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    • 2. 发明授权
    • High silica content zeolite-based catalyst
    • 高二氧化硅含量的沸石基催化剂
    • US06207605B1
    • 2001-03-27
    • US08905409
    • 1997-08-04
    • Masatsugu KawaseKouji NomuraYukito NagamoriJiro Kinoshita
    • Masatsugu KawaseKouji NomuraYukito NagamoriJiro Kinoshita
    • B01J2904
    • C10G11/05B01J29/70B01J2229/16B01J2229/36C10G35/095
    • A high silica content zeolite-based catalyst for use in a reaction which uses a feedstock containing an aromatic hydrocarbon or which gives a product containing an aromatic hydrocarbon, which catalyst satisfies the following requirements (1), (2), (3) and (4): (1) the zeolite constituting a zeolite-based catalyst has an SiO2/Al2O3 molar ratio of from 20 to 200; (2) the zeolite constituting a zeolite-based catalyst has a primary particle diameter of from 0.3 to 3 &mgr;m; (3) when a zeolite-based catalyst is converted into H type, the H type zeolite-based catalyst has a ratio of the number of surface acid sites to the total number of acid sites is from 0.03 to 0.15; and (4) a zeolite-based catalyst exhibits a pyridine-desorbed amount (B) as measured at a temperature of from 500° C. to 900° C. by a hot desorption method when converted into H type after being subjected to a steam treatment at an H2O partial pressure of 0.8 atm and a temperature of 650° C. for 5 hours, and a pyridine-desorbed amount (A) as measured at a temperature of from 500° C. to 900° C. by a hot desorption method when converted into H type without the steam treatment, which amounts satisfy the following requirements: &agr;≦1.6 α = ( 1 B 2 - 1 A 2 ) ÷ 5 × 10 5 .
    • 用于反应中的高二氧化硅含量的沸石基催化剂,其使用含有芳族烃的原料或产生含有芳族烃的产物,该催化剂满足以下要求(1),(2),(3)和( 4):(1)构成沸石型催化剂的沸石的SiO 2 / Al 2 O 3摩尔比为20〜200; (2)构成沸石型催化剂的沸石的初级粒径为0.3〜3μm; (3)当沸石型催化剂转化为H型时,H型沸石型催化剂的表面酸性位数与酸性位置总数之比为0.03〜0.15; 和(4)沸石型催化剂在通过热脱附法在500℃〜900℃的温度下测定的吡啶解吸量(B)后,在经受蒸汽后变为H型时 在H 2 O分压为0.8atm,温度为650℃下处理5小时,并通过热解吸在500℃至900℃的温度下测定吡啶解吸量(A) 方法转换为H型无蒸汽处理,其数量满足以下要求: