Catalytic isomerisation of α-pinene oxide to campholenic aldehyde using silica-supported zinc triflate catalysts: I. Kinetic and thermodynamic studies
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[1] Don W. Green,et al. Perry's Chemical Engineers' Handbook , 2007 .
[2] Kamelia Boodhoo,et al. Catalytic isomerisation of α-pinene oxide to campholenic aldehyde using silica-supported zinc triflate catalysts: II. Performance of immobilised catalysts in a continuous spinning disc reactor , 2007 .
[3] J. Clark,et al. Classical cationic polymerization of styrene in a spinning disc reactor using silica‐supported BF3 catalyst , 2006 .
[4] Colin Grant,et al. 7th World Congress of Chemical Engineering: A Review , 2005 .
[5] G. Neri,et al. Isomerization of α-pinene oxide to campholenic aldehyde over Lewis acids supported on silica and titania nanoparticles , 2005 .
[6] J. Clark,et al. Rearrangement of α-pinene oxide using a surface catalysed spinning disc reactor (SDR) , 2004 .
[7] James H. Clark,et al. Solid acids for green chemistry. , 2002, Accounts of chemical research.
[8] Kamelia Boodhoo,et al. Process intensification: spinning disk reactor for styrene polymerisation , 2000 .
[9] K. Wilson,et al. Novel heterogeneous zinc triflate catalysts for the rearrangement of α-pinene oxide , 1999 .
[10] Colin Ramshaw,et al. Process intensification : heat and mass transfer characteristics of liquid films on rotating discs , 1999 .
[11] J. Clark,et al. Catalysis of liquid phase organic reactions using chemically modified mesoporous inorganic solids , 1998 .
[12] J. C. van der Waal,et al. Application of zeolite titanium Beta in the rearrangement of α-pinene oxide to campholenic aldehyde , 1998 .
[13] W. Hölderich,et al. The use of zeolites in the synthesis of fine and intermediate chemicals , 1997 .
[14] C. Ramshaw,et al. Process intensification: Heat transfer characteristics of tailored rotating surfaces , 1994 .
[15] K. Arata,et al. ISOMERIZATION OF α-PlNENE OXIDE OVER SOLID ACIDS AND BASES , 1979 .
[16] Tran Phuc Thinh,et al. Estimation of standard heats of formation ΔH *fT, standard entropies of formation ΔS *fT, standard free energies of formation ΔF *fT and absolute entropies S *fT of hydrocarbons from group contributions: An accurate approach , 1976 .
[17] R. S. Ramalho,et al. Estimation of Ideal Gas Heat Capacities of Hydrocarbons from Group Contribution Techniques. New and Accurate Approach , 1971 .
[18] John B. Lewis,et al. Reaction of α-Pinene Oxide with Zinc Bromide and Rearrangement of 2,2,3-Trimethyl-3-cyclopentene Products Derived Therefrom1 , 1965 .
[19] L. Doraiswamy,et al. Estimation of Heats of Formation of Organic Compounds , 1965 .
[20] Kamelia Boodhoo,et al. Process intensification: spinning disc reactor for condensation polymerisation , 2000 .
[21] Reinhard Koehler,et al. Shear degradation and deformation of polysaccharides in thin liquid film flow on a rotating disk. , 2000 .
[22] W. Hölderich,et al. Selective isomerization of α-pinene oxide with heterogeneous catalysts , 1997 .
[23] L. Gladden,et al. Transport heterogeneity in porous pellets—II. NMR imaging studies under transient and steady-state conditions , 1995 .
[24] W. Hölderich. New Reactions in Various Fields and Production of Specialty Chemicals , 1993 .
[25] Schwegler,et al. The isomerization of α‐pinene oxide with Brønsted and Lewis acids , 1992 .
[26] N. Brauner,et al. Modeling of wavy flow in inclined thin films , 1983 .
[27] G. Bond,et al. Heterogeneous Catalysis: Principles and Applications , 1974 .
[28] Irving M. Klotz,et al. Chemical Thermodynamics: Basic Theory and Methods , 1972 .
[29] J. M. Thomas,et al. Introduction to the principles of heterogeneous catalysis , 1967 .