Process for preparing methacrolein

Patent metadata

Field	Value
Publication number	US-10723685-B2
Application number	US-201816615841-A
Country	US
Kind code	B2
Filing date	May 24, 2018
Priority date	May 25, 2017
Publication date	Jul 28, 2020
Grant date	Jul 28, 2020

Abstract

Provided is a process for preparing methacrolein which maximizes capture of methanol. Also provided are processes for producing methacrylic acid and methyl methacrylate.

First claim

What is claimed is:

1. A process for preparing methacrolein comprising:
(a) mixing water and an amine-acid catalyst to provide a catalyst stream;
(b) sending the catalyst stream and a reaction stream comprising propionaldehyde, formaldehyde, and methanol to a reactor to produce a first intermediate stream comprising methacrolein, methanol, and at least 8 weight % water;
(c) providing the first intermediate stream to a first phase separator to produce (i) a first aqueous phase comprising methacrolein, methanol, amine-acid catalyst, and at least 65 weight % water, and (ii) a first organic phase comprising water, at least 85 weight % methacrolein, and less than 5 weight % methanol;
(d) distilling the first aqueous phase in a first distillation column to produce (i) a second intermediate stream comprising methacrolein, water, and less than 60 weight % methanol, (ii) a bottoms stream comprising amine-acid catalyst, and (iii) a side draw stream comprising methanol and water;
(e) providing the second intermediate stream and water to a second phase separator to produce (i) a second organic phase comprising methacrolein, water, and less than 55 weight % methanol, and (ii) a second aqueous phase;
(f) distilling the first organic phase and the second organic phase in a second distillation column to produce (i) a third intermediate stream comprising methacrolein and less than 2 weight % methanol, and (ii) an overhead stream;
(g) distilling the third intermediate stream in a third distillation column to produce (i) a product stream comprising methacrolein and water in a combined amount of at least 97 weight %, less than 2 weight % methanol, and less than 1 weight % of impurities comprising one or more of acetic acid, propionic acid, methacrolein dimer, and 2-methyl-2-pentenal, and (ii) a waste stream;
(h) recycling at least part of the overhead stream to the first phase separator; and
(i) recycling at least part of the bottoms stream to the catalyst stream.

2. The process of claim 1 , wherein the propionaldehyde is produced by contacting ethylene with CO and H 2 in the presence of a hydroformylation catalyst.

3. The process of claim 1 , further comprising providing at least part of the product stream to a process comprising contacting the methacrolein with an oxygen-containing gas in the presence of an oxidation catalyst to produce methacrylic acid.

4. The process of claim 3 , further comprising providing the methacrylic acid to a process comprising contacting the methacrylic acid with methanol in the presence of an esterification catalyst to produce methyl methacrylate.

5. The process of claim 2 , further comprising providing at least part of the product stream to a process comprising contacting the methacrolein with an oxygen-containing gas in the presence of an oxidation catalyst to produce methacrylic acid.

6. The process of claim 5 , further comprising providing the methacrylic acid to a process comprising contacting the methacrylic acid with methanol in the presence of an esterification catalyst to produce methyl methacrylate.

7. The process of claim 1 , wherein the first phase separator is operated at a temperature of less than 15° C.

8. The process of claim 1 , wherein the second phase separator is operated at a temperature of less than 25° C.

9. The process of claim 1 , wherein the ratio of the water entering the second phase separator to the second intermediate stream entering the second phase separator is from 1:10 to 100:1.

10. The process of claim 1 , wherein the ratio of the third intermediate stream exiting the second distillation column to the combined amount of first organic phase and the second organic phase entering the second distillation column is from 1:10 to 9:10.

Assignees

• Rohm & Haas

Inventors

• Chakrabarti Reetam
• Krapchetov Dmitry A
• Silvano Mark A
• Xu Jinsuo

Classifications

• Y02P30/40

  Ethylene production · CPC title

• Y02P30/20

  using bio-feedstock · CPC title

• C07C51/252

  of propene, butenes, acrolein or methacrolein · CPC title

• C07C45/82

  by distillation · CPC title

• C07C45/78

  Separation; Purification; Stabilisation; Use of additives · CPC title