Method for production of sulfuric acid from sulfur containing feeds with gas quenching

Patent metadata

Field	Value
Publication number	US-10532930-B2
Application number	US-201716309305-A
Country	US
Kind code	B2
Filing date	Jul 4, 2017
Priority date	Jul 21, 2016
Publication date	Jan 14, 2020
Grant date	Jan 14, 2020

Abstract

A plant for the production of sulfur trioxide from a feed stream containing sulfur-containing compounds and dissolved metals and alkali metals by a process, which involves gas quenching, comprises an incineration furnace, a mixing device and/or a dilution air heater, a dust removal device and an SO2 converter. The plant may further comprise a condenser for the purpose of producing sulfuric acid.

First claim

The invention claimed is:

1. A method for the production of sulfur trioxide from a feed stream comprising sulfur-containing compounds and dissolved metals and alkali metals, said process comprising the following steps:
incineration in the presence of an O 2 -rich stream and optionally a support fuel, whereby the sulfur-containing compounds in the feed stream are converted to SO 2 and the dissolved metals and alkali metals are converted into a partly solidified dust,
mixing the hot process gas from the incinerator with a stream of colder gas in a mixing unit, such that the temperature of the combined stream is below the particle solidification temperature,
cooling of the combined gas stream in one or two heat exchangers,
removing solid dust particles from the combined gas stream in a dust removal device,
optionally adding hot dilution air to the process gas to provide sufficient oxygen for the oxidation of SO 2 to SO 3 in an SO 2 converter, and
feeding the process gas to an SO 2 converter consisting of a number of catalyst layers with heat exchangers installed between the catalyst layers, thereby converting the SO 2 in the process gas to SO 3 .

2. Method according to claim 1 , wherein the incineration temperature is around 900-1300° C. and the exit temperature from the mixing unit is in the interval of 450-700° C.

3. Method according to claim 1 , wherein the temperature of all surfaces in the mixing unit, which are in contact with the process gas from the incinerator, are above the solidification temperature.

4. Method according to claim 1 , wherein the temperature of the colder stream added to the mixing unit is between 25 and 350° C.

5. Method according to claim 1 , wherein the heat exchanger(s) between the mixing step and the dust removal step is a waste heat boiler, a combustion air heater, a dilution air heater or any combination of those.

6. Method according to claim 1 , wherein the temperature of all surfaces of the mixing unit are above the sulfuric acid dew point temperature of the process gas.

7. Method according to claim 1 , wherein the inlet temperature of the catalyst layer(s) of the SO 2 converter is around 375-420° C.

8. Method according to claim 1 , wherein the converted process gas leaving the SO 2 converter is cooled to around 250-310° C.

9. A plant for the production of sulfur trioxide by the method according to claim 1 , said plant comprising an incineration furnace, a mixing device, a dilution air heater, a dust removal device, an SO 2 converter and a sulfuric acid condenser.

10. Plant according to claim 9 , wherein the SO 2 converter consists of a number of catalyst layers with heat exchangers installed between the catalyst layers.

11. Plant according to claim 9 , wherein quench air is added as atmospheric air.

12. Plant according to claim 9 , wherein quench air is added as hot air from the sulfuric acid condenser.

13. Plant according to claim 9 , wherein quench gas is added as process gas recycled from a position downstream from the dust removal device.

14. Plant according to claim 6 , wherein the process gas for quenching is withdrawn from a position upstream from the dust removal device.

Assignees

• Haldor Topsoe As

Inventors

• Thellefsen Morten
• Møllerhøj Martin

Classifications

• C01B17/503

  of sulfuric acid · CPC title

• C01B17/508

  by oxidation of sulfur compounds · CPC title

• B01D53/1468

  Removing hydrogen sulfide · CPC title

• C01B17/74

  Preparation · CPC title

• Y02P20/129

  Energy recovery, e.g. by cogeneration, H2recovery or pressure recovery turbines · CPC title