Reformer tube having a structured catalyst and improved heat balance

Patent metadata

Field	Value
Publication number	US-11351517-B2
Application number	US-201716333004-A
Country	US
Kind code	B2
Filing date	Sep 5, 2017
Priority date	Sep 14, 2016
Publication date	Jun 7, 2022
Grant date	Jun 7, 2022

Abstract

A reformer tube for producing synthesis gas by steam reforming of hydrocarbon-containing feed gases, in which a structured stream reforming catalyst is used, is proposed. According to the invention, a heat exchanger tube is arranged in the interior of the structured catalyst, with the feed gas stream flowing firstly through the structured catalyst and subsequently in countercurrent through the heat exchanger tube. This improves the heat exchange between the synthesis gas product stream and the structured catalyst and the feed gas stream flowing through it, especially in the radial direction.

First claim

The invention claimed is:

1. A reformer tube for converting a hydrocarbon-containing feed into a synthesis gas product containing carbon oxides and hydrogen under steam reforming conditions, the reformer tube comprising:
(a) a reaction chamber comprising an outer, pressure-bearing casing tube, which is configured to receive heat from the outside, wherein the casing tube is demarcated at a first end from an adjacent outlet chamber by means of a separating plate and is closed at a second end by means of a closure device;
(b) at least one structured packing disposed in the reaction chamber and containing a catalyst which is active for steam reforming;
(c) an inlet for a feed gas stream comprising the hydrocarbon-containing feed arranged on the reaction chamber, where the inlet is disposed at an end of the reaction chamber closest to the separating plate and is in fluid communication with a gas inlet into the structured packing;
(d) a heat exchanger tube disposed within the reaction chamber and within the structured packing and having a heat exchanger inlet end that is in fluid communication with a gas outlet from the structured packing, wherein the heat exchanger tube further comprises a heat exchanger outlet end that is in fluid communication with the outlet chamber, where the feed gas stream flows, after entry into the reaction chamber, firstly through the structured packing and subsequently countercurrently through the heat exchanger tube, wherein the heat exchanger tube and the synthesis gas product stream flowing through the heat exchanger tube are in a heat exchange relationship with the structured packing and the feed gas stream flowing through the structured packing;
(e) a collection conduit for the synthesis gas product which is in fluid communication with the outlet chamber, where
(f) the outlet end of the heat exchanger tube passes through the separating plate, opens into the outlet chamber and is in fluid communication with the collection conduit so that the synthesis gas product can go from the reaction chamber via the outlet chamber into the collection conduit, wherein
(g) the outlet chamber comprises an inner tube having an upper end and a lower end, wherein the upper end is proximate the separating plate, and the lower end is proximate the collection conduit, and wherein
(h) there is an absence of a gas tight connection between the inner tube and the separating plate, such that either the inner tube abuts the separating plate or the inner tube is at a distance from the separating plate.

2. The reformer tube according to claim 1 , wherein the casing tube and the heat exchanger tube have a circular cross section and the structured packing has an annular cross section and the casing tube, the structured packing and the heat exchanger tube are arranged coaxially and concentrically, with the structured packing being arranged between the inner wall of the casing tube and the outer wall of the heat exchanger tube so as to form an essentially gastight closure.

3. The reformer tube according to claim 1 , wherein the reformer tube is arranged upright, with the reaction chamber being arranged in the upper region and the outlet chamber being arranged in the lower region and the feed gas stream flowing from the bottom upwards through the structured packing.

4. The reformer tube according to claim 1 , wherein both the structured packing and the heat exchanger tube consist of individual modules or segments, with each heat exchanger tube segment being equipped with a support or bearer device for the associated packing segment.

5. The reformer tube according to claim 1 , wherein the reaction chamber comprises at least one region which contains a bed of a particulate, solid catalyst which is active for steam reforming.

6. The reformer tube according to claim 5 , wherein the region containing the catalyst bed is formed by a corresponding packing segment being left out but the associated heat exchanger tube segment being present.

7. The reformer tube according to claim 1 , wherein the heat exchanger tube is at least partly filled with a bed of inert bodies or is provided on its inside with guide plates.

8. A reformer furnace comprising a lid, a bottom, walls clad or lined with refractory material, and an interior space formed thereby, wherein the reformer furnace further comprises at least one reformer tube as claimed in claim 1 , and at least one burner configured to heat the reformer tube, wherein the at least one reformer tube and the at least one burner are disposed in the interior space or in a secondary space that is in fluid communication with the interior space.

9. The reformer furnace according to claim 8 , wherein the at least one reformer tube is arranged upright in the interior space, where the part of the reformer tube encompassing the reaction chamber is arranged at least partly in the interior space and the part of the reformer tube encompassing the outlet chamber is arranged at least partly outside the interior space.

10. The reformer furnace according to claim 9 , wherein the inlet for the feed gas stream comprising the feed is also arranged outside the interior space.

11. The reformer furnace according to claim 8 , wherein a plurality of reformer tubes and burners are arranged in the interior space and in that the longitudinal axes of flames produced by the burners are directed parallel to the longitudinal axes of the reformer tubes.

12. The reformer tube according to claim 1 , wherein the inner tube is fixed in position between an underside of the separating plate and the collection conduit by means of fasteners.

13. The reformer tube according to claim 1 , further comprising thermal insulation surrounding the inner tube.

14. A process for producing synthesis gas by catalytic steam reforming of hydrocarbon-containing feed under steam reforming conditions in the presence of a solid catalyst which is active for steam reforming, the process comprising the following steps:
(a) catalytically converting the hydrocarbon-containing feed in the presence of steam under steam reforming conditions into a synthesis gas product containing carbon oxides and hydrogen; and
(b) discharging the synthesis gas product,
wherein the catalytic conversion in step (a) is carried out in a reformer tube according to claim 1 .

Assignees

• Air Liquide

Inventors

• Ulber Dieter
• Gary Daniel
• Prost Laurent
• Tadiello Jean-Philippe
• Basin Marie

Classifications

• B01J8/0257

  in a cylindrical annular shaped bed · CPC title

• B01J19/246 Primary

  internally, i.e. the mixture circulating inside the vessel such that the upward stream is separated physically from the downward stream(s) · CPC title

• B01J2208/065

  Heating or cooling the reactor · CPC title

• B01J19/32

  Packing elements in the form of grids or built-up elements for forming a unit or module inside the apparatus for mass or heat transfer · CPC title

• B01J2219/32466

  comprising catalytically active material · CPC title