Method and apparatus for producing high purity phosgene

Patent metadata

Field	Value
Publication number	US-2016176715-A1
Application number	US-201414907417-A
Country	US
Kind code	A1
Filing date	Jul 25, 2014
Priority date	Jul 26, 2013
Publication date	Jun 23, 2016
Grant date	—

Abstract

A reactor for producing phosgene, the reactor comprising: tube located in a shell and a space located between the tube and the shell; a cooling medium located in the space and a catalyst located in the tube or cooling medium located in the tube and a catalyst located in the space; a feed inlet; and a product mixture outlet; wherein the tube comprises one or more of: a mini-tube and a second tube section; a first concentric tube concentrically located in the shell; a twisted tube; an internal scaffold; and an external scaffold.

First claim

I/we claim:

1 . A method of producing phosgene, comprising:
reacting carbon monoxide and chlorine in a phosgene reactor in the presence of a catalyst to produce a final product composition comprising phosgene; wherein carbon tetrachloride is present in the final product composition in an amount of 0 to 10 ppm by volume, based on the total volume of phosgene; wherein the phosgene reactor comprises a tube, a shell, and a space located between the tube and the shell; and wherein the catalyst is disposed in the tube and a cooling medium is located in the space, or the catalyst is disposed in the space and a cooling medium is located in the tube.

2 . The method of claim 1 , wherein the tube comprises a mini-tube section comprising a mini-tube and a second tube section and wherein the reacting comprises:
passing a feed comprising carbon monoxide and chlorine over the catalyst in the mini-tube section to produce a first product composition, wherein the mini-tube has an average diameter of 0.1 to 10 millimeters; and passing at least a portion of the first product composition over the catalyst disposed in the second tube section, wherein the second tube section comprises an increased diameter tube with an average diameter greater than the mini-tube, to produce the final product composition.

3 . The method of claim 1 , wherein a peak temperature in the phosgene reactor is less than 800° C.

4 . The method of claim 3 , wherein the peak temperature is less than 400° C.

5 . The method of claim 1 , wherein the phosgene reactor has a heat transfer area per unit volume of 100 to 10,000 m 2 /m 3 .

6 . A reactor for producing phosgene, the reactor comprising:
tube located in a shell and a space located between the tube and the shell; a cooling medium located in the space and a catalyst located in the tube or cooling medium located in the tube and a catalyst located in the space; a feed inlet; and a product mixture outlet; wherein the tube comprises one or more of
a mini-tube and a second tube section;
a first concentric tube concentrically located in the shell;
a twisted tube;
an internal scaffold; and
an external scaffold.

7 . The reactor of claim 6 , wherein the tube comprises a mini-tube section comprising the mini-tube and the second tube section; wherein the mini-tube has an average diameter of 0.1 to 10 millimeters; and wherein the second tube section comprises an increased diameter tube with an average diameter greater than the mini-tube.

8 . The reactor of claim 7 , wherein the average diameter of the increased diameter tube is greater than 6 millimeters.

9 . The reactor of claim 6 , wherein the tube comprises the first concentric tube concentrically located in the shell.

10 . The reactor of claim 6 , wherein the first concentric tube has a multi-petal cross-sectional geometry.

11 . The reactor of claim 6 , wherein the tube comprises the first concentric tube and further comprises a second concentric tube, wherein the first concentric tube and the second concentric tube are located within the shell, and a cooling medium is located between an outer wall of the second tube and an inner wall of the shell.

12 . The reactor of claim 6 , wherein the tube comprises the twisted tube, and wherein the twisted tube has a major diameter and a minor diameter and a ratio of the major diameter to the minor diameter is 1:1 to 20:1.

13 . The reactor of claim 6 , wherein the twisted tube has a major diameter and a minor diameter and wherein the major diameter and the minor diameter are each independently greater than or equal to 5 mm.

14 . The reactor of claim 6 , wherein the twisted tube has a smooth helical shape, a jagged helical shape, a wavy shape, a bulging shape, or a combination comprising one or more of the forgoing.

15 . The reactor of claim 6 , wherein the tube comprises the internal scaffold, and wherein the internal scaffold comprises one or both of an internal insert and an internal fin.

16 . The reactor of claim 15 , wherein the internal insert, the internal fin, or both comprises an internal scaffolding element, wherein the internal scaffolding element comprises a perpendicular element, an inner element, an angled element, or a combination comprising one or more of the foregoing.

17 . The reactor of claim 6 , wherein the tube comprises the external scaffold, and wherein the external scaffold comprises one or both of an external insert and an external fin.

18 . The reactor of claim 17 , wherein the external insert, the external fin, or both comprises an external scaffolding element and wherein the external scaffolding element comprises a helical element, an annular element, a studded element, a serrated element, a wire element, a cut helical element, a cut annular element, a wavy helical element, a slotted wavy helical element, a slotted helical element, or a combination comprising one or more of the foregoing.

19 . The reactor of claim 6 , wherein the catalyst varies in concentration, activity, or both from a feed end of the tube to an outlet end of the tube and wherein the variance is from low activity, concentration, or both at the feed end to a higher activity, concentration, or both, at the outlet end.

20 . The reactor of claim 6 , wherein the phosgene reactor has a heat transfer area per unit volume of 100 to 10,000 m 2 /m 3 .

Assignees

• Gautam Pankaj Singh
• Sabic Global Technologies Bv

Inventors

• Gautam Pankaj Singh
• Hollar Jr William E

Classifications

• B01J19/2425

  in parallel · CPC title

• B01J19/006

  Baffles · CPC title

• B01J19/2405

  provoking a turbulent flow of the reactants, such as in cyclones, or having a high Reynolds-number · CPC title

• B01J2208/00221

  comprising baffles for guiding the flow of the heat exchange medium · CPC title

• B01J8/0285

  Heating or cooling the reactor (for tubular reactors in furnaces B01J8/062) · CPC title