# US 5,326,928 A · Separation of aliphatic paraffins by adsorption

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- Number: US 5,326,928 A
- Document ID: US5326928A
- Status: Granted
- Kind: A
- Application number: 08/026,791
- Filed: 1993-03-05
- Granted: 1994-07-05
- Earliest claimed: 1992-03-06
- Assignees: Institute Francais du Petrole
- Inventors: Eric Benazzi; Gerard Hotier; Jean-Marie Basset; Agnes Choplin; Albert Theolier; Christophe Nedez
- Web page: https://patentgrep.com/patent/US5326928A

## CPC

- B01J 20/186: {Chemical treatments in view of modifying the properties of the sieve, e.g. increasing the stability or the activity, also decreasing the activity}
- B01J 20/223: {containing metals, e.g. organo-metallic compounds, coordination complexes}
- B01J 20/3204: {Inorganic carriers, supports or substrates}
- B01J 20/3265: {with an organic functional group containing a metal, e.g. a metal affinity ligand}
- C07C 7/13: by molecular-sieve technique
- B01J: CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- C07C: ACYCLIC OR CARBOCYCLIC COMPOUNDS

## Abstract

For the at least partial separation of aliphatic paraffins into at least one effluent comprising the least branched paraffins and at least one effluent comprising the most branched paraffins, use is made of at least one adsorbent bed comprising at least one grafted microporous solid. A preferred use of the invention relates to the treatment of a charge obtained from an isomerization zone, whereby at least one adsorbent bed makes it possible to separate the charge into a first effluent comprising the normal paraffins and a second effluent, and at least one adsorbent bed on which passes the second effluent, comprising at least one grafted microporous solid, making it possible to obtain a third effluent comprising the monomethyl branched paraffins and a fourth effluent comprising the polymethyl branched paraffins.

## Claims

### Claim 1

A process for separating aliphatic paraffins having varying degrees of branching in a hydrocarbon charge containing molecules of 5 to 14 carbon atoms into at least one first effluent comprising less branched paraffins and at least one second effluent comprising more branched paraffins, said process comprising contacting the hydrocarbon charge with at least one adsorbent bed comprising at least one microporous solid having grafted in the pores thereof an organometallic compound of a quantity and shape sufficient to yield pores selective for entry of the less branched paraffins but not the more branched paraffins.

### Claim 2 (depends on 1)

Process according to claim 1, wherein the solid is a grafted zeolite.

### Claim 3 (depends on 1)

Process according to claim 1, wherein said solid is a grafted mordenite.

### Claim 4 (depends on 1)

A process according to claim 1, wherein grafting takes place by the chemical reaction of a organometallic compound on the solid, said compound having the formula MeR.sup.1 R.sup.2 R.sup.3 R.sup.4, Me being an element selected from the group consisting of elements of groups of IIA, IIB, IIIA, IVA and VA of the periodic classification of elements and R.sup.i, i being equal to 1, 2, 3 or 4, being hydrogen or an organic radical, with the proviso that at least one R group is an organic radical.

### Claim 5 (depends on 4)

Process according to claim 4, wherein the element Me is tin.

### Claim 6 (depends on 1)

A process according to claim 1, wherein the charge mainly comprises aliphatic paraffins containing 5 to 6 carbon atoms per molecule and wherein the less branched paraffins mainly comprise normal paraffins, said process further comprising withdrawing the effluent comprising the more branched paraffins and contacting said effluent containing the more branched paraffins with another adsorbent bed so as to separate the more branched paraffins into a third effluent mainly comprising monoethyl branched paraffins and a fourth effluent mainly comprising polymethyl branched paraffins.

### Claim 7 (depends on 6)

A process according to claim 6, wherein the charge if obtained from an isomerization.

### Claim 8 (depends on 6)

Process according to claim 6, wherein the first and third effluents are recycled to said isomerization zone.