Method for producing aromatic hydrocarbons

Patent metadata

Field	Value
Publication number	US-9446997-B2
Application number	US-201113822487-A
Country	US
Kind code	B2
Filing date	Sep 14, 2011
Priority date	Sep 14, 2010
Publication date	Sep 20, 2016
Grant date	Sep 20, 2016

Abstract

Provided is a method for producing aromatic hydrocarbons, by which a feedstock containing a hydrogenation-treated oil of a thermally cracked heavy oil obtainable from an ethylene production apparatus is brought into contact with a catalyst for monocyclic aromatic hydrocarbon production containing a crystalline aluminosilicate, and thereby aromatic hydrocarbons are produced. A raw material having an end point of the distillation characteristics of 400° C. or lower is used as the feedstock. The contact between the feedstock and the catalyst for monocyclic aromatic hydrocarbon production is carried out at a pressure of 0.1 MPaG to 1.5 MPaG.

First claim

The invention claimed is:

1. A method for producing BTX (benzene, toluene, and xylenes), the method comprising the steps of:
thermally cracking a raw material to produce an effluent comprising heavy oil and ethylene;
separating the effluent to obtain the heavy oil;
hydrogenating the heavy oil to obtain a feedstock comprising 8 mass % or less of polycyclic aromatic hydrocarbons with two or more rings and 50 mass % or more of monocyclic aromatic hydrocarbons, wherein the feedstock has a distillation end point temperature of 400° C. or lower; and
contacting the feedstock with a cracking reforming catalyst comprising a crystalline aluminosilicate to produce BTX,
wherein the contacting of the feedstock with the cracking reforming catalyst is carried out under a pressure of 0.1 MPaG to 1.5 MPaG and a contact time between the feedstock and the catalyst is within a range of 5 seconds to 300 seconds.

2. The method according to claim 1 , wherein the feedstock further comprises a content of hydrocarbons having an indane skeleton and an indene skeleton of 5 mass % or more.

3. The method according to claim 1 , wherein:
the step of separating the effluent comprises separating by distillation the effluent to obtain the heavy oil; and
the step of hydrogenating the heavy oil is carried out in the presence of hydrogen and a hydrogenation catalyst under a hydrogen partial pressure of 0.7 MPa to 20 MPa, a LHSV of 0.05 h-1 to 2 h-1, a reaction temperature of 200° C. to 450° C., and a hydrogen/oil ratio of 100 NL/L to 2000 NL/L.

4. The method according to claim 3 , wherein the hydrogenation catalyst comprises at least one metal selected from the metals of Group 6 of the Periodic Table of Elements in an amount of 10 mass % to 30 mass %, and at least one metal selected from the metals of Group 8 to Group 10 of the Periodic Table of Elements in an amount of 1 mass % to 7 mass %, relative to the total catalyst mass, supported on an inorganic carrier containing aluminum oxide.

5. The method according to claim 4 , wherein the at least one metal selected from the metals of Group 6 of the Periodic Table of Elements is molybdenum and/or tungsten, and the at least one metal selected from the metals of Group 8 to Group 10 of the Periodic Table of Elements is cobalt and/or nickel.

6. The method according to claim 1 , wherein:
the step of hydrogenating the heavy oil is carried out in the presence of hydrogen and a hydrogenation catalyst under a hydrogen partial pressure of 0.7 MPa to 20 MPa, a LHSV of 0.05 h-1 to 2 h-1, a reaction temperature of 200° C. to 450° C., and a hydrogen/oil ratio of 100 NL/L to 2000 NL/L; and
separating by distillation the hydrogenated heavy oil to obtain the feedstock.

7. The method according to claim 6 , wherein the hydrogenation catalyst comprises at least one metal selected from the metals of Group 6 of the Periodic Table of Elements in an amount of 10 mass % to 30 mass %, and at least one metal selected from the metals of Group 8 to Group 10 of the Periodic Table of Elements in an amount of 1 mass % to 7 mass %, relative to the total catalyst mass, supported on an inorganic carrier containing aluminum oxide.

8. The method according to claim 7 , wherein the at least one metal selected from the metals of Group 4 of the Periodic Table of Elements is molybdenum and/or tungsten, and the at least one metal selected from the metals of Group 8 to Group 10 of the Periodic Table of Elements is cobalt and/or nickel.

9. The method according to claim 1 , wherein the cracking reforming catalyst contains gallium and/or zinc.

10. The method according to claim 1 , wherein the cracking reforming catalyst contains phosphorus.

11. The method according to claim 1 , wherein the feedstock is brought into contact with the cracking reforming catalyst in the absence of molecular hydrogen.

Assignees

• Yanagawa Shinichiro
• Ida Ryoji
• Kobayashi Masahide
• Jx Nippon Oil & Energy Corp

Inventors

• Yanagawa Shinichiro
• Ida Ryoji
• Kobayashi Masahide

Classifications

• B01J37/0009 Primary

  Use of binding agents; Moulding; Pressing; Powdering; Granulating; Addition of materials ameliorating the mechanical properties of the product catalyst · CPC title

• B01J23/882

  and cobalt · CPC title

• Y02P20/52

  using catalysts, e.g. selective catalysts · CPC title

• C10G69/04

  including at least one step of catalytic cracking in the absence of hydrogen · CPC title

• C10G2300/301

  Boiling range · CPC title