Abstract 2. A CRYSTALLINE SYNTHETIC CATALYST MATERIAL HAVING THE COMPOSITION: ((X/N)M(1 +OR- 0.1-X)H)ALO2.YSIO2.WH2O WHERE X IS LESSS THAN 1, Y IS GREATER THAN 5 BUT LESS THAN 100, W IS UP TO ABOUT 4, M IS A METAL, AND N IS THE VALENCE OF M, SAID MATERIAL BEING CHARACTERIZED BY AN X-RAY POWDER DIFFRACTION PATTERN ESSENTIALLY THE SAME AS THAT SHOWN IN TABLE 4. 15. IN A PROCESS FOR CONDUCTING IN THE PRESENCE OF A SOLID POROUS CATALYST A HYDROCARBON CONVERSION REACTION CHARACTERIZED BY A HEAT OF REACTION NOT LESS THAN ZERO, THE IMPROVEMENT WHICH COMPRISES CONTACTING CHARGE HYDROCARBONS FOR SAID REACTION AT CONVERSION CONDITIONS WITH A CRYSTALLINE ALUMINOSILICATE CATALYST AT LEAST PARTIALLY IN THE HYDROGEN FORM RESULTING FROM TREATMENT OF THE ZEOLITE DEFINED IN CLAIM 2 WITH A FLUID MEDIUM CONTAINING IONS SELECTED FROM THE GROUP CONSISTING OF HYDROGEN IONS AMMONIUM IONS.
A CRYSTALLINE SYNTHETIC CATALYST MATERIAL HAVING THE COMPOSITION: ((X/N)M(1 +OR- 0.1-X)H)ALO2.YSIO2.WH2O WHERE X IS LESSS THAN 1, Y IS GREATER THAN 5 BUT LESS THAN 100, W IS UP TO ABOUT 4, M IS A METAL, AND N IS THE VALENCE OF M, SAID MATERIAL BEING CHARACTERIZED BY AN X-RAY POWDER DIFFRACTION PATTERN ESSENTIALLY THE SAME AS THAT SHOWN IN TABLE 4.
Claim 2
Dependent Claim
78 words
IN A PROCESS FOR CONDUCTING IN THE PRESENCE OF A SOLID POROUS CATALYST A HYDROCARBON CONVERSION REACTION CHARACTERIZED BY A HEAT OF REACTION NOT LESS THAN ZERO, THE IMPROVEMENT WHICH COMPRISES CONTACTING CHARGE HYDROCARBONS FOR SAID REACTION AT CONVERSION CONDITIONS WITH A CRYSTALLINE ALUMINOSILICATE CATALYST AT LEAST PARTIALLY IN THE HYDROGEN FORM RESULTING FROM TREATMENT OF THE ZEOLITE DEFINED IN CLAIM 2 WITH A FLUID MEDIUM CONTAINING IONS SELECTED FROM THE GROUP CONSISTING OF HYDROGEN IONS AMMONIUM IONS.