Modular catalyst monoliths

Patent metadata

Field	Value
Publication number	US-10974964-B2
Application number	US-201615779347-A
Country	US
Kind code	B2
Filing date	Nov 18, 2016
Priority date	Nov 27, 2015
Publication date	Apr 13, 2021
Grant date	Apr 13, 2021

Abstract

The present invention relates to a reactor R with apparatus D, the latter comprising a gas- and/or liquid-permeable tray B, in the edge region of which there is disposed a lateral boundary W which fully encloses the tray B and forms a volume V comprising catalytic and/or noncatalytic shaped bodies (F), wherein there is at least one braid made of precious metal and/or base metal on the upstream side opposite the tray B, and the catalytic and/or noncatalytic shaped bodies (F) are selected from (i) shaped bodies (F 1 ) in the form of straight prisms, the footprint of which is selected from triangle, rectangle, hexagon or fragments of these polygons, and (ii) a combination of the shaped bodies (F 1 ) with shaped bodies (F 2 ) that are smaller than the shaped bodies (F 1 ), wherein groups of m to n shaped bodies (F 1 ), m and n being an integer from 3 to 30 with n>m, are framed in a metal cassette open in the upstream direction and closed in the downstream direction by a gas-permeable tray, in a virtually seamless manner with side face to side face and with their longitudinal axis aligned in vertical direction, virtually completely covering the cross section of the tray, to form modules (M), and the modules (M), optionally with cooperation of a joint filler material, with vertical alignment of the longitudinal axis of the shaped bodies (F 1 ), are joined to one another virtually seamlessly in a mosaic-like manner.

First claim

The invention claimed is:

1. A reactor R with apparatus D, the latter comprising a gas- and/or liquid-permeable tray B, in the edge region of which there is disposed a lateral boundary W which fully encloses the tray B and forms a volume V comprising catalytic and/or noncatalytic shaped bodies (F), wherein there is at least one braid made of precious metal and/or base metal on an upstream side opposite the tray B, and the catalytic and/or noncatalytic shaped bodies (F) are selected from (i) shaped bodies (F 1 ) in the form of straight prisms, the footprint of which is selected from triangle, rectangle, hexagon or fragments of these polygons, and (ii) a combination of the shaped bodies (F 1 ) with shaped bodies (F 2 ) that are smaller than the shaped bodies (F 1 ), wherein groups of m to n shaped bodies (F 1 ), m and n being an integer from 3 to 30 with n>m, are framed in a metal cassette open in the upstream direction and closed in the downstream direction by a gas-permeable tray, with side face to side face and with their longitudinal axis aligned in vertical direction, covering the cross section of the tray, to form modules (M), and the modules (M), optionally with cooperation of a joint filler material, with vertical alignment of the longitudinal axis of the shaped bodies (F 1 ), are joined to one another in a mosaic-like manner such that they cover the cross section of the tray B.

2. The reactor R with apparatus D according to claim 1 , wherein there is a thermally insulating layer S at least over part of the area of the inside of the lateral boundary W of the apparatus D, and the material for the thermally insulating layer S is selected from the group consisting of ceramic material, microporous material and silicate fibers.

3. The reactor R with apparatus D according to claim 1 , wherein the cross section of the reactor Rand of the tray B is round in each case.

4. The reactor R with apparatus D according to claim 1 , wherein the volume V of the apparatus D has been filled with catalytic and/or noncatalytic shaped bodies (F) up to a maximum of the lowermost braid made of precious metal and/or base metal.

5. A process comprising preparing nitrogen oxides by catalytic oxidation of ammonia in the reactor R of claim 1 and optionally reacting of the nitrogen oxides with water to give nitric acid.

6. A process for preparing nitrogen oxides, wherein, in the reactor R of claim 1 , ammonia is catalytically oxidized with an oxygenous gas and the reaction products which comprise nitrogen oxides and are thus formed are allowed to flow through an arrangement of catalytic and/or noncatalytic shaped bodies (F) in an apparatus D, wherein the arrangement of the catalytic and/or noncatalytic shaped bodies (F) and the apparatus D are as defined in claim 1 .

7. A process for preparing nitric acid, wherein, in a reactor R, ammonia is catalytically oxidized with an oxygenous gas and the reaction products which comprise nitrogen oxides and are thus formed are allowed to flow through an arrangement of catalytic and/or noncatalytic shaped bodies (F) in an apparatus D and then reacted with water to give nitric acid, wherein the arrangement of the catalytic and/or noncatalytic shaped bodies (F) and the apparatus D are as defined in claim 1 .

Assignees

• Basf Se

Inventors

• Olbert Gerhard
• Gauer Jochen
• Friedrich Holger
• Spiegel Andreas
• Wölfert Andreas
• Gmeiner Wolfgang
• Lorenz Michael

Classifications

• C01B21/26

  Preparation by catalytic {or non-catalytic} oxidation of ammonia · CPC title

• C01B21/38

  Nitric acid · CPC title

• B01J8/00

  Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes · CPC title

• B01J19/2485

  Monolithic reactors · CPC title

• B01J19/24

  Stationary reactors without moving elements inside (B01J19/08, B01J19/26 take precedence; with stationary particles B01J8/02) · CPC title