Abstract:
AN IMPROVED OXIDATIVE DEHYDROGENATION CATALYST COMPRISING A LITHIUM-TIN-PHOSPHORUS-OXYGEN COMPOSITION IS DISCLOSED. ALSO IS A METHOD OF REACTIVATING A COMPOSITION OF A SIMILAR NATURE. THE IMPROVED CATALYST AND THE REACTIVATED CATALYST, BOTH ARE FORMED BY PROCEDURES INVOLVING PHOSPHORUS DEPOSITION.
Abstract:
THE ACTIVITY OF TIN-PHOSPHORUS OXIDATIVE DEHYDROGENATION CATALYSTS IS SIGNIFICANTLY IMPROVED BY INCLUDING A HEATVOLATILE ACTIVITY-STIMULATING AMMONIUM SALT IN THE CATALYST COMPOSITION PRIOR TO THE CATALYST PARTICLE-FORMING STAGE.
Abstract:
THE PROPERTIES OF A LITHIUM-TIN-PHOSPHOROUS CATALYST ACTIVE FOR THE OXIDATIVE DEHYDROGENATION OF HYDROCARBONS ARE IMPROVED BY THE DEPOSITION OF OXIDES OF ALUMINUM AND CALCIUM ON THE CATALYST.
Abstract:
AN OXIDATIVE DEHYDROGENATION PROCESS WHEREIN A TIN/ PHSOPHROUS/OXYGEN/GROUPS IA OR IIA IS IMPREGNATED WITH ADDITIONAL TIN AND THEN IS HEATED TO IMPROVED THE PHYSICAL INTEGRITY OF THE CATALYST.
Abstract:
THE ACTIVITY OF A CATALYST USEFUL FOR THE OXIDATIVE DEHYDROGENATION OF OLEFINS COMPRISING OXIDES OF PHOSPHORUS AND TIN IS IMPROVED BY TREATING THE CATALYST WITH SUPERHEATED STEAM TO PRODUCE A CATALYST HAVING A SURFACE AREA OF WHICH AT LEAST 2 M.2/G. IS COMPRISED OF PORES HAVING DIAMETERS OF AT LEAST 700* A.
Abstract:
A METHOD FOR THE SELECTIVE HYDROGENATION OF ACETYLENE IS DESCRIBED COMPRISING CONTACT OF ACETYLENE AND AN OLEFININ MIXTURE WITH HYDROGEN IN THE PRESENCE OF A CATALYST CONSISTING OF NICKEL SUPPORTED ON ALUMINA, WHEREIN AT LEAST A SUBSTANTIAL PORTION OF THE PORES IN THE ALUMINA HAVE A DIAMETER OF AT LEAST 120 A.
Abstract:
Catalysts comprising iron, nickel or cobalt, and antimony or arsenic supported on alumina having relatively few pores smaller in diameter than 500 A and a surface area not less than 2 M2/g contributed by pores having diameters larger than about 500 A are used for selective hydrogenation of hydrocarbons.