Coating to inhibit fouling of reactors for cumene hydroperoxide cleavage

Patent metadata

Field	Value
Publication number	US-10047030-B2
Application number	US-201515501184-A
Country	US
Kind code	B2
Filing date	Aug 7, 2015
Priority date	Aug 8, 2014
Publication date	Aug 14, 2018
Grant date	Aug 14, 2018

Abstract

The disclosure concerns methods comprising forming a phenol and acetone mixture from decomposition of a cumene hydroperoxide or a phenol, acetone, and AMS from the decomposition of a mixture containing dicumyl peroxide in a system comprising one or more reactors where at least a portion of an inner surface of the one or more reactors has a polymer coating and wherein the coating inhibits build-up of a fouling precipitate on the coated inner surface of the one or more reactors as compared to such build-up in the absence of the coating.

First claim

What is claimed:

1. A method comprising:
(a) decomposing a cumene hydroperoxide to form phenol and acetone and to react cumene hydroperoxide with dimethylbenzyl alcohol in the presence of a catalyst mixture to form a dicumyl peroxide mixture in a first stage, wherein the first stage occurs in a first system comprising a reactor; and
(b) forming a phenol, acetone, and α-methylstyrene mixture from decomposition of the dicumyl peroxide mixture formed in the first stage in a second stage, wherein the second stage occurs in a second system comprising a reactor;
wherein the first and the second systems are connected in series,
wherein the reactor of the second system has a polymer coating on at least a portion of an inner surface of the reactor,
wherein a surface energy of the coating is from about 19 to about 31 mN/m, and
wherein the coating inhibits build-up of a fouling precipitate on the coated inner surface of the reactor of the second system as compared to such build-up in the absence of the coating.

2. The method of claim 1 , wherein the reactor comprise a stainless steel tubing, a pipe, a pre-heater, a heat exchanger, a calorimeter, or any combination thereof.

3. The method of claim 1 , wherein substantially no fouling precipitate is present on the inner surface of the reactor in the second stage after an operation time of about 80 hours to about 16,000 hours.

4. The method of claim 1 , wherein the fouling precipitate comprises an insoluble phenol-aldehyde resin.

5. The method of claim 1 , wherein the second stage is carried out at a temperature from about 90° C. to about 160° C.

6. The method of claim 1 , wherein the second stage is carried out at a pressure from about 5 to about 200 psi.

7. The method of claim 1 , wherein the coating withstands exposure to pH values from about 1 to about 14 with substantially no cracking, swelling, pitting, or decomposition.

8. The method of claim 1 , wherein the coating withstands exposure to a solvent with substantially no swelling.

9. The method of claim 8 , wherein the solvent comprises water, phenol alpha methyl styrene, dimethyl benzyl alcohol, cumene hydroperoxide, dicumyl peroxide, acetophenone, acetone, or any combination thereof.

10. The method of claim 1 , wherein the coating has substantially no reactivity towards phenol.

11. The method of claim 1 , wherein the coating is formed as a film, mechanical attachment of a “liner”, by a spray coating technique, solution deposition, chemical vapor deposition, plasma deposition, electron beam, or any combination thereof.

12. A method comprising
forming a phenol, acetone, and α-methylstyrene mixture from decomposition of a dicumyl peroxide mixture in a system comprising reactor where at least a portion of an inner surface of the reactor has a polymer coating; wherein a surface energy of the coating is from about 19 to about 31 mN/m; and
wherein the coating inhibits build-up of a fouling precipitate on the coated inner surface of the reactor as compared to such build-up in the absence of the coating.

13. A method comprising:
applying a coating to at least a portion of an inner surface of reactor to form a coated surface wherein the coating minimizes chemical and physical interactions with phenol molecules; and
wherein the reactor are used in a two stage formation of phenol and acetone from cumene hydroperoxide mixture, and substantially no fouling precipitates are present on the coated surface at the second stage during an operation time from about 80 hours to about 16000 hours.

14. The method of claim 1 , wherein the coating comprises a fluorocarbon resin, polypropylene resin, polyethylene resin, fluoro-chlorocarbon resin, fluorinated ethers or any combination thereof.

15. The method of claim 14 , wherein the fluorocarbon resin comprises polytetrafluoroethylene, copolymer of ethylene and chlorotrifluoroethylene, perfluoroalkoxy alkanes, or a combination thereof.

16. The method of claim 1 , wherein the coating has a thickness from about 500 to about 10,000 μm.

17. A system comprising reactor comprising an inner surface, wherein at least a portion of the inner surface has a coating, wherein the coating has a surface energy such that chemical and physical interactions with formed phenol are minimized, wherein a surface energy of the coating is from about 19 to about 31 mN/m, and wherein the system is used for a high throughput two stage method of formation of phenol and acetone from cumene hydroperoxide mixture.

18. The method of claim 1 , wherein the coating has a thickness from about 500 to about 1,000 μm.

Assignees

• Sabic Global Technologies Bv

Inventors

• Nelson Mark Erik
• Dykman Arkady Samuilovich
• Zinenkov Andrey Vladimirovich

Classifications

• B01J2219/00783

  Laminate assemblies, i.e. the reactor comprising a stack of plates · CPC title

• B01J2219/0099

  Cleaning · CPC title

• C07C45/53 Primary

  of hydroperoxides · CPC title

• C09D5/1662

  Synthetic film-forming substance · CPC title

• B01J19/0093 Primary

  Microreactors, e.g. miniaturised or microfabricated reactors (laboratory containers with capillary fluid transport in microfabricated channels or chambers B01L3/5027) · CPC title