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    • 1. 发明授权
    • Process for producing silicon carbide fiber
    • 碳化硅纤维生产工艺
    • US06316051B2
    • 2001-11-13
    • US09216854
    • 1998-12-21
    • Kaoru Okada
    • Kaoru Okada
    • C23C1638
    • D01F9/08C04B35/573C04B35/62272D01F11/12
    • Silicon carbide fibers having an excellent mechanical strength and a superior heat resistance can be produced by the process in which activated carbon fibers having a thickness of 1 to 30 &mgr;m and a BET specific surface area of 700 to 1500 m2/g are reacted with a silicon and/or silicon oxide gas at 1200 to 1500° C. under a reduced pressure or in an inert gas atmosphere; and the resultant SiC fibers are heat treated in the presence of a boron-containing substance and optionally a carbon-containing substance at 1700 to 2300° C. in an inert gas atmosphere, wherein the fibers may be in the form of a shaped article, for example, a sheet or honeycomb structure.
    • 具有优异的机械强度和优异的耐热性的碳化硅纤维可以通过将厚度为1〜30μm,BET比表面积为700〜1500m 2 / g的活性炭纤维与硅 和/或二氧化硅气体,在减压或惰性气体气氛中,在1200〜1500℃下, 并且在惰性气体气氛中,在含硼物质和任选的含碳物质的存在下,将所得的SiC纤维进行热处理,其中所述纤维可以是成形制品的形式, 例如,片状或蜂窝结构体。
    • 2. 发明授权
    • Method of producing silicon carbide fibers
    • 生产碳化硅纤维的方法
    • US5676918A
    • 1997-10-14
    • US745206
    • 1996-11-08
    • Kaoru OkadaKeihachiro Nakajima
    • Kaoru OkadaKeihachiro Nakajima
    • C04B35/573C04B35/622C01B31/36
    • C04B35/62272C04B35/573
    • Silicon carbide fibers having a high mechanical strength at a high temperature, an excellent heat resistance and a uniform structure are produced by activating carbon fibers which have been produced by heat-treating organic carbon fibers such as cellulose, polyacrylonitrile or petroleum pitch, polyimide or phenol resin fibers in an oxidative gas atmosphere and carbonizing the heat-treating organic fibers in an inert gas, with an activating gas, for example, water vapor, to convert them to the activated porous carbon fibers having a specific surface area of 100 to 3,000 m.sup.2 /g, a length of 5 mm or more and a thickness of 5 to 100 .mu.m; reacting the activated porous carbon fibers with a silicon monoxide gas at a temperature of 800.degree. C. to 2,000.degree. C. under a reduced pressure of 10.sup.2 Pa or less to convert them to silicon carbide fibers having a length of 5 mm or more, without generating whiskers; and optionally the resultant silicon carbide fibers are heat-treated at a temperature of 800.degree. C. to 2,000.degree. C. in the presence of an oxidative gas.
    • 通过活化通过热处理诸如纤维素,聚丙烯腈或石油沥青的有机碳纤维,聚酰亚胺或苯酚生产的碳纤维来生产在高温下具有高机械强度,优异的耐热性和均匀结构的碳化硅纤维 树脂纤维在氧化性气体气氛中,并将惰性气体中的热处理有机纤维与活化气体例如水蒸汽碳化,将其转化成比表面积为100〜3000m 2的活性多孔碳纤维 / g,长度为5mm以上,厚度为5〜100μm; 使活化的多孔碳纤维与一氧化碳气体在800℃至2000℃的温度下在102Pa或更低的压力下反应,以将其转化成长度为5mm或更大的碳化硅纤维,而没有 生成晶须 并且任选地,在氧化气体存在下,将所得碳化硅纤维在800℃至2000℃的温度下进行热处理。
    • 5. 发明授权
    • Sizing agent for use in making paper
    • 用于制作纸张的上浆剂
    • US4200562A
    • 1980-04-29
    • US888644
    • 1978-03-21
    • Shigehiko YoshiokaKaoru Okada
    • Shigehiko YoshiokaKaoru Okada
    • C08F2/28D21H17/35D21H17/37D21H17/45C08L33/14
    • D21H17/35C08F2/28D21H17/455
    • A neutral sizing agent of emulsion type to be added to paper pulp for facilitating the disaggregation and recovery of waste paper in making paper including paper board, said sizing agent being produced, for example, by dispersing in an aqueous emulsifying dispersion medium a polymerizable hydrophobic monomer such as styrene or 2-ethylhexyl methacrylate by using as an emulsifying dispersing agent a copolymer having units of one or more monomers given by the formula ##STR1## or ##STR2## wherein R is H or CH.sub.3,X is a halogen atom,A is a (C.sub.2 -C.sub.6) alkylene group, andY is an anion,and a monomer given by the formula ##STR3## wherein R.sup.1, R.sup.2 are H or CH.sub.3, and then subjecting the resultant dispersion to a radical emulsion polymerization.
    • 一种乳液型中性上浆剂加入到纸浆中,用于在制造包括纸板的纸张中促进废纸的分解和回收,所述施胶剂例如通过在水性乳化分散介质中分散可聚合的疏水单体 例如苯乙烯或甲基丙烯酸2-乙基己酯通过使用由下式(IMAGE)或其中R为H或CH 3的单体给出的单体的共聚物,X为卤素原子,A为 (C2-C6)亚烷基,Y为阴离子,通式为:其中R1,R2为H或CH3,然后将所得分散体进行自由基乳液聚合。
    • 9. 发明申请
    • SYSTEM FOR DETERMINING NUMBER OF PARTICLES
    • 用于确定颗粒数的系统
    • US20120090377A1
    • 2012-04-19
    • US13259018
    • 2010-04-02
    • Takashi MatsuyamaMasayoshi ShinoharaYoshinori OtsukiKaoru OkadaMasanobu Akita
    • Takashi MatsuyamaMasayoshi ShinoharaYoshinori OtsukiKaoru OkadaMasanobu Akita
    • G01M15/10
    • G01N1/2252G01N2001/2264G01N2015/0675
    • Provided is a system for determining a number of particles, which has a simplified and compact structure as well as a reduced cost. The system comprises a diluter (PND2) arranged at a connecting point of a main flow channel (ML) and a dilution gas flow channel (DL), a dilution gas flow rate control part (MFC3) that controls the flow rate of the dilution gas introduced into the diluter (PND2), a particle number measuring unit (2) that measures a number of solid particles in a diluted exhaust gas, a bypass flow channel (BL3) that bifurcates from between the diluter (PND2) and the particle number measuring unit (2) in the main flow channel (ML) and in which a constant flow rate unit (CFO3) is arranged, a suction pump (P) that is connected downstream of a converged point of the main flow channel (ML) and the bypass flow channel (BL3), and an information processing unit (4) that calculates the dilution factor of the exhaust gas based on a dilution gas flow rate (Q1) controlled by the dilution gas flow rate control part (MFC3), and a total of a unit flow rate (Q2) of the particle number measuring unit (2) and a set flow rate (Q3) of the constant flow rate unit (CFO3).
    • 提供了一种用于确定颗粒数量的系统,其具有简化且紧凑的结构以及降低的成本。 该系统包括布置在主流路(ML)和稀释气流通道(DL)的连接点处的稀释器(PND2),稀释气体流量控制部分(MFC3),其控制稀释气体的流量 引入到稀释器(PND2)中的粒子数测量单元(2),其测量稀释废气中的固体颗粒数量,从稀释剂(PND2)和测量颗粒数之间分叉的旁路流动通道(BL3) 主流通道(ML)中的单元(2),其中布置有恒流量单元(CFO3);吸入泵(P),其连接在主流路(ML)的汇聚点的下游, 旁路流路(BL3)以及基于由稀释气体流量控制部(MFC3)控制的稀释气体流量(Q1))计算废气的稀释系数的信息处理单元(4) 的粒子数测量单元(2)的单位流量(Q2)和设定流量 恒定流量单位(CFO3)的速率(Q3)。