Method for removing acidic gases from waste gas

• US 6,881,243 B1
• Filed: 10/06/2000
• Issued: 04/19/2005
• Est. Priority Date: 10/12/1999
• Status: Expired due to Fees

• Current Assignee: Lextran Ltd.
• Original Assignee: Lextran Ltd.
• Inventors: Pipko, Gregori, Khitrik, Adolf, Doron, Benjamin
• Primary Examiner(s): Smith, Duane S.
• Application Number:
  US10/110,311
• Time in Patent Office: 1,656 Days
• Field of Search: 951/88, 951/89, 951/90, 951/97, 952/05, 952/06, 952/35, 952/32, 423/235, 423/242.1, 423/242.2, 423/243.01, 423/243.03, 423/243.06
• US Class Current: 95/188
• CPC Class Codes: B01D 53/1456 Removing acid components
• CPC Class Codes: B01D 53/1493 Selection of liquid materials for use as absorbents
• CPC Class Codes: B01D 53/60 Simultaneously removing sulfur oxides and nitrogen oxides
• CPC Class Codes: Y02A 50/20 Air quality improvement or preservation, e.g. vehicle emission control or emission reduction by using catalytic converters

Abstract

A method for removing acidic gases from waste gases is disclosed. The invention relates to a method for removing acid gases, in particular from SO₂ and NO_x, by contacting the waste gas with an emulsion of water in organic sulfoxides, in particular of water in oil-derived-sulfoxides. The organic sulfoxide phase can be regenerated after the emulsion is loaded with polluants, by letting the emulsion to settle down and separate into two phases. The aqueous phase obtained after the separation contains sulfate and nitrate ions which can be collected and used as valuable chemicals.

Claims

1. A method for simultaneously removing acidic gases of sulfur and nitrogen oxides from waste gas before it is emitted to the atmosphere by contacting said waste gas with a scrubbing agent comprising an emulsion of water in organic sulfoxides in the presence of a stream of air or of ozonated air.

2. A method according to claim 1 wherein the waste gas is a combustion flue gas.

3. A method according to claim 1 wherein the waste gas is a gas mixture released from a chemical process.

4. A method according to claim 1 wherein the organic sulfoxides are oil derived sulfoxides.

5. A method according to claim 4 wherein the oil derived sulfoxides are derived from the diesel fraction of oil.

6. A method according to claim 1 wherein the weight ratio of water:

organic sulfoxide in the emulsion is in the range 10;

90 to 90;

10.

7. A method according to claim 1 wherein the scrubbing agent is regenerated after it is loaded, by letting said scrubbing agent to separate into two phases, collecting the upper sulfoxide phase and adding to said sulfoxide phase a fresh amount of aqueous solution.

8. A method according to claim 7 wherein the aqueous phase obtained after the separation of phases contains nitric and/or sulfuric acids and is collected to be used as useful acid solutions.

9. A method according to claim 8 wherein ammonium salts are added to the acid solution obtained after the separation of phases to obtain a solution of ammonium nitrate and/or ammonium sulfate useful as a fertilizer.

10. A method for cleaning fuel gas from acid gases according to claim 1 wherein an aqueous phase of the emulsion further contains ammonium ions and wherein a solution of ammonium nitrate and/or ammonium sulfate obtained after separation of the emulsion is collected to be used as a fertilizing solution.

11. A method according to claim 9 wherein the source for the ammonium ions is selected from the group consisting of ammonia, ammonium carbonates and ammonium carbamate.

12. A method according to claim 1 wherein contacting the waste gas with said scrubbing agent is conducted in a tower embedded with inert particles and wherein the waste gas is passed upward through the tower and the emulsion is circulated downward in a rate which ensures complete wetting of inert particles.

13. A method according to claim 1 wherein contacting the waste gas with said scrubbing agent is conducted in a tower through which the waste gas is passed in an upward direction and the emulsion is sprayed into the tower from the upper opening of the tower forming a fog of said emulsion inside the tower.

14. A method according to claim 6 wherein the weight ratio of water:

organic sulfoxide in the emulsion is in the range of 10;

90 to 50;

50.