CN101069000A - 改进的触媒滤烟器 - Google Patents

改进的触媒滤烟器 Download PDF

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CN101069000A
CN101069000A CNA2005800251831A CN200580025183A CN101069000A CN 101069000 A CN101069000 A CN 101069000A CN A2005800251831 A CNA2005800251831 A CN A2005800251831A CN 200580025183 A CN200580025183 A CN 200580025183A CN 101069000 A CN101069000 A CN 101069000A
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alkali
soot filter
catalyzed soot
combination
porous ceramics
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R·齐巴思
R·T·尼尔松
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Dow Global Technologies LLC
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Abstract

本发明涉及一种改进的触媒滤烟器,其包括在多孔陶瓷的至少一部分上具有无定形催化相的多孔陶瓷,所述无定形催化相包括含有其中具有Si、Al或其结合的氧化物玻璃的碱。通过使例如莫来石、碳化硅或堇青石的多孔陶瓷与含有硅酸盐、铝酸盐或铝硅酸盐的化合物的碱接触,然后加热至足以形成使多孔陶瓷的至少一部分的无定形催化相融合的温度,以形成所述改进的触媒滤烟器。

Description

改进的触媒滤烟器
技术领域
本发明涉及一种改进的触媒微粒滤器。
背景技术
柴油机,由于其操作的方式,会释放出煤烟颗粒或非常细微的冷凝物液滴或这两种的凝聚物(微粒)以及通常有害的汽油机排放物(即HC和CO)。这些“微粒”(此处的柴油机煤烟)富含其中一些可以致癌的稠合多核烃。
由于有害的柴油机煤烟对健康所带来的危害与柴油机所提供的更高燃料效率的需求的矛盾,已经制定出相应规定来约束柴油机煤烟允许排放的数量。为了达到这些要求,已经使用滤烟器。当使用这样的滤器时,必须通过燃尽煤烟来定期再生该滤器。但是因为柴油机煤烟燃烧的温度明显高于柴油机正常操作的温度,已提议使用一些催化剂来降低柴油机煤烟的燃烧温度。
通常,使用含有碱或碱性氧化物的催化剂来显著降低柴油机煤烟的燃烧温度,其描述于,例如,JP 2001-17449;WO 03/011437;US2002/0132727和US 2002/0197191。不幸地是,这些催化剂是挥发性的并且对滤器具有破坏性,以致于具有不实际的短寿命。此外,这些催化剂还需要相当数量的贵金属催化剂以减少与柴油机煤烟一起释放的HC和CO气体。
其它氧化剂,如稀土氧化物(如US 4,515,758;US 2002/0197191;US2002/0044897;US 2003/0124037;WO 01/02083)和贱金属氧化物也可以用于与贵金属催化剂结合以试图降低柴油机煤烟燃烧温度同时促进HC和CO的释放。不幸的是,这些催化剂也需要相当数量的昂贵的贵金属催化剂和/或稀土氧化物。
因此,理想地提供一种用于柴油机颗粒滤器的催化剂,其会避免已知技术的一个或多个问题,例如上述问题中的一个。特别地,理想地提供一种消除已知技术中所需要的昂贵的稀土氧化物和贵金属催化剂的数量的催化剂来氧化煤烟,同时达到长寿命。
发明内容
本发明的第一方面是一种触媒滤烟器,其包括在多孔陶瓷的至少一部分上具有无定形催化相的多孔陶瓷,所述无定形催化相包括含有其中具有Si、Al或其结合的氧化物玻璃的碱。令人吃惊地,触媒滤烟器显示出良好的煤烟燃烧和长寿命,而没有快速的碱挥发或对多孔陶瓷的化学侵蚀,其与碱氧化物催化剂是相同的。同样地,平衡点温度(即由柴油机颗粒滤器达到的煤烟燃烧率等于滤器中煤烟累积率时的温度)可以与通常的碱氧化物基煤烟催化剂、贵金属催化剂、稀土催化剂及其混合物的温度一样低或更低。
本发明的第二方面是一种形成触媒滤烟器的方法,包括将多孔陶瓷体暴露于含有硅酸盐、铝酸盐、铝硅酸盐或它们的结合的化合物的碱,以使得多孔陶瓷的至少一部分与含有化合物的碱接触,并且将接触的多孔陶瓷加热到足以使包含Si、Al或其结合的氧化物玻璃的碱熔于其中的温度。令人吃惊地,该方法允许将碱加入到玻璃相中,然而例如仅与碱氧化物的接触不能使含有玻璃相的熔融碱加入到多孔陶瓷中。更令人吃惊地,该方法可以改进多孔陶瓷的机械性能,然而仅与碱氧化物的的接触几乎都会对多孔陶瓷具有破坏性。
可以将触媒滤烟器用于其中需要从气流如汽车、火车、卡车或固定发电厂的排放物中去除煤烟的任何应用。触媒滤烟器特别用于从柴油机排放物中去除煤烟。
具体实施方式
本发明是触媒滤烟器,其中煤烟是碳基物质,如上述的柴油机煤烟。该触媒滤烟器包括多孔陶瓷。
该多孔陶瓷体是任何适合的陶瓷,如过滤柴油机煤烟的技术中已知的那些。优选地,多孔陶瓷是在多孔陶瓷的陶瓷的至少一部分表面上具有氧化物晶界相或氧化物相的一种,其中所述相包括Si、Al或它们的结合(如几乎不含此处所述的任何碱的二氧化硅、氧化铝、硅酸盐、铝酸盐或铝硅酸盐)。优选地,陶瓷的整个表面上具有上述相。基本上不含碱表示,例如,多孔陶瓷如莫来石、堇青石或碳化硅具有至多约0.05份每100重量份的没有无定形催化相的多孔陶瓷。
示例性陶瓷包括氧化铝、氧化锆、碳化硅、氮化硅和氮化铝、氧氮化硅和碳氮化硅、莫来石、堇青石、β锂辉石、钛酸铝、硅酸锶铝、硅酸锂铝。优选的多孔陶瓷体包括碳化硅、堇青石和莫来石或它们的结合。碳化硅优选为美国专利No.US 6,669,751B1和WO公开EP1142619A1、WO 2002/070106A1中所述的一个。其它适合的多孔陶瓷描述于WO 2004/011386A1、WO 2004/011124A1、US 2004/0020359A1和WO 2003/051488A1。
莫来石优选是具有针状微结构的莫来石。这种针状陶瓷多孔体的例子包括描述于美国专利Nos.5,194,154;5,173,349;5,198,007;5,098,455;5,340,516;6,596,665和6,306,335;美国专利申请公开2001/0038810;和国际PCT公开WO 03/082773的那些。
通常,多孔陶瓷体具有约30%~85%的孔隙率。优选地,多孔陶瓷体具有至少约40%,更优选至少约45%,,甚至更优选至少约50%,最优选至少约55%至优选最多约80%,更优选最多约75%,最优选最多约70%的孔隙率。
多孔陶瓷体具有在其至少一部分上的催化无定形相。部分表示在多孔陶瓷体上的任何有效量的催化相,使得煤烟平衡温度与类似结合物的单独多孔陶瓷体相比更低。通常,由催化相覆盖多孔陶瓷的至少约10%。优选地,由催化相覆盖至多孔陶瓷体的至少约20%,更优选至少约30%,甚至更优选至少约50%且最优选至少约75%。在一个优选实施方案中,由催化相覆盖多孔陶瓷的整个表面。
在一个优选实施方案中,将至少一部分催化相熔于多孔陶瓷体。所述熔于表示使催化相与多孔陶瓷通过共价键或极性键连接。例如,催化相可以在多孔陶瓷体的陶瓷晶粒上作为晶界无定形相而存在,还可以存在于陶瓷晶界连接处。在这个优选体中,通常使所有催化相熔于多孔陶瓷体的陶瓷晶粒。
该催化相是无定形的。无定形表示没有使用一般分析技术检测到的分子结构。也就是说,可以有一些非常小的有序结构,但由于这些有序结构的尺寸,测定这些有序结构的技术不能检测到或本质上并非与无定形物质不同。例如,有序区域可以是X射线衍射或电子衍射产生的漫散射的小尺寸,如果存在这样的区域,那它的尺寸最多约50到100纳米。
即使催化相是无定形的,当碱量相对于所用胶体的硅酸盐、铝酸盐或其结合的量有所增加时,一小部分碱可以作为碳酸盐或碳酸氢盐而沉淀。例如,X射线衍射图可以显示出在X射线技术的噪声之上可辨别出的小峰。例如,在用于针状莫来石多孔陶瓷体的胶体中的Cs2O与SiO2为1∶1的摩尔比下,这样的碳酸盐/碳酸氢盐峰可以观察到并且这些催化剂是本发明的实施方案。在更低比率下,这样的碳酸盐/碳酸氢盐峰变得越来越不易分辨。例如在大约1∶4的比率下,这样的峰从背景噪声中难以分辨,甚至完全不能分辨。
催化相包括含有氧化物玻璃的碱,该氧化物玻璃具有Si、Al或其结合。该玻璃可以含有任何碱或碱原子的结合。优选该碱是Na、K、Rb、Cs或它们的结合。更优选该碱是Na、K、Cs或它们的结合。甚至更优选该碱是K、Cs或它们的结合。最优选该碱是K或Cs。
玻璃中的碱量可以是任何足以促进煤烟燃烧的量。通常玻璃中的碱量为约0.01~50摩尔%。优选玻璃中的碱量为至少约0.5%,更优选至少约1%,最优选至少约2%至优选最多约25%,更优选最多约20%,最优选优选最多约15摩尔%。通常对应于催化多孔陶瓷中存在的碱量的至少约0.05~约10重量%。优选地,碱量为至少约0.1%,更优选至少约0.2%,最优选至少约0.3%至优选最多约7%,更优选最多约5%,最优选最多约3重量%。
除了碱,氧化物玻璃还含有Si、Al或其结合。这表示在玻璃中,存在硅酸盐(Si-O四面体结构)、铝酸盐(Al-O八面体结构)或其结合。Si、Al或其结合的量可以在较大范围内变化,只要其足以抑制在一般操作温度(约500℃)下的碱的挥发。通常,根据存在于玻璃中的玻璃和碱以及可以存在于玻璃中的其它组分,Si、Al或其结合的量可以在较宽范围内变化。例如Si、Al或其结合可以在99.95~50摩尔%的范围内。在一个优选实施方案中,氧化物玻璃是硅酸盐。在一个特别优选的实施方案中,该硅酸盐是硅酸钾。
除了无定形催化相以外,该多孔陶瓷还可以具有其它用于例如柴油机排放物的催化剂。例如,NOx催化剂或储存化合物、HC催化剂、CO催化剂等可以存在于该多孔陶瓷中。这种任选催化剂的例子如下。
第一示例性任选催化剂是直接连接的金属催化剂,例如贵金属、贱金属及其结合。贵金属催化剂的例子包括铂、铑、钯、钌、铼、银及其合金。贱金属催化剂的例子包括铜、铬、铁、钴、镍、锌、锰、钒、钛、钪及其结合。优选地,金属催化剂是以金属的形式,但可以以无机化合物如氧化物、氮化物和碳化物存在,或在多孔陶瓷的陶瓷晶粒中以缺陷结构存在。可以通过任何合适的技术,如本领域公知的技术使用金属。例如,通过化学气相沉积技术使用金属催化剂。
第二示例性任选催化剂是加入到多孔陶瓷的陶瓷晶粒的晶格结构的催化剂。例如,元素可以是Ce、Zr、La、Mg、Ca、上段所述的金属元素或它们的结合。可以以任何适合的方式,如本领域公知的方式加入这些元素。
第三示例性任选催化剂是具有沉积于其上的金属的陶瓷粒子的结合物。这些通常称之为封固底漆(wash coat)。通常,封固底漆是由微米大小的陶瓷粒子组成的,如具有沉积于其上的金属的沸石、硅铝酸盐、二氧化硅、二氧化铈、氧化锆、氧化钡、碳酸钡和氧化铝粒子。金属可以是任何上述用于直接沉积的金属。特别优选的封固底漆催化剂涂料是包括氧化铝粒子的那些,在该氧化铝粒子上具有贵金属。已知封固底漆可以包括一种以上的金属氧化物,如具有锆、钡、镧、镁和铈中至少一种的氧化物的氧化铝。
第四示例性任选催化剂是钙钛矿型催化剂,其包括金属氧化物组合物,例如Golden在美国专利No.5,939,354中所述的那些。
无定形催化相组分碱、Si、Al或其结合可以以任何适合的方法,如本领域公知的方法,沉积在多孔陶瓷上。例如一种或多种催化剂组分可以通过以下方法沉积,如美国专利Nos.4,515,758;4,740,360;5,013,705;5,063,192;5,130,109;5,254,519;5,993,762和;美国专利申请公开2002/0044897;2002/0197191和2003/0124037;国际专利申请WO 97/00119;WO 99/12642;WO 00/62923;WO 01/02083和WO03/011437;和英国专利No.1,119,180中所述的方法。
在一个具体实施方案中,可以通过沉淀化合物,例如溶于含有碱的硅酸盐、铝酸盐或铝硅酸盐的液体(通常为水)的碱的硅酸盐、铝酸盐或其结合来沉积催化剂的碱成分。
优选地,通过将多孔陶瓷体暴露于含有硅酸盐、铝酸盐或铝硅酸盐或其结合的化合物以制备催化相。通常,碱的硅酸盐、铝酸盐或铝硅酸盐是分散在液体中的胶体。此处的胶体表示每个具有小于1微米的平均粒子大小的颗粒。胶体可以是晶体或无定形的。优选地,胶体是无定形的。胶体优选为Na、Cs、K或其结合的硅酸盐。优选地,胶体是Cs、K或其结合的硅酸盐。最优选地,胶体是K或Cs的硅酸盐。示例性碱的硅酸盐、铝酸盐或铝硅酸盐包括粘土、合成胶体,如本领域已知并且以如下商标可得的那些:KASIL和N,PQ Corporation,POBox 840,Valley Forge,PA.;ZACSIL,Zaclon Incorporated,2981Independence Rd.,Cleveland,OH;硅酸钠,Occidental ChemicalCorporation,Occidental Tower,5005 LBJ Freeway,Dallas,TX。
胶体优选具有小粒子尺寸,其中所有粒子的直径小于1微米。优选地,平均粒子直径为直径小于约500纳米(nm),更优选小于约250nm,甚至更优选小于约100nm,最优选小于约50nm至优选至少约1nm,更优选至少约5nm,最优选至少约10nm。
多孔体可以以任何适合的方法,如本领域公知的方法,暴露于上述的碱的硅酸盐、铝酸盐或铝硅酸盐。例如通过喷雾、浸渍、沉浸将胶体的液体分散浸渗到多孔体中,然后干燥。
在多孔陶瓷与例如胶体接触以后,加热多孔体,例如,以形成无定形催化相并且如需要,使催化相熔于多孔陶瓷体。通常,加热温度为至少约400℃~约1600℃。典型地,温度为至少约500℃~约1000℃。通常,大气需要含有足够量的氧气以确保玻璃是硅酸盐、铝酸盐或铝硅酸盐(即含有氧的一个)。通常,空气适于加热催化剂组合以形成无定形催化相。如需要或必要,可以进行所述的另一种在降低或惰性气氛中的加热至相似温度以形成其它任选的催化剂,如贵金属。
令人吃惊地,与仅由碱氧化物催化的相同滤器相比,触媒滤器具有改进的煤烟燃烧,其中平衡点温度通常至少一样低,并且寿命得以显著改进。此外,煤烟燃烧温度比用于煤烟燃烧的典型二氧化铈和贵金属催化剂的温度明显地低。
实施例
实施例1
用足够的硅酸钾溶液(KASIL#1,PQ Corp.,Valley Forge,PA)浸渗一个具有2×5的单元、约1.5英寸长的针状莫来石柴油机颗粒滤器(200单元/平方英寸)以充满墙孔体积,然后在115℃的烘箱干燥,该滤器用描述于WO 03/0827731A的实施例4(包括如WO 03/082773A1的实施例4中所述的至1400℃的热处理)的相同方式制得。在800℃下煅烧干燥样品1小时。
用含有分散于约0.5重量%的淤浆TRITON X-100(Rohm & Haas,Philadelphia,PA)表面活性剂的水溶液的5重量%碳黑(Regal 330R,Cabot Corporation,Boston,MA)的悬浮液对棒进行喷雾,然后在115℃的烘箱干燥。将约0.5mg的碳黑沉积在棒上以形成不透明的黑涂层。在550℃下,将该棒放置于管形熔炉中10分钟,然后移出。碳黑完全燃尽。
重复循环该棒以进行所述燃烧测试,除了将熔炉条件变为在575℃下15分钟。在48周循环之后,碳仍然完全燃尽,此时停止燃烧测试。
实施例2
使用与实施例1相同的方式制备第二个棒,除了使用SiC柴油机颗粒滤器(Ibiden Co.,LTD,Ogaki-shi,Japan)而非针状莫来石柴油机颗粒滤器。用相同方式测试该棒,并且在550℃碳完全燃尽,在28周循环之后在575℃煤烟完全燃尽,此时停止测试。
实施例3
使用与实施例1相同的方式制备第三个棒,除了使用堇青石颗粒滤器(Corning Incorporated,Corning,NY)而非针状莫来石柴油机颗粒滤器。用实施例2中所述的相同方式测试该棒并且该棒得到与实施例2相同的结果。
实施例4
使用与实施例1相同的方式制备第四个棒,除了用硅酸铯溶液(3.92SiO2:Cs2O)浸渗该棒,然后在115℃的烘箱中干燥。通过用50重量%CsOH(其余为水)加热雾化二氧化硅至85℃进行4小时以产生该溶液。在700℃下煅烧干燥样品1小时。
用相同方式测试该棒,除了将5重量%油(Mobil 1,ExxonMobilCorporation,Irving,TX)加入到碳淤浆中。在500℃下碳完全燃尽并且在550℃下经过450周循环后煤烟完全燃尽,此时停止测试。
对比实施例1
用足够的20重量%的硝酸盐稳定的二氧化铈的溶液(Nyacol NanoTechnologies,Inc,Ashland,MA)浸渗与实施例1相同的具有2×5的单元、约1.5英寸长的针状莫来石柴油机颗粒滤器的一部分,以充满墙孔体积,然后在115℃的烘箱干燥。在800℃下煅烧干燥样品1小时。如实施例1所述,在550℃下测试该棒。该棒保持为黑色,带有煤烟。
对比实施例2
用实施例1中描述的相同方法制备棒,除了不在基质中添加催化剂。如实施例1所述,在550℃下测试该棒。该棒保持为黑色,带有煤烟。

Claims (31)

1.一种触媒滤烟器,包括在多孔陶瓷的至少一部分上具有无定形催化相的多孔陶瓷,所述无定形催化相包括含有其中具有Si、Al或其结合的氧化物玻璃的碱。
2.根据权利要求1所述的触媒滤烟器,其中所述含有玻璃的碱是Na、K、Cs或它们的结合的碱。
3.根据权利要求2所述的触媒滤烟器,其中所述碱是Cs、K或它们的结合。
4.根据权利要求3所述的触媒滤烟器,其中所述碱是K。
5.根据权利要求1所述的触媒滤烟器,其中所述含有氧化物玻璃的碱是硅酸盐。
6.根据权利要求1所述的触媒滤烟器,其中所述多孔陶瓷中碱量占多孔陶瓷和无定形催化相的重量的至少约0.1至最多约7重量%。
7.根据权利要求6所述的触媒滤烟器,其中所述碱量为至少约0.2%。
8.根据权利要求7所述的触媒滤烟器,其中所述碱量为至少约0.3%。
9.根据权利要求6所述的触媒滤烟器,其中所述碱量为最多约5%。
10.根据权利要求9所述的触媒滤烟器,其中所述碱量为最多约3%。
11.根据权利要求1所述的触媒滤烟器,其中所述多孔陶瓷是莫来石、堇青石、碳化硅或它们的结合。
12.根据权利要求11所述的触媒滤烟器,其中所述多孔陶瓷是堇青石或莫来石。
13.根据权利要求12所述的触媒滤烟器,其中所述多孔陶瓷是莫来石。
14.根据权利要求13所述的触媒滤烟器,其中所述多孔陶瓷是针状莫来石。
15.一种形成触媒滤烟器的方法,包括将多孔陶瓷体暴露于含有硅酸盐、铝酸盐、铝硅酸盐或它们的结合的化合物的碱,以使得多孔陶瓷的至少一部分与含有化合物的碱接触,并且将接触的多孔陶瓷加热到足以使包含Si、Al或其结合的氧化物玻璃的碱熔于其中的温度。
16.根据权利要求15所述的方法,其中所述含有化合物的碱是为K、Na、Cs或它们的结合的碱。
17.根据权利要求16所述的方法,其中所述碱是Cs、K或它们的结合的碱。
18.根据权利要求17所述的方法,其中所述碱是K。
19.根据权利要求15所述的方法,其中所述含有化合物的碱是硅酸盐。
20.根据权利要求15所述的方法,其中所述含有化合物的碱是平均粒度为直径小于约500nm的胶体。
21.根据权利要求15所述的方法,其中所述含有化合物的碱是胶态碱硅酸盐。
22.根据权利要求21所述的方法,其中所述胶态碱硅酸盐是K、Cs或它们的结合的碱。
23.根据权利要求22所述的方法,其中所述碱是K。
24.根据权利要求15所述的方法,其中所述含有化合物的碱是粘土。
25.根据权利要求15所述的方法,其中所述多孔陶瓷体是在多孔陶瓷的陶瓷表面的至少一部分上具有氧化物相的一种,其中所述表面相包括基本上不含碱的Si、Al或其结合。
26.根据权利要求25所述的方法,其中所述多孔陶瓷是堇青石、莫来石、碳化硅或它们的结合。
27.根据权利要求26所述的方法,其中所述多孔陶瓷是莫来石或堇青石或它们的结合。
28.根据权利要求27所述的方法,其中所述多孔陶瓷是莫来石。
29.根据权利要求28所述的方法,其中所述莫来石是针状莫来石。
30.根据权利要求3所述的触媒滤烟器,其中所述碱是Cs。
31.根据权利要求17所述的方法,其中所述碱是Cs。
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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102482143A (zh) * 2009-09-30 2012-05-30 住友化学株式会社 玻璃料和利用其的碳微粒的氧化方法
CN103269774A (zh) * 2010-10-22 2013-08-28 庄信万丰股份有限公司 NOx存储组分

Families Citing this family (17)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US7485594B2 (en) * 2005-10-03 2009-02-03 Dow Global Technologies, Inc. Porous mullite bodies and methods of forming them
EP2001574B1 (en) * 2006-03-31 2011-01-19 Porvair, PLC Low expansion corrosion resistant ceramic foam filters for molten aluminum filtration
DE102006026769A1 (de) * 2006-06-09 2007-12-13 Robert Bosch Gmbh Filter zur Entfernung von Partikeln aus einem Gasstrom sowie Verfahren zu seiner Herstellung
EP2027371B1 (en) * 2006-06-15 2019-12-04 Dinex Finland Oy Coating for particulate filters
DE102006034119A1 (de) * 2006-07-24 2008-01-31 Robert Bosch Gmbh Filter zur Entfernung von Partikeln aus einem Gasstrom sowie Verfahren zu seiner Herstellung
US8356475B2 (en) 2007-02-01 2013-01-22 University Of Notre Dame Du Lac Catalysts with slow, passive release of alkali ions
US7998423B2 (en) 2007-02-27 2011-08-16 Basf Corporation SCR on low thermal mass filter substrates
CA2701486A1 (en) 2007-12-21 2009-07-09 Dow Global Technologies Inc. Improved catalyzed soot filter and method (s) to make these
US20090196812A1 (en) 2008-01-31 2009-08-06 Basf Catalysts Llc Catalysts, Systems and Methods Utilizing Non-Zeolitic Metal-Containing Molecular Sieves Having the CHA Crystal Structure
WO2010033763A1 (en) * 2008-09-18 2010-03-25 Dow Global Technologies, Inc. Method for making porous mullite-containing composites
RU2466933C1 (ru) * 2011-04-25 2012-11-20 Вера Борисовна Обухова Коллоидный алюмосиликат
IN2014CN02124A (zh) 2011-09-21 2015-05-29 Dow Global Technologies Llc
US8980187B2 (en) 2011-11-29 2015-03-17 Deere & Company Diesel particulate filters having a washcoat that improves filter performance
US9592490B2 (en) 2011-11-30 2017-03-14 University Of Notre Dame Du Lac Glass catalysts for soot combustion and methods of manufacturing the same
JP6121542B2 (ja) * 2013-08-30 2017-04-26 大塚化学株式会社 排ガス浄化フィルタ及び排ガス浄化装置
CN108290115A (zh) * 2015-07-15 2018-07-17 圣母大学 用于改善的水热耐久性的玻璃催化剂组合物
JP2022149955A (ja) * 2021-03-25 2022-10-07 日本碍子株式会社 複合焼結体、ハニカム構造体、電気加熱触媒および複合焼結体の製造方法

Family Cites Families (45)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB1119180A (en) 1966-04-01 1968-07-10 Morganite Res & Dev Ltd Forming deposits within porous material
US3460523A (en) 1967-08-28 1969-08-12 Du Pont Catalytic oven coating compositions
US4294806A (en) * 1979-02-14 1981-10-13 Sakai Chemical Industry Co., Ltd. Method for preventing the wear of a monolithic catalyst by dusts
JPS5881419A (ja) * 1981-11-12 1983-05-16 Toyota Motor Corp 微粒子の捕集材
DE3232729A1 (de) 1982-09-03 1984-03-08 Degussa Ag, 6000 Frankfurt Verfahren zur herabsetzung der zuendtemperatur von aus dem abgas von dieselmotoren herausgefiltertem dieselruss
NL8503090A (nl) 1985-11-11 1987-06-01 Harshaw Chemie Bv Werkwijze voor het bereiden van gedragen katalysator systemen.
ATE78717T1 (de) 1987-10-30 1992-08-15 Degussa Platin-freier dreiweg-katalysator.
JPH0338250A (ja) 1989-07-06 1991-02-19 Mazda Motor Corp 排気ガス浄化用触媒
CA2020453A1 (en) 1989-07-28 1991-01-29 Bulent O. Yavuz Thermal shock and creep resistant porous mullite articles
US5340516A (en) 1989-07-28 1994-08-23 Engelhard Corporation Thermal shock and creep resistant porous mullite articles prepared from topaz and process for manufacture
US5130109A (en) 1990-02-22 1992-07-14 Wan Chung Zong Catalyst composition containing segregated platinum and rhodium components
US5254519A (en) 1990-02-22 1993-10-19 Engelhard Corporation Catalyst composition containing platinum and rhodium components
US5098455A (en) 1990-12-21 1992-03-24 The Dow Chemical Company Regenerable exhaust gas filter element for diesel engines
US5198007A (en) * 1991-12-05 1993-03-30 The Dow Chemical Company Filter including a porous discriminating layer on a fused single crystal acicular ceramic support, and method for making the same
US5194154A (en) 1991-12-05 1993-03-16 The Dow Chemical Company Structure for filter or heat exchanger, composed of a fused single crystal acicular ceramic
JPH05306614A (ja) * 1992-04-28 1993-11-19 Matsushita Electric Ind Co Ltd 排気ガスフィルタとその製造方法
GB9226434D0 (en) 1992-12-18 1993-02-10 Johnson Matthey Plc Catalyst
US5611831A (en) * 1994-11-16 1997-03-18 Isuzu Ceramics Research Institute Co., Ltd. Diesel particulate filter apparatus
ZA963235B (en) 1995-06-15 1996-10-25 Engelhard Corp Diesel exhaust stream treating catalyst and method of use
US5939354A (en) 1996-04-10 1999-08-17 Catalytic Solutions, Inc. Perovskite-type metal oxide compounds and method for preparing the compounds
JP3900563B2 (ja) * 1996-10-23 2007-04-04 松下電器産業株式会社 排ガス浄化触媒及びこれを用いた排ガス浄化フィルタ
JP3382504B2 (ja) * 1997-06-03 2003-03-04 本田技研工業株式会社 排気ガス用hc浄化部材
WO1999012642A1 (en) 1997-09-09 1999-03-18 Ceramem Corporation Catalytic gas filter and methods
DE69927718T2 (de) 1998-11-13 2006-07-13 Engelhard Corp. Katalysator und verfahren zur reduzierung der abgasemissionen
WO2000062923A1 (en) 1999-04-19 2000-10-26 Engelhard Corporation Catalyst composition comprising ceria and a platinum group metal
ATE359857T1 (de) 1999-07-02 2007-05-15 Engelhard Corp Katalysatorsystem zum behandeln von abgasen aus dieselmotoren und verfahren
US6306335B1 (en) * 1999-08-27 2001-10-23 The Dow Chemical Company Mullite bodies and methods of forming mullite bodies
DE20023989U1 (de) 1999-09-29 2008-09-18 IBIDEN CO., LTD., Ogaki-shi Keramische Filteranordnung
KR100843992B1 (ko) 1999-12-23 2008-07-07 다우 글로벌 테크놀로지스 인크. 촉매 장치
US7052532B1 (en) * 2000-03-09 2006-05-30 3M Innovative Properties Company High temperature nanofilter, system and method
JP2001314762A (ja) 2000-05-11 2001-11-13 Ngk Insulators Ltd 排ガス浄化用触媒体
DE10024038A1 (de) * 2000-05-13 2001-11-22 Dmc2 Degussa Metals Catalysts Wabenkörper aus einem keramischen Material mit verbesserter radialer Druckfestigkeit
JP4075292B2 (ja) 2000-07-24 2008-04-16 トヨタ自動車株式会社 パティキュレート浄化触媒
US6826906B2 (en) 2000-08-15 2004-12-07 Engelhard Corporation Exhaust system for enhanced reduction of nitrogen oxides and particulates from diesel engines
US6423415B1 (en) 2000-08-31 2002-07-23 Corning Incorporated Potassium silicate frits for coating metals
US7524546B2 (en) * 2000-12-28 2009-04-28 3M Innovative Properties Company Thermal insulating material and pollution control device using the same
JP4404497B2 (ja) 2001-03-01 2010-01-27 日本碍子株式会社 ハニカムフィルター、及びその製造方法
US20020172633A1 (en) 2001-03-06 2002-11-21 Koermer Gerald S. Vehicular atmosphere cleansing system
US6624113B2 (en) 2001-03-13 2003-09-23 Delphi Technologies, Inc. Alkali metal/alkaline earth lean NOx catalyst
WO2003011437A1 (en) 2001-08-01 2003-02-13 Johnson Matthey Public Limited Company Gasoline engine with an exhaust system for combusting particulate matter
US6736875B2 (en) 2001-12-13 2004-05-18 Corning Incorporated Composite cordierite filters
CA2480167C (en) 2002-03-25 2011-03-08 Dow Global Technologies Inc. Mullite bodies and methods of forming mullite bodies
US6764664B2 (en) 2002-04-22 2004-07-20 Delphi Technologies, Inc. Catalyst for the combustion of diesel soot, methods for making the catalyst and methods of using the catalyst
JP4750415B2 (ja) 2002-07-31 2011-08-17 コーニング インコーポレイテッド チタン酸アルミニウムベースのセラミック製品
US6849181B2 (en) 2002-07-31 2005-02-01 Corning Incorporated Mullite-aluminum titanate diesel exhaust filter

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102482143A (zh) * 2009-09-30 2012-05-30 住友化学株式会社 玻璃料和利用其的碳微粒的氧化方法
CN103269774A (zh) * 2010-10-22 2013-08-28 庄信万丰股份有限公司 NOx存储组分
CN103269774B (zh) * 2010-10-22 2016-06-08 庄信万丰股份有限公司 NOx存储组分

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