Process for making phenol and xylenes

Patent metadata

Field	Value
Publication number	US-11767280-B2
Application number	US-201917419952-A
Country	US
Kind code	B2
Filing date	Feb 4, 2019
Priority date	Feb 4, 2019
Publication date	Sep 26, 2023
Grant date	Sep 26, 2023

Abstract

Processes for making phenol and xylenes from a phenols-containing feed are described. The processes involve transalkylation of alkylphenols to form phenol and alkylbenzenes. The phenol is separated from the alkylbenzenes, and the alkylbenzenes may be separated into benzene, toluene, xylenes, and heavy alkylbenzene streams. The benzene stream may be recycled to the transalkylation reaction zone. The toluene may be sent to a disproportionation reaction zone, and the product is sent back to the aromatic separation zone. The toluene can also be recycled to the transalkylation zone. The xylenes are separated into a p-xylene stream and a mixed xylene stream comprising m-xylene and o-xylene. The mixed xylene stream is isomerized and the isomerized product is sent back to the aromatic separation zone. The heavy alkylbenzenes are dealkylated and separated, with the aromatic stream being recycled to the aromatic separation zone.

First claim

What is claimed is:

1. A process for producing one or more of phenol, and xylenes comprising:
introducing a phenols containing feed stream into a feed separation zone;
separating the phenols containing feed stream in the feed separation zone to obtain a phenol stream comprising phenol, and a crude alkylphenol stream comprising alkylphenols;
transalkylating the crude alkylphenol stream and a reactant stream comprising one or more of benzene or toluene in a transalkylation reaction zone under transalkylation reaction conditions to produce a transalkylation effluent stream comprising phenols, and alkylbenzenes;
separating the transalkylation effluent stream in a phenol separation zone into a phenol recycle stream comprising phenols, and an aromatic stream comprising benzene, toluene, xylenes, and heavy alkylbenzenes;
separating the aromatic stream in an aromatic separation zone into at least a recycle stream comprising one or more of benzene or toluene, a heavy alkylbenzene stream comprising heavy alkylbenzenes, and a mixed xylene stream comprising mixed xylenes;
separating the mixed xylene stream in a xylene separation zone into a second xylene stream comprising o-xylene and m-xylene, and a p-xylene stream comprising p-xylene;
isomerizing the second xylene stream in an isomerization reaction zone under isomerization reaction conditions to form an isomerization effluent stream comprising mixed xylenes; and
recovering one or more of the phenol stream and the p-xylene stream.

2. The process of claim 1 wherein separating the aromatic stream in the aromatic separation zone into at least the recycle stream comprising one or more of benzene or toluene, the heavy alkylbenzene stream comprising heavy alkylbenzenes, and the mixed xylene stream comprising mixed xylenes comprises separating the aromatic stream in the aromatic separation zone into at least the benzene stream comprising benzene, the heavy alkylbenzene stream comprising heavy alkylbenzenes, the mixed xylene stream comprising mixed xylenes, and a toluene stream comprising toluene, and further comprising one or more of:
disproportionating the toluene stream in a disproportionation reaction zone under disproportionation reaction conditions to form a disproportionation effluent stream comprising xylenes, and recycling the disproportionation effluent stream to the aromatic separation zone;
or
recycling the toluene stream to the transalkylation reaction zone.

3. The process of claim 1 further comprising:
dealkylating the heavy alkylbenzene stream in a dealkylation reaction zone under dealkylation reaction conditions to form a dealkylation effluent stream comprising benzene, toluene, xylenes, heavy aromatics, hydrogen and light hydrocarbons.

4. The process of claim 3 further comprising:
separating the dealkylation effluent stream in a dealkylation separation zone into a light gas stream comprising hydrogen and light hydrocarbons, and a second aromatic stream comprising benzene, toluene, xylenes, and heavy alkylbenzenes; and
recycling the second aromatic stream to the aromatic separation zone.

5. The process of claim 4 further comprising:
separating the light gas stream in a gas separation zone into hydrogen stream comprising hydrogen and a light hydrocarbon gas stream comprising C2-C4 hydrocarbons; and
recycling the hydrogen stream to the dealkylation reaction zone.

6. The process of claim 3 further comprising:
introducing a fresh hydrogen stream into the dealkylation reaction zone.

7. The process of claim 1 further comprising one or more of:
recycling the recycle stream to the transalkylation reaction zone;
or
recycling the isomerization effluent stream to the aromatic separation zone.

8. The process of claim 1 wherein the reactant stream comprises one or more of fresh benzene, recycled benzene, fresh toluene, or recycled toluene.

9. The process of claim 1 wherein separating the phenols containing feed stream comprises extracting a first fraction of the phenols containing feed stream into an extracted phenol stream comprising phenol and alkylphenols and a hydrocarbon stream.

10. The process of claim 9 further comprising:
fractionating the phenols containing feed stream into the first fraction and a second fraction comprising naphthols; and
recovering the naphthols from the second fraction.

11. The process of claim 1 further comprising:
fractionating the extracted phenol stream into at least the alkylphenol stream and the phenol stream.

12. The process of claim 1 further comprising purifying the phenol stream.

13. The process of claim 1 wherein the phenols containing feed stream comprises coal tar.

14. A process for producing one or more of phenol, and xylenes comprising:
introducing a phenols containing feed stream into a feed separation zone;
separating the phenols containing feed stream in the feed separation zone to obtain a phenol stream comprising phenol and a crude alkylphenol stream comprising alkylphenols;
transalkylating the crude alkylphenol stream and a reactant stream comprising one or more of benzene or toluene in a transalkylation reaction zone under transalkylation reaction conditions to produce a transalkylation effluent stream comprising phenols, and alkylbenzenes;
separating the transalkylation effluent stream in a phenol separation zone into a phenol recycle stream comprising phenol, and an aromatic stream comprising benzene, toluene, xylenes, and heavy alkylbenzenes;
separating the aromatic stream in an aromatic separation zone into at least a recycle stream comprising benzene, a toluene stream comprising toluene, a mixed xylene stream comprising mixed xylenes, and a heavy alkylbenzene stream comprising heavy alkylbenzenes;
disproportionating the toluene stream in a disproportionation reaction zone under disproportionation reaction conditions to form a disproportionation effluent stream comprising xylenes;
separating the mixed xylene stream in a xylene separation zone into a second xylene stream comprising o-xylene and m-xylene, and a p-xylene stream comprising p-xylene;
isomerizing the second xylene stream in an isomerization reaction zone under isomerization reaction conditions to form an isomerization effluent stream comprising mixed xylenes;
dealkylating the heavy alkylbenzene stream in a dealkylation reaction zone under dealkylation reaction conditions to form a dealkylation effluent stream comprising benzene, toluene, xylenes, heavy aromatics, hydrogen and light hydrocarbons; and
recovering one or more of the phenol stream and the p-xylene stream.

15. The process of claim 14 further comprising one or more of:
recycling the recycle stream to the transalkylation reaction zone;
recycling the disproportionation effluent stream to the aromatic separation zone; or
recycling the isomerized xylene stream to the aromatic separation zone.

16. The process of claim 14 further comprising:
separating the dealkylation effluent stream in a dealkylation separation zone into a light gas stream comprising hydrogen and light hydrocarbons, and a second aromatic stream comprising benzene, toluene, xylenes, and heavy aromatics; and
recycling the second aromatic stream to the aromatic separation zone.

17. The process of claim 16 further comprising:
separating the light gas stream in a gas separation zone into hydrogen stream comprising hydrogen and a light hydrocarbon gas stream comprising C2-C4 hydrocarbon stream; and
recycling the hydrogen stream to the dealkylation reaction zone.

18. The process of claim 14 wherein separating the

Assignees

• China Petroleum & Chem Corp
• Uop Llc

Inventors

• Zhang Shuguang
• Zhou Lubo

Classifications

• C07C37/50 Primary

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

• C07C6/126

  of more than one hydrocarbon · CPC title

• C07C37/72

  by liquid-liquid treatment · CPC title

• C07C5/2729 Primary

  Changing the branching point of an open chain or the point of substitution on a ring · CPC title