Process for making xylenes and phenol from coal derived liquids

Patent metadata

Field	Value
Publication number	US-10723675-B2
Application number	US-201916593125-A
Country	US
Kind code	B2
Filing date	Oct 4, 2019
Priority date	Nov 21, 2017
Publication date	Jul 28, 2020
Grant date	Jul 28, 2020

Abstract

Processes and apparatus for making xylenes and phenol are described. Phenol and alkyl phenols are separated from coal derived liquid. The phenol is separated from the alkyl phenols. The alkyl phenols can be reacted with aromatics such as benzene and toluene to make xylenes. The xylenes and other aromatics are then separated from the phenol and alkyl phenols. Para-xylene is separated and recovered using a xylene separation process, and meta-xylene and ortho-xylene are optionally converted to para-xylene through an isomerization reaction.

First claim

What is claimed is:

1. A process for making xylenes and phenol comprising:
providing a first phenols stream comprising phenol and alkyl phenols from a coal derived liquid;
separating the first phenols stream into at least a phenol product stream comprising phenol, and a cresols stream comprising cresols in a phenols separation zone;
transalkylating the cresols stream with a first aromatics stream comprising toluene, benzene, or both in a cresols transalkylation reaction zone in the presence of a cresols transalkylating catalyst to form a first effluent stream comprising aromatics, phenol, and alkyl phenols;
separating the first effluent stream into at least a second aromatics stream comprising aromatics and a second phenols stream comprising phenol and alkyl phenols in a phenols and aromatics separation zone;
separating the second aromatics stream into at least the first aromatics stream and a first xylenes stream comprising para-xylene, ortho-xylene, and meta-xylene in an aromatics separation zone; and
introducing the second phenols stream into the phenols separation zone.

2. The process of claim 1 wherein separating the first phenols stream into at least the phenol product stream, and the cresols stream comprises separating the first phenols stream into at least the phenol product stream, the cresols stream, and a xylenols stream comprising xylenols; wherein the first aromatics stream comprises toluene; and wherein separating the second aromatics stream into at least the first aromatics stream and the first xylenes stream comprises separating the second aromatics stream into at least the toluene stream, the first xylenes stream, and a benzene stream comprising benzene; and further comprising:
transalkylating the xylenols stream with the benzene stream in a xylenols transalkylation reaction zone in the presence of a xylenols transalkylating catalyst to form a second effluent stream comprising aromatics, phenol, and alkyl phenols;
combining the first effluent stream and the second effluent stream to form a combined stream; and
wherein separating the first effluent stream into at least the second aromatics stream and the second phenols stream comprises separating the combined stream into at least the second aromatics stream and the second phenols stream.

3. The process of claim 2 further comprising separating the first xylenes stream into a para-xylene product stream comprising para-xylene and a second xylenes stream comprising ortho-xylene and meta-xylene in a xylenes separation zone.

4. The process of claim 3 further comprising:
isomerizing the second xylenes stream in a xylenes isomerization zone in the presence of a xylenes isomerization catalyst to form an isomerized xylenes stream comprising para-xylene, ortho-xylene, and meta-xylene; and
introducing the isomerized xylenes stream into the xylenes separation zone.

5. The process of claim 1 further comprising introducing a feed stream comprising aromatics to the aromatics separation zone.

6. The process of claim 1 wherein providing a first phenols stream comprises separating the phenols from the coal derived liquid using distillation, acid and caustic extraction, solvent extraction, adsorption with adsorbent, membrane separation, supercritical fluid extraction, crystallization, chelation, and eutectic reaction, and combinations thereof.

7. The process of claim 1 wherein transalkylating the cresols stream with the first aromatics stream takes place under reaction conditions comprising at least one of: a temperature in a range of 50° C. to 600° C.; a pressure in a range of 0 MPa(g) to 7.6 MPa(g); and a LHSV in a range of 0.1 to 5 hr −1 .

8. The process of claim 2 wherein transalkylating the xylenols stream with the benzene stream takes place under reaction conditions comprising at least one of: a temperature in a range of 50° C. to 600° C.; a pressure in a range of 0 MPa(g) to 7.6 MPa(g); and a LHSV in a range of 0.1 to 5 hr −1 .

9. The process of claim 4 wherein isomerizing the second xylenes stream takes place under reactions conditions comprising at least one of: a temperature in a range of 50° C. to 600° C.; a pressure in a range of 0 MPa(g) to 7.6 MPa(g); and a LHSV in a range of 0.1 to 5 hr −1 .

10. The process of claim 1 wherein the cresols transalkylation catalyst comprises at least one homogeneous acid catalyst, or at least one a heterogeneous acid catalyst.

11. A process for making xylenes and phenol comprising:
providing a first phenols stream comprising phenol and alkyl phenols from a coal derived liquid;
separating the first phenols stream into at least a phenol product stream comprising phenol, a cresols stream comprising cresols, and a xylenols stream comprising xylenols in a phenols separation zone;
transalkylating the cresols stream with a toluene stream comprising toluene in a cresols transalkylation reaction zone in the presence of a cresols transalkylating catalyst to form a first effluent stream comprising aromatics, phenol, and alkyl phenols;
transalkylating the xylenols stream with a benzene stream comprising benzene in a xylenols transalkylation reaction zone in the presence of a xylenols transalkylating catalyst to form a second effluent stream comprising aromatics, phenol, and alkyl phenols;
separating the first effluent stream and the second effluent stream into at least an aromatics stream comprising aromatics and a second phenols stream comprising phenol and alkyl phenols in a phenols and aromatics separation zone;
separating the aromatics stream into at least the benzene stream, the toluene stream, and a first xylenes stream comprising para-xylene, ortho-xylene, and meta-xylene in an aromatics separation zone; and
introducing the second phenols stream into the phenols separation zone.

12. The process of claim 11 further comprising separating the first xylenes stream into a para-xylene product stream comprising para-xylene and a second xylenes stream comprising ortho-xylene and meta-xylene in a xylenes separation zone.

13. The process of claim 12 further comprising:
isomerizing the second xylenes stream in a xylenes isomerization zone in the presence of a xylenes isomerization catalyst to form an isomerized xylenes stream comprising para-xylene, ortho-xylene, and meta-xylene; and
introducing the isomerized xylenes stream into the xylenes separation zone.

14. The process of claim 11 further comprising introducing a feed stream comprising aromatics to the aromatics separation zone.

15. The process of claim 11 wherein providing phenols from the coal derived liquid comprises separating the phenols from the coal derived liquid using distillation, acid and caustic extraction, solvent extraction, adsorption with adsorbent, membrane separation, supercritical fluid extraction, crystallization, chelation, and eutectic reaction, and combinations thereof.

16. The process of claim 11 wherein transalkylating the cresols stream with the toluene stream takes place under reactions conditions comprising at least one of: a temperature in a range of 50° C. to 600° C.; a pressure in a range of 0 MPa(g) to 7.6 MPa(g); and a LHSV in a range of 0.1 to 5 hr −1 .

17. The process of claim 11 wherein transalkylating the xylenols stream with the benzene stream takes place under reactions conditions comprising at least one of: a temperature in a range of 50° C. to 600° C.; a pressure in a range of 0 MPa(g) to 7.6 MPa(g); and a LHSV in a range of 0.1 to 5 hr −1 .

18. The process of claim 13 wherein isomerizing the second xylenes stream takes place under reactions conditions co

Assignees

• China Petroleum & Chem Corp
• Uop Llc

Inventors

• Zhou Lubo
• Zhang Shuguang

Classifications

• C07C37/74 Primary

  by distillation · CPC title

• C07C37/48

  by exchange of hydrocarbon groups, which may be substituted, from the same of other compounds, e.g. transalkylation · CPC title

• C07C7/04

  by distillation · CPC title

• C07C6/12

  of exclusively hydrocarbons containing a six-membered aromatic ring · CPC title

• C07C37/50

  by reactions decreasing the number of carbon atoms (C07C37/04, C07C37/045, C07C37/055, C07C37/08 take precedence) · CPC title