Paraxylene production process and apparatus

Patent metadata

Field	Value
Publication number	US-9457292-B2
Application number	US-201314035660-A
Country	US
Kind code	B2
Filing date	Sep 24, 2013
Priority date	Jun 25, 2010
Publication date	Oct 4, 2016
Grant date	Oct 4, 2016

Abstract

The invention concerns a process for the production of paraxylene and an apparatus suitable for said process. The process separates the overhead from a xylenes re-run into a xylene-rich stream and a xylene-lean stream. The xylene-lean stream is isomerized under conditions such that the xylenes are in the liquid phase.

First claim

What is claimed is:

1. A xylene loop system comprising a distillation column fluidly connected with a paraxylene recovery unit selected from a crystallization unit and an adsorptive separation unit, wherein said paraxylene recovery unit is fluidly connected with a first xylenes isomerization unit, the improvement comprising:
inserting a subsystem between said distillation column and said paraxylene recovery unit, fluidly connected to said distillation column and said paraxylene recovery unit, said subsystem comprising a separation unit to effectively separate paraxylene and ethylbenzene from metaxylene and orthoxylene, selected from an adsorption unit, a membrane unit, and an extraction unit, and inserting a second xylenes isomerization unit between said subsystem and said distillation column, said second xylenes isomerization unit fluidly connected with said subsystem and said distillation column.

2. The system according to claim 1 , wherein said first xylenes isomerization unit is a vapor phase xylenes isomerization unit and said second xylenes isomerization unit is a liquid phase isomerization unit.

3. The system according to claim 2 , wherein said second xylenes isomerization unit comprises a ZSM-5 catalyst characterized by one or more of the following characteristics:
the ZSM-5 is in the proton form (HZSM-5);
the ZSM-5 has a crystal size of less than 0.1 microns;
the ZSM-5 has a mesoporous surface area (MSA) greater than 45 m 2 /g;
the ZSM-5 has a zeolite surface area (ZSA) to mesoporous surface area (MSA) ratio of less than 9;
the ZSM-5 has a silica to alumina weight ratio in the range of 20 to 50.

4. The system according to claim 3 , wherein said ZSM-5 catalyst is characterized by all of said characteristics.

Assignees

• Exxonmobil Chemical Patents Inc

Inventors

• Ou John Di-Yi

Classifications

• B01J35/45

  Nanoparticles · CPC title

• C07C5/2737

  with crystalline alumino-silicates, e.g. molecular sieves · CPC title

• B01J2219/00006

  Large-scale industrial plants · CPC title

• B01J35/023

  Operations & Transport · mapped topic

• C07C2529/40

  of the pentasil type, e.g. types ZSM-5, ZSM-8 or ZSM-11 · CPC title