TRANSFORMATIONS OF N-HEXANE ON EUROPT-1 AT LOW CONVERSIONS

被引:16
作者
PAAL, Z [1 ]
ZHAN, ZQ [1 ]
MANNIGER, I [1 ]
MUHLER, M [1 ]
机构
[1] MAX PLANCK GESELL, FRITZ HABER INST, W-1000 BERLIN 33, GERMANY
来源
APPLIED CATALYSIS | 1990年 / 66卷 / 02期
关键词
ageing; catalyst characterization (XPS); coke formation; EuroPt-1; hexane skeletal reactions; platinum/silica; regeneration;
D O I
10.1016/S0166-9834(00)81646-2
中图分类号
O64 [物理化学(理论化学)、化学物理学];
学科分类号
070304 ; 081704 ;
摘要
Skeletal reactions of n-hexane were studied over Pt/SiO2 (EuroPt-1) at conversions approaching zero. Various catalyst activation procedures involve the removal of different amounts of surface carbon as checked by XPS of carbon, therefore various activities are observed in the first runs. Activity vs, time as well as selectivity vs. conversion curves and optimum performance envelopes (OPE), i.e. yield vs. conversion plots are presented over catalysts cleaned by several oxidation-reduction cycles. In the very first moments of contact of n-hexane with the catalyst, on a relatively clean, hydrogen covered platinum ("Pt-H"), hydrogenolysis to methane and benzene formation are preferred reactions. A primary C5-cyclization, in some cases also isomerization is possible. Thereafter, a "Pt-C-H" system is built up gradually: single, internal hydrogenolysis and nondegradative reactions are characteristic of this period of catalyst life. Over a more severely carbonized catalysts (a "Pt-C" state), sequential terminal fission and alkene formation predominates. Aromatization seems to occur with rather constant selectivity over Pt-C-H and Pt-C. The lifetime of the Pt-H state is up to ca. 1-2 min at 603 K whereas Pt-C-H lasts for several minutes; higher hydrogen pressures preserve these states longer. At 693 K, the initial clean Pt (or Pt-H) can transform directly to Pt-C. © 1990.
引用
收藏
页码:301 / 317
页数:17
相关论文
共 41 条
[1]   THE CATALYTIC ISOMERIZATION OF 1-HEXENE ON H-ZSM-5 ZEOLITE - THE EFFECTS OF A SHAPE-SELECTIVE CATALYST [J].
ABBOT, J ;
CORMA, A ;
WOJCIECHOWSKI, BW .
JOURNAL OF CATALYSIS, 1985, 92 (02) :398-408
[2]   THE INFLUENCE OF METAL SUPPORT INTERACTIONS ON THE REACTION OF NORMAL-HEXANE OVER SUPPORTED PT CATALYSTS [J].
ANDERSON, JBF ;
BURCH, R ;
CAIRNS, JA .
JOURNAL OF CATALYSIS, 1987, 107 (02) :364-374
[3]   IDENTIFYING PRIMARY AND SECONDARY PRODUCTS OF CATALYTIC CRACKING OF CUMENE [J].
BEST, D ;
WOJCIECHOWSKI, BW .
JOURNAL OF CATALYSIS, 1977, 47 (01) :11-27
[4]  
BOND GC, 1985, APPL CATAL, V18, P221
[5]   CHARACTERIZATION OF THE STANDARD PLATINUM SILICA CATALYST EUROPT-1 .6. CATALYTIC PROPERTIES [J].
BOND, GC ;
GARIN, F ;
MAIRE, G .
APPLIED CATALYSIS, 1988, 41 (1-2) :313-335
[6]   COMPARATIVE-STUDY OF VARIOUS PLATINUM CATALYSTS IN SKELETAL REACTIONS OF C6-HYDROCARBONS [J].
BRAGIN, OV ;
KARPINSKI, Z ;
MATUSEK, K ;
PAAL, Z ;
TETENYI, P .
JOURNAL OF CATALYSIS, 1979, 56 (02) :219-228
[7]  
CANDY JP, 1980, J CHEM SOC F1, V76, P1704
[8]   INTERACTION OF HYDROGEN WITH PT(111) - ROLE OF ATOMIC STEPS [J].
CHRISTMANN, K ;
ERTL, G .
SURFACE SCIENCE, 1976, 60 (02) :365-384
[9]   SURFACE-STRUCTURE AND TEMPERATURE-DEPENDENCE OF N-HEXANE SKELETAL REARRANGEMENT REACTIONS CATALYZED OVER PLATINUM SINGLE-CRYSTAL SURFACES - MARKED STRUCTURE SENSITIVITY OF AROMATIZATION [J].
DAVIS, SM ;
ZAERA, F ;
SOMORJAI, GA .
JOURNAL OF CATALYSIS, 1984, 85 (01) :206-223
[10]   MECHANISMS OF 1,5-DEHYDROCYCLIZATION AND ISOMERIZATION OF ALKANES ON IRIDIUM, RHODIUM, PALLADIUM AND PLATINUM FILMS [J].
FINLAYSON, OE ;
CLARKE, JKA ;
ROONEY, JJ .
JOURNAL OF THE CHEMICAL SOCIETY-FARADAY TRANSACTIONS I, 1984, 80 :191-209