Fractionation and treatment of full boiling range gasoline

• US 6,927,314 B1
• Filed: 07/17/2002
• Issued: 08/09/2005
• Est. Priority Date: 07/17/2002
• Status: Expired due to Fees

• Current Assignee: UOP Llc (Honeywell International Inc.)
• Original Assignee: UOP Llc (Honeywell International Inc.)
• Inventors: Weiszmann, Joseph A., Schultz, Michael A.
• Primary Examiner(s): Dang, Thuan D
• Application Number:
  US10/198,196
• Time in Patent Office: 1,119 Days
• Field of Search: 585/734, 585/737
• US Class Current: 585/734
• CPC Class Codes: B01D 3/141 where at least one distillation column contains at least one dividing wall
• CPC Class Codes: C10G 35/085 containing platinum group metals or compounds thereof
• CPC Class Codes: C10G 45/62 containing platinum group metals or compounds thereof
• CPC Class Codes: C10L 1/06 for spark ignition

Abstract

A process to increase the octane number of a naphtha boiling range feed stock has been developed. Using a dividing wall column, the feed stock is separated into a light fraction comprising compounds containing five carbon atoms or less, an intermediate fraction containing largely compounds having six carbon atoms, and a heavy fraction which comprises compounds containing more than six carbon atoms. The light and heavy fractions are passes to a gasoline blending pool. The intermediate fraction is isomerized to increase the octane number of the intermediate fraction and form an isomerate. The isomerate is passed to the gasoline bending pool.

Claims

1. A process for the separation and treatment of a naphtha boiling range feed stock comprising compounds containing from five to seven carbon atoms, said process comprising

a) passing the feedstock into a dividing wall column and separating the feed stock into a light fraction comprising compounds containing five carbon atoms or less, an intermediate fraction containing largely compounds having six carbon atoms, and a heavy fraction which comprises compounds containing more than six carbon atoms, wherein at least a portion of the feedstock is selected from the group consisting of FCC gasoline, coker naphtha, straight run gasoline, naptha fraction from a hydrocracking process, naphtha fraction from a thermal cracking process and mixtures thereof;

b) passing the light fraction to a gasoline blending pool;

c) treating the intermediate fraction in an isomerization zone to increase the octane number of the intermediate fraction and form an isomerate;

d) passing the heavy fraction to the gasoline blending pool; and

,

e) passing the isomerate to the gasoline bending pool.

2. The process of claim 1 wherein the intermediate fraction contains no more than about three volume percent compounds having five or less carbon atoms, and no more than about eight volume percent compounds having seven or greater carbon atoms.

3. The process of claim 1 wherein the light fraction contains no more than about 3 vol % of compounds having six or more carbon atoms.

4. The process of claim 1 wherein the heavy fraction contains no more than about 2 vol % compounds having six or less carbon atoms.

5. The process of claim 1 wherein the isomerization zone contains an isomerization catalyst and is operated at conditions effective for the isomerization of the intermediate fraction.

6. The process of claim 1 wherein the isomerization zone contains an isomerizatior catalyst comprising alumina having from 0.01 to 0.25 wt.% platinum and from 2 to 10 wt.% of a chloride component.

7. In a process for the separation of an FCC naphtha fraction wherein the FCC naphtha fraction is separated by fractional distillation yielding at least light and heavy fractions, the improvement comprises performing the fractional distillation in a dividing wall column and producing a light fraction comprising compounds containing five carbon atoms or less, an intermediate fraction containing largely compounds having six carbon atoms, and a heavy fraction which comprises compounds containing more than six carbon atoms;

passing the light fraction to a gasoline blending pool;

treating the intermediate fraction in an isomerization zone to increase the octane number of the intermediate fraction and form an isomerate;

passing the heavy fraction to the gasoline blending pool; and

, passing the isomerate to the gasoline bending pool.