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11.
公开(公告)号:EP1354853A1
公开(公告)日:2003-10-22
申请号:EP02710339.9
申请日:2002-01-24
IPC分类号: C01B3/48 , C01B3/16 , H01M8/06 , B01J23/652 , B01J23/42 , B01J23/656 , B01J29/14 , B01J29/16 , B01J29/12 , B01J29/62 , B01J29/22 , B01J29/44 , B01J29/74 , B01J29/89 , B01J29/072 , B01J29/068
CPC分类号: H01M8/0662 , B01J8/009 , B01J8/0453 , B01J8/048 , B01J8/0496 , B01J19/2485 , B01J23/002 , B01J23/63 , B01J23/64 , B01J23/652 , B01J23/6567 , B01J23/89 , B01J23/8993 , B01J2208/00194 , B01J2208/00495 , C01B3/16 , C01B3/48 , C01B2203/0233 , C01B2203/0283 , C01B2203/0288 , C01B2203/044 , C01B2203/047 , C01B2203/066 , C01B2203/0811 , C01B2203/0822 , C01B2203/0827 , C01B2203/0883 , C01B2203/1023 , C01B2203/1064 , C01B2203/1076 , C01B2203/1082 , C01B2203/1094 , C01B2203/1241 , C01B2203/1288 , C01B2203/1604 , C01B2203/1609 , C01B2203/1619 , C01B2203/1661 , C01B2203/1676 , C10K3/04 , H01M8/0612 , Y02P20/128 , Y02P20/52
摘要: Conventional hydrogen purification apparatuses cannot be used satisfactorily for applications in which much time is required for startup of the apparatus, and the apparatus is repeatedly started and stopped at frequent intervals because of complicated handling.
In a hydrogen purification apparatus comprising at least a catalysis body 1 removing carbon monoxide from a reformed gas containing hydrogen, carbon monoxide and steam, the catalyst body 1 is constituted by a carrier comprised of a complex oxide in which at least one of Mo, W and Re is compounded with Zr, or comprised of an oxide of one of Mo, W, Re and Zr, and at least one of Pt, Pd, Rh and Ru carried on the surface of the carrier.摘要翻译: 传统的氢气净化装置不能令人满意地用于在其中大部分时间是必需的设备的启动应用程序,并且该装置被启动,并在频繁的时间间隔由于复杂的处理的反复停止。 ?>在氢气提纯装置从含有氢气,一氧化碳和水蒸气的重整气体,其包括至少一个催化体1中去除一氧化碳,催化体1由其中的至少一个由一复合氧化物的载体构成 的Mo,W和Re是复合有Zr或包括钼,钨,Re和Zr中的一种的氧化物,以及铂,钯,Rh和Ru中的至少一种所述载体的表面上。
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公开(公告)号:EP1314690A1
公开(公告)日:2003-05-28
申请号:EP01955648.9
申请日:2001-08-10
CPC分类号: B01J19/2485 , B01J8/001 , B01J8/0085 , B01J8/0453 , B01J8/0457 , B01J8/0496 , B01J19/0013 , B01J23/40 , B01J23/63 , B01J2208/00061 , B01J2208/00132 , B01J2208/00168 , B01J2208/00176 , B01J2208/00495 , B01J2208/00504 , B01J2208/0053 , B01J2219/00063 , B01J2219/00081 , B01J2219/00087 , B01J2219/00155 , B01J2219/00157 , B01J2219/00159 , B01J2219/00198 , B01J2219/00202 , C01B3/48 , C01B2203/0233 , C01B2203/0288 , C01B2203/066 , C01B2203/1064 , C01B2203/1076 , C01B2203/1082 , C01B2203/1614 , C01B2203/1619 , C01B2203/1623 , H01M8/0612 , H01M8/0662
摘要: It was difficult to acquire a good CO cleanup efficiency in a hydrogen refining apparatus, for instance, when the start-up and stop operations are frequently repeated.
A hydrogen refining apparatus, including a shifter 3 having a shifting catalyst body 3a containing noble metals and metal oxides, and a reforming section 1 for supplying hydrogen gas containing carbon monoxide to the shifter 3, (1) the temperature of an upstream side of the shifting catalyst body 3a relative to the hydrogen gas flow being substantially between 300°C and 500°C and (2) the temperature of a downstream side of the shifting catalyst body 3a relative to the hydrogen gas flow being substantially at 300°C or less.摘要翻译: 在氢精炼装置中难以获得良好的CO净化效率,例如,当启动和停止操作经常重复时。 一种氢精炼装置,包括具有含有贵金属和金属氧化物的变换催化剂体3a的变速器3和用于向变速器3供给含有一氧化碳的氢气的转化部1,(1)上游侧的温度 转换催化剂体3a相对于氢气流量基本上在300℃至500℃之间,和(2)变换催化剂体3a的下游侧相对于氢气流的温度基本上在300℃以下 。
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公开(公告)号:EP0852175A1
公开(公告)日:1998-07-08
申请号:EP97918386.0
申请日:1997-05-08
发明人: UKAI, Kunihiro , TOMIZAWA, Takeshi , FUJITA, Tatsuo , SUZUKI, Jiro , NAKAZONO, Mitsuyuki , HATTORI, Tomotaka
IPC分类号: B29B17/00
CPC分类号: B30B1/003 , B29B17/0047 , B29B17/0052 , B30B9/3035 , Y02W30/62 , Y10S241/38
摘要: A waste plastic disposal apparatus (K1-K4) comprises a storage section (2) having a cover (2b), a waste plastic heating unit (7) having a heater (7b) and a fan (7a), a hot air circulating path (20) formed by the storage section (2) and the heating unit (7) so as to circulate hot air, an exhaust path (10) branching from the hot air circulating path (20), and a deodorizing unit (9) provided in the exhaust path (10), the exhaust path (10) permitting an amount of hot air equal to a predetermined amount of outside air, which is taken into the hot air circulating path (20) every unit time, to be discharged therefrom through the deodorizing unit (9).
摘要翻译: 一种废塑料处理装置(K1-K4)包括具有盖(2b)的储存部分(2),具有加热器(7b)和风扇(7a)的废塑料加热单元(7),热空气循环路径 (2)和加热单元(7)形成以使热空气循环的热交换器(20),从热空气循环路径(20)分支的排气通路(10)和设置的除臭单元(9) 在排气通路10中,能够使每单位时间吸入热风循环路径20的规定量的外部空气量的排气通路10从排气通路10排出 除臭单元(9)。
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