Method of producing aromatic hydrocarbons

Patent metadata

Field	Value
Publication number	US-11976039-B2
Application number	US-202017430302-A
Country	US
Kind code	B2
Filing date	Nov 9, 2020
Priority date	Jun 16, 2020
Publication date	May 7, 2024
Grant date	May 7, 2024

Abstract

Method of producing aromatic hydrocarbons including: supplying a raw material stream to a C6 separation column, supplying an upper discharge stream from the C6 separation column to a first gasoline hydrogenation unit, and supplying a lower discharge stream from the C6 separation column to a C7 separation column; supplying an upper discharge stream from the C7 separation column to a hydrodealkylation reaction unit and supplying a lower discharge stream from the C7 separation column to a C8 separation column; separating benzene from discharged streams from the first gasoline hydrogenation unit and the hydrodealkylation reaction unit; removing a lower discharge stream from the C8 separation column and supplying an upper discharge stream from the C8 separation column to a second extractive distillation column; and separating styrene from a lower discharge stream of the second extractive distillation column and separating xylene from an upper discharge stream of the second extractive distillation column.

First claim

The invention claimed is:

1. A method of producing aromatic hydrocarbons, the method comprising:
a step of supplying a first raw material stream to a C6 separation column, supplying an upper discharge stream from the C6 separation column to a first gasoline hydrogenation unit, and supplying a lower discharge stream from the C6 separation column to a C7 separation column;
a step of supplying an upper discharge stream from the C7 separation column to a hydrodealkylation reaction unit and supplying a lower discharge stream from the C7 separation column to a C8 separation column;
a step of separating benzene from a discharge stream of the first gasoline hydrogenation unit and a discharge stream of the hydrodealkylation reaction unit;
a step of removing a lower discharge stream from the C8 separation column and supplying an upper discharge stream from the C8 separation column to a second extractive distillation column; and
a step of separating styrene from a lower discharge stream of the second extractive distillation column and separating xylene from an upper discharge stream of the second extractive distillation column,
wherein the first gasoline hydrogenation unit is separately supplied with a second raw material stream including a C5 hydrocarbon and a C6 hydrocarbon,
wherein the second raw material stream supplied to the first gasoline hydrogenation unit is different from the first raw material stream and does not include styrene; and
wherein the first raw material stream includes C5 to C10 hydrocarbons.

2. The method of producing aromatic hydrocarbons of claim 1 , wherein in the step of separating benzene, the discharge stream from the first gasoline hydrogenation unit is supplied to a first extractive distillation column, and benzene is separated from a lower discharge stream of the first extractive distillation column.

3. The method of producing aromatic hydrocarbons of claim 2 , wherein the lower discharge stream from the first extractive distillation column and the discharge stream from the hydrodealkylation reaction unit form a mixed stream, and benzene is separated from the mixed stream.

4. The method of producing aromatic hydrocarbons of claim 1 , wherein in the step of separating xylene, the upper discharge stream of the second extractive distillation column is supplied to a second gasoline hydrogenation unit, and xylene is separated from a discharge stream of the second gasoline hydrogenation unit.

5. The method of producing aromatic hydrocarbons of claim 4 , wherein the second gasoline hydrogenation unit includes a gasoline hydrogenation reactor, and
wherein an operation temperature of the gasoline hydrogenation reactor is 250° C. to 350° C.

6. The method of producing aromatic hydrocarbons of claim 1 , wherein the lower discharge stream from the C8 separation column includes C9+ hydrocarbons.

Assignees

• Lg Chemical Ltd

Inventors

• Hwang Sung June
• Kim Tae Woo
• Lee Sung Kyu

Classifications

• C07C7/167 Primary

  for removal of compounds containing a triple carbon-to-carbon bond · CPC title

• C07C7/08 Primary

  by extractive distillation · CPC title

• C07C15/04

  Benzene · CPC title

• C07C15/08

  Xylenes · CPC title

• C07C15/46

  Styrene; Ring-alkylated styrenes · CPC title