Conversion of certain hydrocarbons using silicoaluminophosphate catalysts

Claim 2

A low severity process for the preparation of a benzene-toluene-xylenes enriched stream containing minimal monoolefin and diolefin content, from a feed stream comprising a by-product effluent of a process for the pyrolitic cracking of hydrocarbons to produce light olefins or diolefins, said by-product effluent stream containing olefins and diolefins, said process comprising contacting said by-product effluent stream, under low severity conditions including a temperature within the range of about 300°-700° C., a pressure within the range of about 0 to 100 atmospheres, and a weight hourly space velocity within the range of about 0.1 to about 20, with a catalyst comprising a silicoaluminophosphate molecular sieve.

Claim 3

The process of claim 1 wherein the silicoaluminophosphate molecular sieve has a unit empirical formula on an anhydrous basis of: 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" represents the moles of "R" present per mole of (Si x Al y P z )O 2 and has a value from zero (0) to about 0.3, with the maximum value of m being related, at least in part, to the molecular dimensions of the template and the void volume of the intracrystalline pore system of the particular SAPO; "x", "y" and "z" represent the mole fractions of silicon, aluminum and phosphorus, respectively, present as tetrahedral oxide units, said mole fractions being within the pentagonal compositional area defined by points A, B, C, D and E of the ternary compositional diagram depicted by FIG. 1 of the drawings where the points A, B, C, D and E are represented by the following values for "x", "y" and "z": ______________________________________ Mole Fraction Point x y z ______________________________________ A 0.01 0.47 0.52 B 0.94 0.01 0.05 C 0.98 0.01 0.01 D 0.39 0.60 0.01 E 0.01 0.60 0.39 ______________________________________

Claim 4

The process of claim 2 wherein the silicoaluminophosphate has a minimum value for "m" of 0.02 in the as-synthesized form and have values for "x", "y" and "z" within the pentagonal compositional area defined by the points a, b, c, d and e of the ternary diagram which is FIG. 2 of the drawings, wherein said points a, b, c, d and e are represented by the following values for "x", "y" and "z": ______________________________________ Mole Fraction Point x y z ______________________________________ a 0.02 0.49 0.49 b 0.25 0.37 0.38 c 0.25 0.48 0.27 d 0.13 0.60 0.27 e 0.02 0.60 0.38 ______________________________________

Claim 5

Process of claim 1 wherein said conditions include a temperature within the range of about 350°-600° C., a pressure within the range of about 0-7 atmospheres, and a weight hourly space velocity within the range of about 0.5-5.0.

Claim 6

Process of claim 1 wherein said by-product effluent comprises a C 4 stream.

Claim 7

Process of claim 1 wherein said by-product effluent comprises a C 5 stream.

Claim 8

Process of claim 1 wherein said by-product effluent comprises a whole or fractionated dripolene stream.

Claim 9

Process of claim 1 wherein said feed stream is admixed with a diluent.

Claim 10

Process of claim 6 wherein said diluent is steam.

Claim 11

Process of claim 6 wherein said diluent is hydrogen.

Claim 12

Process of claim 6 wherein said diluent is a low boiling paraffin.

Claim 13

Process of claim 6 wherein said diluent is a mixture of a low boiling paraffin, hydrogen and/or steam.

Claim 14

Process of claim 2 wherein the silicoaluminophosphate is SAPO-11.

Claim 15

Process of claim 2 wherein the silicoaluminophosphate is SAPO-31.

Claim 16

Process of claim 2 wherein the silicoaluminophosphate is SAPO-5.