Claims
- 1. Process for converting a hydrocarbon which comprises contacting said hydrocarbon under hydrocarbon converting conditions with a microporous crystalline silicoaluminophosphate the pores of which are uniform and have nominal diameters of greater than about 3 Angstroms and whose essential empricial chemical composition in the as-synthesized and anhydrous form is
- mR:(Si.sub.x Al.sub.y P.sub.z)O.sub.2
- wherein "R" represents at least one organic templating agent present in the intracrystalline pore system; "m" has a value of from 0.02 to 0.3; "m" represents the moles of "R" present per mole of (Si.sub.x Al.sub.y P.sub.z)O.sub.2 ; "x", "y" and "z" represent the mole fractions of silicon, aluminum and phosphorus respectively, present as tetrahedral oxides, said mole fractions being such that they are within the pentagonal compositional area defined by points ABCD and E of the ternary diagram which is FIG. 1 of the drawings.
- 2. Process according to claim 1 wherein the silicoaluminophosphate has been calcined at a temperature sufficiently high to remove at least some of the organic templating agent present in the intracrystalline pore system.
- 3. Process according to claim 2 wherein the mole fractions of silicon, aluminum and phosphorus of the silicoaluminophosphate are within the pentagonal compositional area defined by points a, b, c, d and e of the ternary diagram which is FIG. 2 of the drawings.
- 4. Process according to claim 2 wherein the silicoaluminophosphate has a characteristic X-ray powder diffraction pattern which contains at least the d-spacings set forth below in any one of Tables I, III, V, VII, IX, XIII, XVII, XXI, XXIII or XXV.
- 5. Process according to claim 1 wherein the silicoaluminophosphate has a characteristic X-ray powder diffraction pattern which contains at least d-spacings set forth below in any one of Tables I, III, V, VII, IX, XIII, XVII, XXI, XXIII or XXV.
- 6. Process according to claim 1 wherein the hydrocarbon conversion process is cracking.
- 7. Process according to claim 1 wherein the hydrocarbon conversion process is hydrocracking.
- 8. Process according to claim 1 wherein the hydrocarbon conversion process is hydrogenation.
- 9. Process according to claim 1 wherein the hydrocarbon conversion process is polymerization.
- 10. Process according to claim 1 wherein the hydrocarbon conversion process is alkylation.
- 11. Process according to claim 1 wherein the hydrocarbon conversion process is reforming.
- 12. Process according to claim 1 wherein the hydrocarbon conversion process is hydrotreating.
- 13. Process according to claim 1 wherein the hydrocarbon conversion process is isomerization.
- 14. Process according to claim 1 wherein the isomerization is xylene isomerization.
- 15. Process according to claim 1 wherein the hydrocarbon conversion process is dehydrocyclization.
Parent Case Info
This application is a continuation of prior U.S. application Ser. No. 575,745, filing date Jan. 31, 1984, now abandoned, which is a division of application Ser. No. 400,438, filing date Jul. 26, 1982, now U.S. Pat. No. 4,440,871.
US Referenced Citations (11)
Divisions (1)
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400438 |
Jul 1982 |
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Continuations (1)
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575745 |
Jan 1984 |
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