Process for performing an endothermic reaction

Patent metadata

Field	Value
Publication number	US-9492803-B2
Application number	US-201414536093-A
Country	US
Kind code	B2
Filing date	Nov 7, 2014
Priority date	Jul 5, 2007
Publication date	Nov 15, 2016
Grant date	Nov 15, 2016

Abstract

Process for performing an endothermic reaction in a reactor containing catalyst tubes, the catalyst tubes containing a catalyst promoting the endothermic reaction, the process comprising the steps of,
a. contacting the catalyst contained in the catalyst tubes with a feed flow passing through the channels from an entrance end to an exit end, b. contacting an outer surface of the catalyst tubes with a flow of a heating medium having an initial heating temperature and flowing co-currently with the flow of feeds to heat the surface by convection, c. mixing at least part of the heating medium after having been contacted with the catalyst tubes with a flow of fresh heating medium having a start temperature higher than the initial heating temperature to form the co-current heating medium having the initial heating temperature and reactor for carrying out the process.

First claim

The invention claimed is:

1. A reactor for performing an endothermic reaction process, comprising a heat providing section containing heat providing means, the heat providing section communicating with an inlet end of a reactor section, the reactor section containing catalyst tubes and having an outlet end communicating with a head space section, the catalyst tubes being screened from heat radiation of the heat generating means, the reactor further comprising a recirculation section connecting the head space section to the heat providing section;
further comprising a feed line and a product line and wherein the reactor section contains reactor panels, each reactor panel comprising a feed header, a product header and adjacent channels, each channel having a length, running from an entrance end to an exit end, and wherein the entrance ends are directly connected to and open into the feed header and the exit ends are directly connected to and open into the product header and wherein the feed header has at least one connection to a feed line and the product header has at least one connection to a product line and wherein part of at least one of the feed header and the product header is detachable giving access to the channel ends.

2. The reactor according to claim 1 , wherein the heat providing means comprise at least one burner.

3. The reactor according to claim 1 , wherein the entrance end of each catalyst tube is provided with flow restricting means suitable to impose a critical pressure drop on a feed flow entering the tube.

4. The reactor according to claim 1 , wherein the product line and the feed line are connected to a heat exchanger to exchange heat between a feed stream and a product stream.

5. The reactor according to claim 1 , wherein the reactor panels are located between the inlet end and the outlet end of the reactor section of the reactor.

6. The reactor according to claim 1 , further comprising shielding means to prevent direct exposure of the reactor panels to the reactor walls.

7. The reactor according to claim 6 , further comprising a temperature control separate from the reactor panels.

Assignees

• Saudi Basic Ind Corp

Inventors

• Kösters Peter Hubertus

Classifications

• Y02P20/584

  Recycling of catalysts · CPC title

• B01J19/2425

  in parallel · CPC title

• C07C5/333

  Catalytic processes · CPC title

• B01J19/006

  Baffles · CPC title

• B01J2208/00504

  by means of a burner · CPC title