Separation of a mixture of normal paraffins branched chain paraffins and cyclic paraffins

Claim 2

A process for separating a mixture of saturated hydrocarbons into normal paraffins, branched chain paraffins, and cyclic paraffins, which comprises: contacting said mixture at retention conditions with a molecular sieve comprising a first silicalite having a pore size and crystal structure which will retain normal paraffins, and pass through branched chain paraffins and cyclic paraffins; contacting at retention conditions the unretained mixture of branched chain paraffins and cyclic paraffins with a molecular sieve comprising a second silicalite having a pore size and crystal structure which will retain branched chain paraffins and pass through cyclic paraffins, said second silicalite heated to a temperature of at least 70° C.; recovering the cyclic paraffins unretained by the second silicalite; recovering the normal paraffins by displacing the normal paraffins from the first silicalite with a displacement material; and recovering the branched chain paraffins by displacing the branched chain paraffins from the second silicalite with a displacement material.

Claim 3

The method of claim 1, wherein the first silicalite has a pore size of about 5.4±0.2 angstroms.

Claim 4

The method of claim 1, wherein the second silicalite has a pore size greater than or equal to about 6.2 angstroms.

Claim 5

The method of claim 1, wherein the first and second silicalite are packed into separation columns.

Claim 6

The method of claim 1, wherein said mixture is injected with a mobile phase of a branched chain alkane having from about 5 to about 8 carbon atoms.

Claim 7

The method of claim 1, wherein the branched chain paraffins are displaced by backflushing the second silicalite with a displacement material of a normal alkane, or a mixture of a normal alkane and a branched chain alkane, each having from about 5 to about 8 carbon atoms.

Claim 8

The method of claim 1, wherein the normal paraffins are displaced by backflushing the first silicalite with a displacement material of a normal alkane or a mixture of a normal alkane and a branched chain alkane having from about 5 to about 8 carbon atoms.

Claim 9

The method of claim 1, further comprising regenerating the first silicalite and the second silicalite by backflushing both silicalites with an inert gas.

Claim 10

The method of claim 8, wherein the inert gas is helium, argon, or nitrogen.

Claim 11

The method of claim 8, further comprising backflushing with helium at least 50 psi for at least 20 minutes.

Claim 12

The method of claim 8, further comprising restabilizing the column by backflushing with a branched chain alkane having from about 5 to about 8 carbon atoms after regenerating with an inert gas.

Claim 13

A process for separating a mixture of saturated hydrocarbons into normal paraffins, branched chain paraffins, and cyclic paraffins, which comprises: dissolving said mixture in a solvent of iso-octane; injecting said mixture in a solvent with a mobile phase of iso-octane; contacting said mixture at retention conditions with a molecular sieve comprising a first silicalite having a pore size of about 5.4±0.2 angstroms which will retain normal paraffins, and pass through branched chain paraffins and cyclic paraffins; contacting at retention conditions the unretained mixture of branched chain paraffins and cyclic paraffins with a molecular sieve comprising a second silicalite having a pore size greater than or equal to about 6.2 angstroms which will retain branched chain paraffins and pass through cyclic paraffins, said second silicalite heated to a temperature of at least 90° C.; recovering the cyclic paraffins unretained by the second silicalite; recovering the normal paraffins by backflushing the normal paraffins from the first silicalite with octane; and recovering the branched chain paraffins by backflushing the branched chain paraffins from the second silicalite with octane.

Claim 14

A process for separating a mixture of saturated hydrocarbons into normal paraffins, branched chain paraffins, and cyclic paraffins, which comprises: dissolving said mixture in a solvent of iso-octane; injecting said mixture in a solvent with a mobile phase of iso-octane; contacting said mixture at retention conditions with a molecular sieve comprising a first silicalite having a pore size of about 5.4±0.2 angstroms which will retain normal paraffins, and pass through branched chain paraffins and cyclic paraffins; contacting at retention conditions the unretained mixture of branched chain paraffins and cyclic paraffins with a molecular sieve comprising a second silicalite having a pore size greater than or equal to about 6.2 angstroms which will retain branched chain paraffins and pass through cyclic paraffins, said second silicalite heated to a temperature of at least 90° C.; recovering the cyclic paraffins unretained by the second silicalite; recovering the normal paraffins by backflushing the normal paraffins from the first silicalite with octane; and recovering the branched chain paraffins by backflushing the branched chain paraffins from the second silicalite with octane.

Claim 15

A process for separating a mixture of saturated hydrocarbons into normal paraffins, branched chain paraffins, and cyclic paraffins, which comprises: contacting said mixture at retention conditions with a molecular sieve comprising a second silicalite having a pore size and crystal structure which will retain normal paraffins and branched chain paraffins and pass through cyclic paraffins, said second silicalite heated to a temperature of at least 70° C.; recovering the normal paraffins and branched chain paraffins by displacing the normal paraffins and branched chain paraffins from the second silicalite with a displacement material; contacting at retention conditions the mixture of normal paraffins and branched chain paraffins displaced from the second silicalite with a molecular sieve comprising a first silicalite having a pore size and crystal structure which will retain normal paraffins and pass through branched chain paraffins; recovering the cyclic paraffins unretained by the second silicalite; recovering the branched chain paraffins unretained by the first silicalite; and recovering the normal paraffins retained by the first silicalite by displacing the normal paraffins from the first silicalite with a displacement material.

Claim 16

A process for separating a mixture of saturated hydrocarbons into normal paraffins, branched chain paraffins, and cyclic paraffins, which comprises: contacting said mixture at retention conditions with a molecular sieve comprising a second silicalite having a pore size and crystal structure which will retain normal paraffins and branched chain paraffins and pass through cyclic paraffins, said second silicalite heated to a temperature of at least 70° C.; recovering the normal paraffins and branched chain paraffins by displacing the normal paraffins and branched chain paraffins from the second silicalite with a displacement material; contacting at retention conditions the mixture of normal paraffins and branched chain paraffins displaced from the second silicalite with a molecular sieve comprising a first silicalite having a pore size and crystal structure which will retain normal paraffins and pass through branched chain paraffins; recovering the cyclic paraffins unretained by the second silicalite; recovering the branched chain paraffins unretained by the first silicalite; and recovering the normal paraffins retained by the first silicalite by displacing the normal paraffins from the first silicalite with a displacement material.