Reformer tube with internal heat exchange

Patent metadata

Field	Value
Publication number	US-9278328-B2
Application number	US-201214356608-A
Country	US
Kind code	B2
Filing date	Nov 7, 2012
Priority date	Nov 11, 2011
Publication date	Mar 8, 2016
Grant date	Mar 8, 2016

Abstract

A reformer tube for producing synthesis gas by steam reforming of hydrocarbon-containing feed gases, preferably natural gas, includes one or more helically coiled heat exchanger tubes which are arranged within a catalyst bed of a reforming catalyst and are helically coiled over part of their length located within the catalyst bed and are otherwise straight are present, where the straight proportion of the heat exchanger tubes and/or the helix pitch of the helically coiled part alters within the catalyst bed and matching to requirements of the pressure drop, the heat exchange properties, and the corrosion resistance.

First claim

The invention claimed is:

1. A reformer tube for converting a hydrocarbonaceous feedstock into a synthesis gas product comprising a carbon oxide and hydrogen under steam reforming conditions, the reformer tube comprising:
(a) an outer tube comprising an open tube end, a closed tube end, and a bed of a solid catalyst active suitable for steam reforming, wherein the outer tube is configured to be heated from outside;
(b) a feed gas stream inlet, configured to feed in the feedstock, wherein the feed gas stream inlet is arranged at the open tube end and is in fluid connection with the catalyst bed;
(c) a helically-coiled heat exchanger tube arranged within the catalyst bed, wherein a helically-coiled heat exchanger tube inlet end is in fluid connection with the catalyst bed and a helically-coiled heat exchanger tube outlet end is in fluid connection with a synthesis gas product stream outlet, and wherein the helically-coiled heat exchanger tube is in heat exchanging relationship with the catalyst bed and the feed gas stream flowing through the catalyst bed; and
(d) a synthesis gas product stream outlet arranged at the open tube end and in fluid connection with the outlet end of the helically-coiled heat exchanger tube, but not in fluid connection with the inlet for the feed gas stream,
wherein the feed gas stream initially flows through the catalyst bed and subsequently in counterflow through the heat exchanger tube,
wherein (i) the helically-coiled heat exchanger tube is coiled along not more than 90% of its length located within the catalyst bed and otherwise extends straight, or (ii) a coil pitch of the helically-coiled heat exchanger tube changes within the catalyst bed, or (iii) both.

2. The reformer tube of claim 1 , wherein
a coiled part of the helically-coiled heat exchanger tube,
a change in the coil pitch within the catalyst bed, or
both,
are configured such that with a defined feed gas stream and temperature of the feed gas at the feed gas stream inlet, an outlet temperature lies above a temperature range active for metal corrosion by metal dusting.

3. The reformer tube of claim 1 , wherein
a coiled part of the helically-coiled heat exchanger tube,
a change in the coil pitch within the catalyst bed, or
both,
are configured such that with a defined feed gas stream and temperature of the feed gas at the feed gas stream inlet, a pressure loss between inlet and outlet lies below a defined maximum value.

4. The reformer tube of claim 1 wherein a coiled part of the helically-coiled heat exchanger tube is arranged in the vicinity of the helically-coiled heat exchanger tube outlet end.

5. The reformer tube of claim 4 , wherein a coil pitch of the helically-coiled heat exchanger tube decreases towards the helically-coiled heat exchanger tube outlet end.

6. The reformer tube of claim 1 wherein the helically-coiled heat exchanger tube is coiled along a part of not more than 90% of its length located within the catalyst bed.

7. The reformer tube of claim 1 wherein a free space arranged within the outer tube at the closed tube end,
wherein the free space is separated from the catalyst bed by a gas-permeable separating device,
wherein an inlet end of at least one helically-coiled heat exchanger tube protrudes into the free space, and
wherein the free space is in fluid connection with the catalyst bed and the helically-coiled heat exchanger tube.

8. The reformer tube of claim 1 comprising two helically-coiled heat exchanger tubes.

9. The reformer tube of claim 1 wherein the solid catalyst active comprises nickel.

10. The reformer tube of claim 1 wherein the helically-coiled heat exchanger tube outlet end opens into a brick-lined or coated tube portion,
wherein the brick lining or coating comprises a material resistant to metal dusting.

11. A reformer furnace, comprising:
a wall comprising a refractory lining;
a ceiling;
a bottom; and
an interior space formed by the wall, ceiling and bottom
wherein the reformer tube of claim 1 and a burner configured to heat the reformer tube are arranged in the interior space or in a secondary space which is in fluid connection with the interior space with respect to the burner flue gases.

12. The reformer furnace of claim 11 , wherein the closed tube end is arranged freely suspended in the interior space.

13. The reformer furnace of claim 11 , comprising a plurality of reformer tubes and burners arranged in the interior space,
wherein longitudinal axes of flames generated by the burners are aligned parallel to longitudinal axes of the reformer tubes.

14. A process for producing synthesis gas by catalytic steam reforming of a hydrocarbonaceous feedstock under steam reforming conditions in the presence of a solid catalyst active suitable for steam reforming, the method comprising:
(a) providing a feed gas stream comprising the feedstock, and adding reforming steam;
(b) catalytically converting the feedstock under steam reforming conditions to obtain a synthesis gas product comprising a carbon oxide and hydrogen;
(c) discharging and optionally reprocessing the synthesis gas product,
wherein the catalytically converting (b) is effected in the reformer tube of claim 1 .

15. The reformer tube of claim 1 , wherein the coil pitch of the helically-coiled heat exchanger tube changes within the catalyst bed.

16. The reformer tube of claim 1 , wherein the helically-coiled heat exchanger tube is coiled along not more than 90% of its length located within the catalyst bed and otherwise extends straight, and
wherein the coil pitch of the helically-coiled heat exchanger tube changes within the catalyst bed.

17. The method of claim 14 , wherein the hydrocarbonaceous feedstock is natural gas.

18. The reformer tube of claim 1 , wherein the coil pitch changes continuously.

19. The reformer tube of claim 1 wherein the helically-coiled heat exchanger tube is coiled along a part of in a range of from 50% to not more than 90% of its length located within the catalyst bed.

20. The reformer tube of claim 1 , comprising two of the heat exchanger tubes, arranged in the catalyst bed as a double helix.

Assignees

• Schlichting Holger
• Wolf Ulrich
• Pohl Sven
• Ulber Dieter
• Zolnowski Udo
• Coscia Antonio
• Cances Julien
• Camy-Peyret Frederic
• Mathey Fabrice
• Air Liquide
• Air Liquide Global E&C Solutions Germany Gmbh

Inventors

• Schlichting Holger
• Wolf Ulrich
• Pohl Sven
• Ulber Dieter
• Zolnowski Udo
• Coscia Antonio
• Cances Julien
• Camy-Peyret Frederic
• Mathey Fabrice

Classifications

• C01B3/38

  using catalysts · CPC title

• C01B2203/1235

  Hydrocarbons · CPC title

• B01J8/067

  Heating or cooling the reactor (B01J8/062 takes precedence) · CPC title

• B01J2208/0053

  Controlling multiple zones along the direction of flow, e.g. pre-heating and after-cooling · CPC title

• C01B2203/0883

  by indirect heat exchange · CPC title