008198357
申请日：2008-07-31
申请人： Chiyoda Kako Kensetsu Kk , Nippon Oil Corp , Univ Of Tokyo , 千代田化工建設株式会社 , 国立大学法人東京大学 , 新日本石油株式会社
发明人： MATSUDA KAZUO , HIROCHI YOSHIICHI , KAERUISHI KENICHI , SATO REI , MIMURA KENICHI , SHIMOKAWARA KAORU , SHIKATANI YUTAKA , KUNIKIYO KOJI , TAKESHITA TAKAAKI , TSUTSUMI ATSUSHI , FUSHIMI CHIHIRO , TSURU NAOKI , KANSHA YASUKI
IPC分类号： B01D3/00
摘要： PROBLEM TO BE SOLVED: To provide a separation process module with high energy-saving effect, an integration separation process module, and a large scale integration separation process module.
SOLUTION: In the separation process module 100, first and second branched lines R1, R2 run input fluid branchingdly, the fluid joins at a merging path W to flow joinedly. A separator S separates the input fluid flowing in the merging path W into the first output fluid and second input fluid. A first compressor C1 raises the temperature of the first output fluid output from the separator S by compressing it. A first heat exchanger H1 heat-exchanges between the first compressed output fluid and the input fluid flowing in the merging path W. A second heat exchanger H2 heat-exchanges between the first output fluid having passed through the first heat exchanger H1 and the input fluid flowing in the first branched line R1. A third heat exchanger H3 heat-exchanges between the second output fluid output from the separator S and the input fluid flowing in the second branched line R2.
COPYRIGHT: (C)2010,JPO&INPIT
摘要翻译：要解决的问题：提供具有高节能效果的分离工艺模块，集成分离工艺模块和大规模集成分离工艺模块。解决方案：在分离处理模块100中，第一和第二分支管线R1，R2以分支方式运行输入流体，流体在合流路径W处连接流动。分离器S将在合流路径W中流动的输入流体分离成第一输出流体和第二输入流体。第一压缩机C1通过压缩来提高从分离器S输出的第一输出流体的温度。第一热交换器H1在第一压缩输出流体和在合流路径W中流动的输入流体之间进行热交换。第二热交换器H2通过第一热交换器H1的第一输出流体与输入流体在第一分支线路R1中流动。第三热交换器H3在从分离器S输出的第二输出流体与在第二分支线R2中流动的输入流体之间热交换。版权所有（C）2010，JPO＆INPIT

4. 发明专利

JP2009095802A Reaction apparatus 有权
标题翻译：反应装置
公开(公告)号：JP2009095802A
公开(公告)日：2009-05-07
申请号：JP2007271547
申请日：2007-10-18
申请人： Chiyoda Corp , National Institute Of Advanced Industrial & Technology , Nippon Oil Corp , Univ Of Tokyo , 千代田化工建設株式会社 , 国立大学法人東京大学 , 新日本石油株式会社 , 独立行政法人産業技術総合研究所
发明人： MATSUDA KAZUO , HIROCHI YOSHIICHI , KAERUISHI KENICHI , SATO REI , MIMURA KENICHI , SHIMOKAWARA KAORU , IRIKURA MOTOKI , SHIKATANI YUTAKA , KUNIKIYO KOJI , TAKESHITA TAKAAKI , MIYAZAWA AKIRA , YAMAMOTO EIZO , TANAKA SAKIO , MOGI AKIRA , NAKAIWA MASARU , TSUTSUMI ATSUSHI , FUSHIMI CHIHIRO
IPC分类号： B01J19/00 , C10G45/02
摘要： PROBLEM TO BE SOLVED: To provide a reaction apparatus which saves energy and reduces exergy loss.
SOLUTION: The reaction apparatus 10 has a reactor 12 which is supplied a mixture fluid 30 in which a naphtha 22 as a raw material and H
2 24 for reacting with the naphtha 22 are mixed, and makes the naphtha 22 and H
2 24 react to produce a reacted fluid 40, a heat exchanger 14 for heat exchanging between the reacted fluid 40 from the reactor 12 and the mixed fluid 30, and a compressor which is arranged between the reactor 12 and the heat exchanger 14 and compresses the mixed fluid 30.
COPYRIGHT: (C)2009,JPO&INPIT
摘要翻译：要解决的问题：提供一种节省能量并降低能量损耗的反应装置。解决方案：反应装置10具有反应器12，该反应器12混合作为原料的石脑油22和与石脑油22反应的H SB 2的混合流体30混合，使石脑油22和H 2 SB 2反应以产生反应流体40，用于在来自反应器12的反应流体40与混合流体30之间进行热交换的热交换器14和压缩机布置在反应器12和热交换器14之间并压缩混合流体30.版权所有：（C）2009，JPO＆INPIT

5. 发明专利

JP2014108909A Carbon dioxide recovery apparatus 有权
标题翻译：二氧化碳回收装置
公开(公告)号：JP2014108909A
公开(公告)日：2014-06-12
申请号：JP2012264018
申请日：2012-12-03
申请人： Ihi Corp , 株式会社Ihi , Univ Of Tokyo , 国立大学法人東京大学
发明人： NISHIYAMA YUICHI , MURAMOTO TOMOYA , NAKAMURA NORITAKA , OKUNO MASAYA , MATSUZAWA KATSUAKI , TSUTSUMI ATSUSHI
IPC分类号： B01D53/14 , B01D53/62 , C01B32/50
CPC分类号： Y02A50/2342 , Y02C10/06 , Y02P20/152 , Y02P20/57
摘要： PROBLEM TO BE SOLVED: To recover efficiently heat energy necessary for regeneration of an absorbent.SOLUTION: A carbon dioxide recovery apparatus 100 comprises an absorption portion 120, a heating portion 134 heating a rich absorbent R and preparing a gas-liquid mixed fluid comprising the absorbent, carbon dioxide and water vapor, a first gas-liquid separation portion 140 separating the gas-liquid mixed fluid into the absorbent and a recovery gas X, a passage line 210 through which the recovery gas X passes, a compression portion 220 compressing the recovery gas X, a first heat exchange portion 320 recovering heat generated in compression of the recovery gas X and heating the rich absorbent R before heating by the heating portion 134, a second gas-liquid separation portion 230 separating, from the recovery gas X, water condensed owing to heat recovery by the first heat exchange portion 320 and a second heat exchange portion 310 recovering heat of the recovery gas X separated by the second gas-liquid separation portion 320 and heating the rich absorbent R before heating by the first heat exchange portion 320.
摘要翻译：要解决的问题：有效地回收吸收剂再生所需的热能。解决方案：二氧化碳回收装置100包括吸收部分120，加热富含吸收剂R的加热部分134和制备气液混合流体，吸收剂，二氧化碳和水蒸气，将气液混合流体分离成吸收剂的第一气液分离部分140和回收气体X，回收气体X通过的通道210，压缩部分220 回收气体X，第一热交换部320，其回收在回收气体X的压缩中产生的热量，并且在加热部134加热之前加热富吸收剂R.第二气液分离部230，与回收气体X分离，由于第一热交换部分320的热回收而冷凝的水和第二热交换部分310回收由秒分开的回收气体X的热量在第一热交换部分320加热之前加热富吸收剂R。

6. 发明专利

JP2010015783A Fuel cell storage battery, and battery module using the same 有权
标题翻译：燃料电池储存电池和使用该电池的电池模块
公开(公告)号：JP2010015783A
公开(公告)日：2010-01-21
申请号：JP2008173760
申请日：2008-07-02
申请人： Kawasaki Heavy Ind Ltd , Univ Of Tokyo , 国立大学法人東京大学 , 川崎重工業株式会社
发明人： TSUTSUMI KAZUO , TSUTSUMI ATSUSHI , LEE SUNMOOK , CHOI BOKKYU
IPC分类号： H01M10/28 , H01M2/10 , H01M4/24 , H01M4/32 , H01M10/30 , H01M10/42 , H01M10/60 , H01M10/613 , H01M10/617 , H01M10/643 , H01M10/647 , H01M10/653 , H01M10/6557 , H01M10/6563 , H01M10/6568 , H01M10/658 , H01M10/659
CPC分类号： Y02E60/124
摘要： PROBLEM TO BE SOLVED: To provide a fuel cell storage battery and a battery module, which can use electric energy supplied at the time of excessive charge by saving as a gas and by reconverting into the electric energy and is excellent in energy utilization efficiency, energy density, and a load following property. SOLUTION: In the fuel cell storage battery having a negative electrode including a hydrogen absorption alloy and a positive electrode, a separator intervened between the negative electrode and the positive electrode and passing a proton and not passing a hydrogen gas and an oxygen gas is used, and a hydrogen storage chamber and an oxygen storage chamber which directly and independently save the hydrogen gas generated in the negative electrode and the oxygen gas generated in the positive electrode respectively are arranged. COPYRIGHT: (C)2010,JPO&INPIT
摘要翻译：要解决的问题：提供一种燃料电池蓄电池和电池模块，其可以使用通过节省作为气体并且再转换成电能并且能量利用率优异的过充电时供给的电能效率，能量密度和负载跟随特性。解决方案：在具有包含氢吸收合金和正极的负极的燃料电池用蓄电池中，隔着负极和正极之间通过质子，不通过氢气和氧气的隔膜并且分别直接且独立地保存在负极中产生的氢气和在正极中产生的氧气的储氢室和储氧室。版权所有（C）2010，JPO＆INPIT

7. 发明专利

JP2014108389A Carbon dioxide recovery apparatus 有权
标题翻译：二氧化碳回收装置
公开(公告)号：JP2014108389A
公开(公告)日：2014-06-12
申请号：JP2012264017
申请日：2012-12-03
申请人： Ihi Corp , 株式会社Ihi , Univ Of Tokyo , 国立大学法人東京大学
发明人： MURAMOTO TOMOYA , NISHIYAMA YUICHI , OKUNO MASAYA , MATSUZAWA KATSUAKI , TSUTSUMI ATSUSHI
IPC分类号： B01D53/14 , B01D53/62 , C01B32/50
CPC分类号： B01D53/62 , B01D53/1418 , B01D53/1475 , B01D2252/20478 , Y02C10/04 , Y02C10/06
摘要： PROBLEM TO BE SOLVED: To efficiently recover thermal energy required for regenerating an absorbing solution while reducing cost required for a compressor by maintaining a low temperature of the compressor.SOLUTION: A carbon dioxide recovery apparatus 100 includes: an absorption part 120; a regeneration part 140; a passing line 210 through which recovery gas X including carbon dioxide and stream discharged from the regeneration part 140 passes; a plurality of stages of compression parts 220, 222, 224 installed in the passing line and compressing the recovery gas X; a temperature measurement part 280 for measuring an outlet temperature of each of the compression parts; a rotational frequency control part 282 for controlling rotational frequency of each of the compression parts so that the temperature measured by the temperature measurement part reaches 200°C or lower; and a heat exchange part (second heat exchange part 320) for recovering heat generated along with compression of the recovery gas X by the compression parts downstream of the compression parts and supplying the heat to the regeneration part.
摘要翻译：要解决的问题：为了有效地回收再生吸收溶液所需的热能，同时通过保持压缩机的低温来降低压缩机所需的成本。解决方案：二氧化碳回收装置100包括：吸收部分120; 再生部140; 通过管线210，从再生部140排出的包含二氧化碳和流的回收气体X通过该通过管线210通过; 压缩部220,222,224的多级，压缩回收气体X; 用于测量每个压缩部件的出口温度的温度测量部件280; 旋转频率控制部282，用于控制各压缩部的旋转频率，使得由温度测量部测量的温度达到200℃以下; 以及热交换部（第二热交换部320），用于回收通过压缩部下游的压缩部压缩回收气体X而产生的热量，并向再生部供给热量。

8. 发明专利

JP2013007512A Air separation method and air separator 有权
标题翻译：空气分离方法和空气分离器
公开(公告)号：JP2013007512A
公开(公告)日：2013-01-10
申请号：JP2011139532
申请日：2011-06-23
申请人： Air Water Inc , エア・ウォーター株式会社 , Shinko Air Water Cryoplant Ltd , 神鋼エア・ウォーター・クライオプラント株式会社 , Univ Of Tokyo , 国立大学法人東京大学
发明人： TSUTSUMI ATSUSHI , KANSHA YASUKI , KISHIMOTO HIROSHI , ASAOKA HITOSHI , TANIGUCHI KENAKI , SUENAGA JUNYA
IPC分类号： F25J3/04
CPC分类号： F25J3/0406 , F25J3/0409 , F25J3/04309 , F25J3/04351 , F25J3/04393 , F25J3/044 , F25J2200/40 , F25J2200/50 , F25J2200/76
摘要： PROBLEM TO BE SOLVED: To provide an air separation method which is available in safety because an oxygen gas having difficulty in handling is not compressed, there is neither initial cost for introduction nor dissipation energy are small, and is excellent in economical efficiency, and to provide an air separator.SOLUTION: Cold needed in a nitrogen gas liquefaction process for manufacturing a reflux liquid used in a rectifying column 1 for rectifying an air component by cryogenic separation and cold needed in a reflux liquid supply process are obtained from a product nitrogen gas guiding process in which a high purity nitrogen gas taken out of the top part 1a of the rectifying column 1 is adiabatically expanded by a product nitrogen expansion turbine 4. Part of the nitrogen gas taken out of the top part 1a of the rectifying column 1 is caused to pass through a nitrogen cooler 6, a reboiler 8, and a supercooler 7 in order and then liquefied to be introduced into the top part of the rectifying column 1. As a result, the reflux liquid can be efficiently cooled without using the oxygen in the rectifying column 1 for cold.
摘要翻译：要解决的问题：提供一种由于难以处理的氧气不被压缩而安全可用的空气分离方法，既不具有初始的引入成本，也不具有耗散能量小，经济性优异，并提供空气分离器。解决方案：在氮气液化过程中需要冷却，用于制造用于精馏塔1中的回流液体，用于通过低温分离进行的空气组分的精馏和回流液体供应过程中所需的冷却从产品氮气引导过程其中从精馏塔1的顶部1a取出的高纯度氮气被产品氮气膨胀涡轮4绝热膨胀。将从精馏塔1的顶部1a取出的氮气的一部分通过氮气冷却器6，再沸器8和过冷却器7，然后液化并引入精馏塔1的顶部。结果，可以有效地冷却回流液体而不使用在整流柱1为冷。版权所有（C）2013，JPO＆INPIT

9. 发明专利

JP2010036059A Separation process module 有权
标题翻译：分离过程模块
公开(公告)号：JP2010036059A
公开(公告)日：2010-02-18
申请号：JP2008198442
申请日：2008-07-31
申请人： Chiyoda Kako Kensetsu Kk , Nippon Oil Corp , Univ Of Tokyo , 千代田化工建設株式会社 , 国立大学法人東京大学 , 新日本石油株式会社
发明人： MATSUDA KAZUO , HIROCHI YOSHIICHI , KAERUISHI KENICHI , SATO REI , MIMURA KENICHI , SHIMOKAWARA KAORU , SHIKATANI YUTAKA , KUNIKIYO KOJI , TAKESHITA TAKAAKI , TSUTSUMI ATSUSHI , FUSHIMI CHIHIRO , TSURU NAOKI , KANSHA YASUKI
IPC分类号： B01D3/00
摘要： PROBLEM TO BE SOLVED: To provide a separation process module having high energy saving effect.
SOLUTION: The separation process module 100 is provided with a separator S separating input fluid into a first output fluid and a second output fluid; a first branched part J1 branching the first output fluid output from the separator S; a compressor C to raise the temperature of the first output fluid output from the first branched part J1 by compressing it; a second branched part j2 branching the second output fluid output from the separator S; and a heat exchanger H heat-exchanging between the second output fluid output from the second branched part j2 and the first fluid compressed by the compressor C. The first output fluid having passed through the heat exchanger H and second output fluid having passed through the heat exchanger H are input into the separator S.
COPYRIGHT: (C)2010,JPO&INPIT
摘要翻译：要解决的问题：提供具有高节能效果的分离处理模块。解决方案：分离处理模块100设置有将输入流体分离成第一输出流体和第二输出流体的分离器S; 分离从分离器S输出的第一输出流体的第一分支部分J1; 压缩机C，其通过压缩从第一分支部分J1输出的第一输出流体的温度升高; 分支从分离器S输出的第二输出流体的第二分支部分j2; 以及在从第二分支部分j2输出的第二输出流体与由压缩机C压缩的第一流体之间进行热交换的热交换器H.经过热交换器H的第一输出流体和已经通过热量的第二输出流体交换器H输入到分离器S.版权所有（C）2010，JPO＆INPIT

10. 发明专利

JP2013093146A Fuel cell positive electrode and fuel cell including the same 有权
标题翻译：燃料电池正极和燃料电池，包括它们
公开(公告)号：JP2013093146A
公开(公告)日：2013-05-16
申请号：JP2011233497
申请日：2011-10-25
申请人： Univ Of Tokyo , 国立大学法人東京大学
发明人： TSUTSUMI ATSUSHI , CHOI BOKKYU
IPC分类号： H01M4/90 , H01M8/04 , H01M8/10 , H01M12/08
CPC分类号： Y02E60/128
摘要： PROBLEM TO BE SOLVED: To solve such problems that a fuel cell has high energy density but low output density, while a secondary battery has high output density but low energy density and also limited electric capacity, one of the reason for the problems being increased thickness of an electrode.SOLUTION: A fuel cell includes: a positive electrode obtained by electrolytic deposition of manganese dioxide on carbon fibers; and a negative electrode including a hydrogen absorbing alloy. The fuel cell is provided with a hydrogen storage chamber and an oxygen storage chamber which directly and independently storage hydrogen gas produced at the negative electrode and oxygen gas produced at the positive electrode, respectively, and thereby there are provided a positive electrode for a fuel cell which is excellent in energy utilization efficiency, energy density and load followability while using a relatively small electrode, and a fuel cell including the positive electrode.
摘要翻译：要解决的问题为了解决燃料电池具有高能量密度但输出密度低的问题，二次电池具有高输出密度但能量密度低并且电容量有限的问题之一是问题之一增加电极的厚度。解决方案：燃料电池包括：通过在碳纤维上电解沉积二氧化锰获得的正极; 以及包含吸氢合金的负极。燃料电池设置有分别直接且独立地存储在负极处产生的氢气和在正极产生的氧气的储氢室和储氧室，由此设置用于燃料电池的正极在使用相对小的电极的同时能量利用效率，能量密度和负载追随性优异，以及包括正极的燃料电池。版权所有（C）2013，JPO＆INPIT

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