Fluidized oligomerization

Claim 2

A process for oligomerizing olefins comprising: (a) fluidizing a fluidizable oligomerization catalyst comprising an essentially aluminum-free intermediate pore size silicaceous crystalline molecular sieve having a silica:alumina mole ratio greater than about 200:1 with a feed including gaseous olefins in an oligomerization reaction zone; and (b) converting at least 30% of said gaseous olefins to higher boiling olefins by maintaining oligomerization reaction zone at oligomerization conditions including a temperature of less than 400° C. and a gas hourly space velocity of said feed sufficient to fluidize at least a portion of said catalyst.

Claim 3

A process for treating a normally gaseous component of the effluent from a catalytic cracking zone, said component including normally gaseous olefins, comprising: (a) fluidizing a fluidizable oligomerization catalyst comprising an essentially aluminum-free intermediate pore size silicaceous crystalline molecular sieve having a silica:alumina mole ratio greater than about 200:1 with at least a portion of said normally gaseous component in an oligomerization reaction zone; and (b) converting at least 30% of said normally gaseous olefins to higher boiling olefins by maintaining said oligomerization reaction zone at oligomerization conditions including a temperature of less than 400° C. and a gas hourly space velocity of said normally gaseous component sufficient to fluidize at least a portion of said catalyst.

Claim 4

A process for treating a normally gaseous component of the effluent from a catalytic cracking zone, said component including normally gaseous olefins, comprising: (a) fluidizing a fluidizable oligomerization catalyst comprising an essentially aluminum-free intermediate pore size silicaceous crystalline molecular sieve having a silica:alumina mole ratio greater than about 200:1 with at least a portion of said normally gaseous component in an oligomerization reaction zone; and (b) converting at least 30% of said normally gaseous olefins to higher boiling olefins by maintaining said oligomerization reaction zone at oligomerization conditions including a temperature of less than 400° C. and a gas hourly space velocity of said normally gaseous component sufficient to fluidize at least a portion of said catalyst.

Claim 5

The process of claim 1 wherein said olefins comprise C 3 and C 4 olefins.

Claim 6

The process of claim 1 or 2 wherein said oligomerization catalyst comprises attrition-resistant essentially aluminum-free intermediate pore size silicaceous crystalline molecular sieve particles.

Claim 7

The process of claim 1 or 2 wherein said molecular sieve is silicalite or a crystalline metal organosilicate disclosed in U.S. Pat. No. Re. 29,948.

Claim 8

The process of claim 1 or 2 wherein said silica:alumina ratio is greater than about 500:1.

Claim 9

The process of claim 6 wherein said silica:alumina ratio is greater than about 1000:1.

Claim 10

The process of claim 4 wherein said catalyst further comprises zinc or a compound thereof.

Claim 11

The process of claim 5 wherein said catalyst further comprises zinc or a compound thereof.

Claim 12

The process of claim 1 or 2, further comprising: contacting through heat exchanging means at least part of the effluent of said oligomerization zone with said feed.

Claim 13

The process of claim 1 or 2, further comprising: periodically removing said catalyst from contact with said feed; stripping said catalyst with a stripping gas; and recontacting said catalyst with said feed.

Claim 14

The process of claim 11 wherein said stripping gas is steam.

Claim 15

The process of claim 1 or 2, further comprising: hydrogenating at least part of the effluent of said oligomerization reaction zone.

Claim 16

The process of claim 1 or 2 further comprising: introducing at least part of the olefin oligomers present in the effluent from said oligomerization reaction zone into at least one further oligomerization reaction zone.

Claim 17

The process of claim 14 wherein said olefin oligomers are contacted in said further oligomerization reaction zone with an intermediate pore size silicaceous molecular sieve under reaction conditions such that at least some of said oligomers are liquids.