Method for carrying out a chemical reaction in an upflow reactor

Patent metadata

Field	Value
Publication number	US-2025058309-A1
Application number	US-202218721057-A
Country	US
Kind code	A1
Filing date	Dec 12, 2022
Priority date	Dec 17, 2021
Publication date	Feb 20, 2025
Grant date	—

Abstract

The present invention relates to a method for carrying out a catalysed chemical reaction using one or more liquid reactants, preferably acetone and phenol to form bisphenol A, in an upflow reactor comprising feeding at least a portion of said reactants to a bottom section of the reactor positioned below a flow distributor plate, passing said portion through the flow distributor plate, passing said portion through a layer of inert particles positioned above and preferably in contact with said flow distributor plate, passing said portion through a catalyst layer comprising a particulate catalyst, said catalyst layer being positioned above and in contact with said layer of inert particles, wherein the reactants react to form a product stream, collecting said product stream via collecting means positioned above said catalyst layer. The invention also relates to a reactor assembly. The catalyst is a core-shell catalyst which is manufactured by graft polymerizing aromatic vinyl compounds onto the hydroxylated and functionalized core particles, followed by sulfonation.

First claim

1 . Method for the manufacture of a core-shell catalyst comprising the steps of
a) providing core particles, b) functionalizing at least part of the surface of said core particles with a functionalizing agent thereby forming functionalized core particles, c) graft polymerizing one or more aromatic vinyl compounds onto the functionalized core particles thereby forming core-shell particles wherein the core is comprised of said core particles and the shell is comprised of graft polymerized aromatic vinyl compounds, and d) activating the shell, wherein prior to step b) the core particles are hydroxylated.

2 . The method of claim 1 , wherein the core particles have an average particle diameter of 200-2000 μm, as determined with microscopy in accordance with the method described in the description.

3 . The method of claim 1 , wherein the functionalizing agent comprises at least one functional group for reacting with the core particle and at least one functional group for reacting with said one or more aromatic vinyl compounds.

4 . The method of claim 1 , wherein the functionalizing agent is a silane represented by the following general formula (1),

wherein,
R1, R2 and R3 may be the same or different, and are independently selected from the group consisting of hydrogen, halogen, alkyl, haloalkyl, alkylene, alkynyl, aromatic groups, substituted aromatic groups, heteroaromatic groups, ester, ether, allyl, alkoxy, alkynoxy, aryloxy, acyloxy, acrylate, methacrylate, isocyanate, urethane, carbamate, epoxy, carboxylic acid, carboxylic acid anhydride, carboxylate, hydroxy, thiol, amine, aminoalkyl, arylammo and amide provided that at least one of R1, R2 and R3 is an acrylate, allyl, alkoxy, alkynoxy, aryloxy, acyloxy, methacrylate, isocyanate, urethane, carbamate, epoxy, carboxylic acid, carboxylic acid anhydride, carboxylate, hydroxy, thiol, amine, aminoalkyl, arylammo and amide,
R4 is a functional group for reacting with the said aromatic vinyl compounds, and
n is between 0-20.

5 . The method of claim 1 , wherein the aromatic vinyl compound comprises styrene and optionally a substituted styrene.

6 . The method of claim 1 , wherein the activating step comprises sulfonating at least part of the graft polymerized aromatic vinyl compound using a sulfonating agent.

7 . The method of claim 1 , wherein the shell has a thickness from 10-500 μm.

8 . Method for carrying out a catalysed chemical reaction using one or more liquid reactants in an upflow reactor comprising:
feeding at least a portion of said reactants to a bottom section of the reactor positioned below a flow distributor plate, passing said portion through the flow distributor plate, passing said portion through a layer of inert particles positioned above said flow distributor plate, passing said portion through a catalyst layer comprising a particulate catalyst, said catalyst layer being positioned above and in contact with said layer of inert particles, wherein the reactants react to form a product stream, collecting said product stream via collecting means positioned above said catalyst layer, wherein, the upflow reactor is operated at a weight hourly space velocity of at least 1.5, and the inert particles have a density of at least 2000 kg/m3 and an average particle size of from 500 to 5000 μm, and the particulate catalyst comprises or consists of a core-shell catalyst obtained or obtainable by the method of claim 1 , the height of the layer of inert particles is at least 40 times the average particle size of the inert particles.

9 . The method of claim 8 , wherein the catalysed chemical reaction comprises the reaction between phenol and ketone.

10 . The method of claim 8 , wherein the inert particles comprise, essentially consist or consist of particles selected from sand particles, glass particles, ceramic particles, diatomaceous earth particles, inert metal particles and combinations of at least two hereof.

11 . The method of claim 8 , wherein the distributor plate is a slotted plate with a plurality of openings having a size smaller than the average particle size of the inert particles.

12 . The method of claim 1 , wherein the height of the layer of inert particles is at least 2.0 cm.

13 . A reactor assembly for carrying out a catalysed chemical reaction using one or more liquid reactants in upflow comprising:
feeding means for feeding at least a portion of said reactants to a bottom section of the reactor, said feeding means being positioned below a flow distributor plate, layer of inert particles positioned above said flow distributor plate, a catalyst layer comprising a particulate catalyst positioned above and in contact with said layer of inert particles, collecting means positioned above said catalyst layer for collecting a product stream from the reactor, wherein, the inert particles have a density of at least 2000 kg/m3 and an average particle size of from 500 to 5000 μm, and the particulate catalyst comprises or consists of a core-shell catalyst obtained or obtainable by the method of claim 1 , the height of the layer of inert particles is at least 40 times the average particle size of the inert particles.

Assignees

• Sabic Global Technologies Bv

Inventors

• Sen Suman Kumar
• Patil Prashant
• Daliparthi Surya Prakasa Rao
• Dhar Dwairath
• Mondal Amit Kumar
• Eijsbouts Paulus Johannes Maria
• Van Der Heijden Rudolf Martinus Petrus
• Schoenmakers Gert-Jan
• Murukutla Mouli

Classifications

• B01J35/53 Primary

  with a core-shell structure · CPC title

• B01J35/397

  Egg shell like · CPC title

• B01J2235/30

  Scanning electron microscopy; Transmission electron microscopy · CPC title

• B01J35/45

  Nanoparticles · CPC title

• B01J35/31

  Density · CPC title