IP Library Granted Patent US 11,933,552
Granted Patent B2
US 11,933,552 · App. 17/688,032 · Granted Mar 19, 2024

Heat exchanger for heating gas and use of the heat exchanger

Inventors: Oskar Stephan (Ludwigshafen, DE); Karl-Friedrich Schneider (Altrip, DE); Matthias Weismantel (Ludwigshafen, DE)
Assignee: BASF SE
F28F19/06C23C2/06C23C2/28F26B3/04F26B17/04F26B21/02
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Quick Facts
Patent No.
US 11,933,552
App. No.
17/688,032
Granted
Mar 19, 2024
Kind
B2
Abstract

The invention relates to a heat exchanger for heating gas to a temperature in the range from 150 to 400° C., wherein the gas is heated by indirect heat transfer and all the surfaces of the walls of the heat exchanger which come into contact with the gas have been hot dip galvanized and the surfaces which come into contact with the gas, after the hot dip galvanization, have been heat treated at a temperature in the range from 400 to 750° C. The invention further relates to the use of the heat exchanger.

Claims (6)

1. A method of drying superabsorbent particles comprising heating a drying gas to a temperature in a range from 150 to 400° C. by indirect heat transfer in a heat exchanger for heating gas to a temperature in the range from 150 to 400° C. by indirect heat transfer, wherein all surfaces of walls of the heat exchanger which contact a gas have been hot dip galvanized and then cooled under air to form a zinc-iron diffusion layer and a pure zinc layer on the walls, wherein after the hot dip galvanization and cooling under air, surfaces which contact the gas have been heat treated at a temperature in the range from 400 to 750° C., thereby achieving a zinc coating that remains stable and wherein no Kirkendall effect occurs.

2. The method according to claim 1 , wherein the heat exchanger is disposed beneath a drying belt of a belt drier.

3. The method according to claim 1 for drying superabsorbent particles.

4. The method according to claim 1 , wherein the heat exchanger heats the drying gas which is added to a spray tower for production of superabsorbent particles.

5. The method according to claim 1 , wherein the drying gas is circulated.

6. The method according to claim 1 , wherein a thermal oil, an ionic liquid, a salt melt, or steam is used as a heat transfer medium.

Priority Claims (1)
EP 15202312 · Dec 23, 2015 · regional
Continuity (2)
Continuation 16064021
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