Process Comprising Two Reaction Zones And Apparatus Therefore

Patent metadata

Field	Value
Publication number	US-2017173548-A1
Application number	US-201515116089-A
Country	US
Kind code	A1
Filing date	Jan 5, 2015
Priority date	Feb 17, 2014
Publication date	Jun 22, 2017
Grant date	—

Abstract

In a process for carrying out a chemical reaction gaseous reactants are supplied to a first reaction zone including a first catalyst having a first particle equivalent diameter. The first reaction zone is operated such that when the reactants are contacted with the first catalyst a portion of the reactants is converted to the desired product. An intermediate stream of unreacted reactants and the desired product is removed and passed to a second reaction zone including a tubular reactor. Tubes of the reactor are catalyst carriers containing a second catalyst having a second particle equivalent diameter smaller than the first particle equivalent diameter. The second reaction zone is operated such that when the unreacted reactants are contacted with the second catalyst, at least some of the unreacted reactants are converted to the desired product. A product stream is then recovered. Apparatus for carrying out the process is also described.

First claim

1 . A process for carrying out a chemical reaction comprising:
supplying gaseous reactants to a first reaction zone comprising a first catalyst having a first catalyst particle equivalent diameter; operating said first reaction zone such that when the reactants are contacted with the first catalyst a portion of the reactants are converted to a desired product; removing an intermediate stream comprising unreacted reactants and the desired product and passing the intermediate stream to a second reaction zone comprising a tubular reactor which comprises tubes, wherein said tubes comprise a plurality of catalyst carriers containing a second catalyst having a second catalyst particle equivalent diameter which is smaller than the first catalyst particle equivalent diameter of the first catalyst; operating said second reaction zone such that when the unreacted reactants in the intermediate stream from the first reaction zone are contacted with the second catalyst, at least some of the unreacted reactants are converted to the desired product; and recovering a product stream,
wherein each catalyst carrier comprises:
an annular container for holding the second catalyst in use, said container having a perforated inner wall defining a tube, a perforated outer wall, a top surface closing the annular container and a bottom surface closing the annular container;
a surface closing the bottom of said tube formed by the inner wall of the annular container;
a skirt extending upwardly from the perforated outer wall of the annular container from a position at or near the bottom surface of said container to a position below the location of a seal;
and a seal located at or near the top surface and extending from the container by a distance which extends beyond an outer surface of the skirt.

2 . (canceled)

3 . (canceled)

4 . (canceled)

5 . The process according to claim 1 wherein interstage cooling is provided between the first and second reaction zones.

6 . The process according to claim 1 wherein the first reaction zone comprises a tubular fixed bed reactor.

7 . (canceled)

8 . The process according to claim 6 wherein the first and second zones are contiguous and each tube is packed with conventional catalyst in the first zone and with catalyst loaded into catalyst carriers in the second zone.

9 . (canceled)

10 . (canceled)

11 . The process according to claim 1 wherein the first catalyst particle equivalent diameter is from about 1 mm to about 6 mm.

12 . (canceled)

13 . The process according to claim 1 wherein the second catalyst particle equivalent diameter is from about 0.1 mm to about 3 mm.

14 . The process according to claim 1 wherein a portion of the product stream is recycled to at least one of the first and second reaction zones.

15 . The process according to claim 1 wherein at least one reactant is one of a) added to the second reaction zone, and b) added to the intermediate stream before it is added to the second reaction zone.

16 . (canceled)

17 . (canceled)

18 . The process according to claim 1 wherein the process is for the production of formaldehyde from methanol or methylal.

19 . The process according to claim 18 wherein the first catalyst and the second catalyst is a silver catalyst.

20 . The process according to claim 18 wherein the first catalyst and the second catalyst is an iron/molybdenum oxide based catalyst.

21 . (canceled)

22 . The process according to claim 18 wherein the first reaction zone is sized such that it terminates at a point when about 50% of the methanol or methylal will have been converted.

23 . The process according to claim 18 wherein the reactor pressure is from about 1.1 bar(a) to about 10 bar(a).

24 . The process according to claim 18 wherein the reactor temperature is from about 250° C. to about 450° C.

25 . Apparatus for carrying out a chemical reaction comprising:
means for supplying gaseous reactants to a first reaction zone comprising a first catalyst having a first catalyst particle equivalent diameter; means for removing an intermediate stream comprising unreacted reactants and a desired product and passing the intermediate stream to a second reaction zone comprising a tubular reactor comprising tubes, wherein said tubes comprise a plurality of catalyst carriers containing a second catalyst having a second catalyst particle equivalent diameter which is smaller than the first catalyst particle equivalent diameter of the first catalyst; and means for recovering a product stream,
wherein each catalyst carrier comprises:
an annular container for holding the second catalyst in use, said container having a perforated inner wall defining a tube, a perforated outer wall, a top surface closing the annular container and a bottom surface closing the annular container;
a surface closing the bottom of said tube formed by the inner wall of the annular container; a skirt extending upwardly from the perforated outer wall of the annular container from a position at or near the bottom surface of said container to a position below the location of a seal;
and a seal located at or near the top surface and extending from the container by a distance which extends beyond an outer surface of the skirt.

26 . (canceled)

27 . (canceled)

28 . (canceled)

29 . The apparatus according to claim 25 wherein interstage cooling is provided between the first and second reaction zones.

30 . The apparatus according to claim 25 wherein the first reaction zone comprises a tubular fixed bed reactor.

31 . (canceled)

32 . (canceled)

33 . (canceled)

34 . (canceled)

35 . (canceled)

36 . The apparatus according to claim 25 further comprising means to recycle a portion of the product stream to at least one of the first and second reaction zones.

37 . The apparatus according to claim 25 further comprising one of a) means for adding at least one reactant& to the intermediate stream before it is added to the second reaction zone, and b) means for adding at least one reactant to the second reaction zone.

38 . (canceled)

39 . The apparatus according to claim 25 wherein the first reaction zone is sized such that it terminates at a point when about 50% of the gaseous reactants will have been converted.

Assignees

• Johnson Matthey Davy Technologies Ltd

Inventors

• Holdsworth Duncan David
• Gray Julian Stuart

Classifications

• B01J2208/00176

  outside the reactor · CPC title

• C07C45/38

  being a primary hydroxyl group · CPC title

• B01J8/0457

  the beds being placed in separate reactors · CPC title

• B01J19/1812

  Tubular reactors · CPC title

• B01J2208/025

  Two or more types of catalyst · CPC title