Generation of sulfur trioxide and sulfuric acid

• US 8,052,949 B2
• Filed: 05/11/2009
• Issued: 11/08/2011
• Est. Priority Date: 05/11/2009
• Status: Expired due to Fees

• Current Assignee: Thermo Fisher Scientific Incorporated
• Original Assignee: Thermo Fisher Scientific Incorporated
• Inventors: Li, Yongquan, Marcotte, Bryan A., Kita, Dieter, Socha, Jeffrey
• Primary Examiner(s): Mayes; Melvin
• Assistant Examiner(s): DAVIS, SHENG HAN
• Application Number:
  US12/463,795
• Publication Number:
  US 20100284899A1
• Time in Patent Office: 911 Days
• Field of Search: None
• US Class Current: 423/222
• CPC Class Codes: C01B 17/76 by contact processes
• CPC Class Codes: C01B 17/80 Apparatus
• CPC Class Codes: G01N 2001/2893 Preparing calibration standards
• CPC Class Codes: G01N 33/0006 Calibrating gas analysers
• CPC Class Codes: G01N 33/0042 for SO2, SO3
• CPC Class Codes: Y10T 436/10 Composition for standardization, calibration, simulation, stabilization, preparation or preservation; processes of use in preparation for chemical testing

Abstract

Configurations herein include a novel process and apparatus for generating and maintaining sulfur trioxide gas. The generation system and process operate to provide sulfur trioxide calibration gas for calibrating sulfur trioxide detection devices. The system and process provides a known, concentration of sulfur trioxide gas via a heated catalyst, which enables accurate calibration of measurement equipment. The system functions in part by controlling temperature, amount of moisture, residence time, catalyst selection, diluting generated sulfur trioxide and by locating the sulfur trioxide generator at a point of injection of a sulfur trioxide detection system.

Claims

1. A method of generating and maintaining sulfur trioxide gas, the method comprising:

receiving a known concentration of sulfur dioxide gas;

receiving an oxidizing agent gas;

exposing the known concentration of sulfur dioxide gas and the oxidizing agent gas to a catalyst, the catalyst being heated, to react the known concentration of sulfur dioxide gas and the oxidizing agent gas into a known concentration of sulfur trioxide gas;

maintaining the known concentration of sulfur trioxide gas in a gaseous state;

wherein maintaining the known concentration of sulfur trioxide gas in the gaseous state includes maintaining the sulfur trioxide gas above a conversion point temperature of sulfuric acid;

passing a portion of the sulfur trioxide gas, having a known concentration of sulfur trioxide gas, through a sulfur trioxide detection device, the sulfur trioxide detection device being a device that measures a concentration of sulfur trioxide;

wherein receiving the known concentration of sulfur dioxide gas includes pre-heating the sulfur dioxide gas before exposing the sulfur dioxide gas to the catalyst;

wherein exposing the known concentration of sulfur dioxide gas and the oxidizing agent gas to a catalyst includes heating the catalyst to a temperature between 225 degrees Celsius and 600 degrees Celsius;

performing the step of reacting the known concentration of sulfur dioxide gas and the oxidizing agent gas into the known concentration of sulfur trioxide gas, and the step of maintaining the known concentration of sulfur trioxide gas in the gaseous state, within a sulfur trioxide gas generation system that supplies sulfur trioxide gas as a calibration gas to a combustion gas probe that measures exhaust gases; and

heating the catalyst to above about 550 degrees Celsius to restore a degraded condition of the catalyst, the degraded condition causing reduced efficiency of converting the sulfur dioxide into the sulfur trioxide.

2. The method of claim 1, further comprising:

wherein maintaining the known concentration of sulfur trioxide gas in the gaseous state includes;

diluting the sulfur trioxide gas with a dilution gas; and

passing a portion of the diluted sulfur trioxide gas, having a known concentration of sulfur trioxide gas, through a sulfur trioxide detection device.

3. The method of claim 2, wherein passing the portion of the diluted sulfur trioxide gas, having a known concentration of sulfur trioxide gas, through the sulfur trioxide detection device includes:

passing the diluted sulfur trioxide gas through a multi-pass optical cell that measures a concentration of sulfur trioxide.

4. The method of claim 2, further comprising:

calibrating the sulfur trioxide detection device by measuring the known concentration of sulfur trioxide gas passing through the sulfur trioxide detection device; and

adjusting the measurements of the sulfur trioxide detection device based on calibration using the known concentration of sulfur trioxide gas.

5. The method of claim 1, wherein exposing the known concentration of sulfur dioxide gas and the oxidizing agent gas to a catalyst includes:

exposing the known concentration of sulfur dioxide gas and the oxidizing agent gas to a catalyst at different flow rates at different time periods; and

adjusting the temperature of the catalyst according to the different flow rates at the different time periods to yield a conversion of sulfur dioxide gas to sulfur trioxide gas at an efficiency level above about 99%.

6. The method of claim 1, further comprising:

converting the sulfur trioxide gas to sulfuric acid by adding dihydrogen monoxide; and

heating the sulfuric acid to a temperature sufficient to convert the sulfuric acid to sulfur trioxide gas.

7. The method as in claim 1 further comprising:

controlling application of heat to the known concentration of sulfur dioxide gas and oxidizing agent gas to convert the sulfur dioxide gas into the sulfur trioxide gas, the concentration of sulfur trioxide being known based on a known reaction conversion efficiency of converting the sulfur dioxide gas into the sulfur trioxide gas.

8. The method as in claim 7, further comprising:

wherein the catalyst is a porous metallic catalyst and wherein the step of exposing includes passing a mixture of the known concentration of sulfur dioxide gas and the oxidizing agent gas through the porous metallic catalyst, the reaction conversion efficiency of converting the sulfur dioxide gas into the sulfur trioxide gas being greater than 99%;

receiving the known concentration of sulfur dioxide gas and oxidizing agent gas from a resource that stores the known concentration of sulfur dioxide gas and oxidizing agent gas as a mixture, the mixture stored in the resource being substantially free of water; and

passing the known concentration of sulfur trioxide gas through an optical measurement system to calibrate the optical measurement system.

9. The method as in claim 8 further comprising:

controlling application of heat to the sulfur trioxide gas to prevent the sulfur trioxide gas from converting into sulfur dioxide.

10. A method of generating and maintaining sulfur trioxide gas, the method comprising:

receiving a known concentration of sulfur dioxide gas;

receiving an oxidizing agent gas;

exposing the known concentration of sulfur dioxide gas and the oxidizing agent gas to a catalyst, the catalyst being heated, to react the known concentration of sulfur dioxide gas and the oxidizing agent gas into a known concentration of sulfur trioxide gas;

maintaining the known concentration of sulfur trioxide gas in a gaseous state;

wherein the steps of receiving the known concentration of sulfur dioxide gas and receiving the oxidizing agent gas comprise receiving the known concentration of sulfur dioxide gas and receiving the oxidizing agent gas from a same gas cylinder at a known gas flow rate, the same gas cylinder containing both the known concentration of sulfur dioxide and the oxidizing agent gas mixed together, wherein a concentration of the oxidizing agent gas in the same gas cylinder exceeds the known concentration of the sulfur dioxide gas;

wherein exposing the known concentration of sulfur dioxide gas and the oxidizing agent gas to the catalyst to react the known concentration of sulfur dioxide gas and the oxidizing agent gas into a known concentration of sulfur trioxide gas comprises reacting the sulfur dioxide gas with a surface area of the catalyst, the catalyst being a metallic catalyst, the catalyst being heated to a specific temperature between 225 degrees Celsius and 600 degrees Celsius based on the known gas flow rate to and known concentration to yield a conversion efficiency of sulfur dioxide to sulfur trioxide above about a 99% conversion efficiency such that the known concentration of sulfur trioxide is known based on the known concentration of sulfur dioxide received and the conversion efficiency above about 99%;

wherein maintaining the known concentration of sulfur trioxide gas in a gaseous state comprises;

maintaining the known concentration of sulfur trioxide at a conversion efficiency level above about 99%;

maintaining the sulfur trioxide gas above a conversion point temperature of sulfuric acid; and

maintaining the known concentration of sulfur trioxide gas in a gaseous state for a duration sufficient to deliver the known concentration of sulfur trioxide gas as a calibration gas to a sulfur trioxide gas measurement chamber via a sulfur trioxide gas delivery conduit connecting a sulfur dioxide oxidizing chamber to the sulfur trioxide measurement chamber;

diluting the known concentration of sulfur trioxide gas with heated air, that is substantially free of water, prior to delivering the known concentration of sulfur trioxide gas as a calibration gas to a sulfur trioxide gas measurement chamber via the sulfur trioxide gas delivery conduit;

delivering the known concentration of sulfur trioxide gas, as the calibration gas, to the sulfur trioxide gas measurement chamber via the sulfur trioxide gas delivery conduit;

using the known concentration of sulfur trioxide calibration gas in the sulfur trioxide gas measurement chamber to calibrate a sulfur trioxide gas detection device that directly measures sulfur trioxide gas concentrations, wherein calibrating the sulfur trioxide gas detection device includes adjusting measurements of the sulfur trioxide detection device using the known concentration of sulfur trioxide gas;

subsequent to calibrating the sulfur trioxide gas measurement device, measuring sulfur trioxide concentrations in gas samples received from a flue that carries exhaust gases from a coal-fired system via the sulfur trioxide gas measurement device that directly measures sulfur trioxide gas concentrations;

wherein using the known concentration of sulfur trioxide calibration gas in the sulfur trioxide gas measurement chamber to calibrate the sulfur trioxide gas detection device includes passing the diluted sulfur trioxide calibration gas through a multi-pass device that measures a concentration of sulfur trioxide directly; and

performing the step of reacting the known concentration of sulfur dioxide gas and the oxidizing agent gas into the known concentration of sulfur trioxide gas, and the step of maintaining the known concentration of sulfur trioxide gas in the gaseous state, within a sulfur trioxide gas generation system used with a combustion gas probe that is configured to attach to an exhaust gas stack.

11. The method of claim 10, further comprising:

wherein exposing the known concentration of sulfur dioxide gas and the oxidizing agent gas to the catalyst comprises;

exposing the known concentration of sulfur dioxide gas and the oxidizing agent gas to a catalyst at different flow rates at different time periods;

adjusting the temperature of the catalyst according to the different flow rates at the different time periods to yield the conversion efficiency of sulfur dioxide to sulfur trioxide above about the 99% conversion efficiency; and

wherein diluting the known concentration of sulfur trioxide gas with heated air comprises;

diluting the sulfur trioxide calibration gas to a concentration amount that is substantially equal to an expected amount of sulfur trioxide gas in a non-calibration gas sample from the gas samples received from the flue that carries exhaust gases from the coal-fired system.

12. The method of claim 10, wherein diluting the known concentration of sulfur trioxide gas with heated air comprises:

diluting the sulfur trioxide calibration gas at a first amount to calibrate the sulfur trioxide detection device at a first concentration setting; and

diluting the sulfur trioxide calibration gas at a second amount to calibrate the sulfur trioxide detection device at a second concentration setting.

13. The method of claim 10, further comprising:

adjusting flow rates and oxidizing temperatures according to a type of fuel being used to generate exhaust within the exhaust gas stack; and

heating the metallic catalyst to above about 550 degrees Celsius to restore a degraded condition of the catalyst, the degraded condition causing reduced efficiency of converting the sulfur dioxide into the sulfur trioxide, the metallic catalyst being loose metallic particles positioned within the sulfur dioxide oxidizing chamber using porous frits.

14. A method of generating and maintaining sulfur trioxide gas, the method comprising:

receiving a known concentration of sulfur dioxide gas;

receiving an oxidizing agent gas;

exposing the known concentration of sulfur dioxide gas and the oxidizing agent gas to a catalyst, the catalyst being heated, to react the known concentration of sulfur dioxide gas and the oxidizing agent gas into a known concentration of sulfur trioxide gas;

maintaining the known concentration of sulfur trioxide gas in a gaseous state;

wherein exposing the known concentration of sulfur dioxide gas and the oxidizing agent gas to the catalyst to react the known concentration of sulfur dioxide gas and the oxidizing agent gas into a known concentration of sulfur trioxide gas comprises reacting substantially all of the sulfur dioxide gas with a surface area of the catalyst, the catalyst being a metallic catalyst, the catalyst being heated to a specific temperature between 225 degrees Celsius and 600 degrees Celsius based on a known gas flow rate and known concentration to yield a conversion efficiency of sulfur dioxide to sulfur trioxide above about a 99% conversion efficiency such that the known concentration of sulfur trioxide is known based on the known concentration of sulfur dioxide received and the conversion efficiency above about 99%;

wherein maintaining the known concentration of sulfur trioxide gas in a gaseous state includes maintaining the sulfur trioxide gas above a conversion point temperature of sulfuric acid, and maintaining the known concentration of sulfur trioxide gas in a gaseous state for a duration sufficient to deliver the known concentration of sulfur trioxide gas as a calibration gas to a sulfur trioxide gas measurement chamber via a sulfur trioxide gas delivery conduit connecting a sulfur dioxide oxidizing chamber to the sulfur trioxide measurement chamber;

using the known concentration of sulfur trioxide calibration gas in the sulfur trioxide gas measurement chamber to calibrate a sulfur trioxide gas detection device that directly measures sulfur trioxide gas concentrations, wherein calibrating the sulfur trioxide gas detection device includes adjusting measurements of the sulfur trioxide detection device using the known concentration of sulfur trioxide gas;

performing the step of reacting the known concentration of sulfur dioxide gas and the oxidizing agent gas into the known concentration of sulfur trioxide gas, and the step of maintaining the known concentration of sulfur trioxide gas in the gaseous state, within a sulfur trioxide gas generation system; and

wherein the steps of receiving the known concentration of sulfur dioxide gas and receiving the oxidizing agent gas comprise receiving the known concentration of sulfur dioxide gas and receiving the oxidizing agent gas from a same gas cylinder at the known gas flow rate, the same gas cylinder containing both the known concentration of sulfur dioxide and the oxidizing agent gas mixed together, wherein a concentration of the oxidizing agent gas in the same gas cylinder exceeds the known concentration of the sulfur dioxide gas.

15. The method of claim 14, further comprising:

heating the metallic catalyst to above about 550 degrees Celsius to restore a degraded condition of the catalyst, the degraded condition causing reduced efficiency of converting the sulfur dioxide into the sulfur trioxide, the metallic catalyst being metallic particles positioned within the sulfur dioxide oxidizing chamber;

diluting the sulfur trioxide calibration gas to a concentration amount that is substantially equal to an expected amount of sulfur trioxide gas in a non-calibration gas sample from the gas samples received from a flue that carries exhaust gases; and

passing a portion of the diluted sulfur trioxide gas, having the known concentration of sulfur trioxide gas, through the sulfur trioxide gas detection device.

16. The method of claim 15, wherein the sulfur trioxide gas generation system is housed within a combustion gas probe configured to attach to a combustion system.

17. A method of generating and maintaining sulfur trioxide gas, the method comprising:

receiving a known concentration of sulfur dioxide gas;

receiving an oxidizing agent gas;

exposing the known concentration of sulfur dioxide gas and the oxidizing agent gas to a catalyst, the catalyst being heated, to react the known concentration of sulfur dioxide gas and the oxidizing agent gas into a known concentration of sulfur trioxide gas;

maintaining the known concentration of sulfur trioxide gas in a gaseous state;

wherein maintaining the known concentration of sulfur trioxide gas in the gaseous state includes;

diluting the sulfur trioxide gas with a dilution gas; and

maintaining the diluted sulfur trioxide gas above a conversion point temperature of sulfuric acid;

passing a portion of the diluted sulfur trioxide gas, having a known concentration of sulfur trioxide gas, through a sulfur trioxide detection device, the sulfur trioxide detection device being a device that measures a concentration of sulfur trioxide;

wherein receiving the known concentration of sulfur dioxide gas includes pre-heating the sulfur dioxide gas before exposing the sulfur dioxide gas to the catalyst; and

wherein exposing the known concentration of sulfur dioxide gas and the oxidizing agent gas to a catalyst includes heating the catalyst to a temperature between 225 degrees Celsius and 600 degrees Celsius; and

performing the step of reacting the known concentration of sulfur dioxide gas and the oxidizing agent gas into the known concentration of sulfur trioxide gas, and the step of maintaining the known concentration of sulfur trioxide gas in the gaseous state, within a sulfur trioxide gas generation system that supplies sulfur trioxide gas as a calibration gas to a combustion gas probe that measures exhaust gases.

18. The method of claim 17, further comprising:

using the known concentration of sulfur trioxide calibration gas in a sulfur trioxide gas measurement chamber to calibrate a sulfur trioxide gas detection device that directly measures sulfur trioxide gas concentrations, wherein calibrating the sulfur trioxide gas detection device includes adjusting measurements of the sulfur trioxide detection device using the known concentration of sulfur trioxide gas; and

heating the catalyst to above about 550 degrees Celsius to restore a degraded condition of the catalyst, the degraded condition causing reduced efficiency of converting the sulfur dioxide into the sulfur trioxide, the metallic catalyst being platinum particles positioned within a sulfur dioxide oxidizing chamber.

19. The method of claim 18, wherein the known concentration of sulfur dioxide gas is known is indicated as a numeric value in parts per million.