Apparatus, method, and system for concentrating adsorbable pollutants and abatement thereof

• US 6,105,365 A
• Filed: 04/08/1997
• Issued: 08/22/2000
• Est. Priority Date: 04/08/1997
• Status: Expired due to Fees

• Current Assignee: Engelhard Corporation (BASF SE)
• Original Assignee: Engelhard Corporation (BASF SE)
• Inventors: Deeba, Michel, Hochmuth, John K.
• Primary Examiner(s): Denion, Thomas
• Assistant Examiner(s): TRAN, BINH Q
• Application Number:
  US08/833,700
• Time in Patent Office: 1,232 Days
• Field of Search: 60/274, 60/287, 60/288, 60/301, 60/303, 60/311, 60/295, 60/297
• US Class Current: 60/274
• CPC Class Codes: B01D 2251/20 Reductants
• CPC Class Codes: B01D 2255/1021 Platinum
• CPC Class Codes: B01D 2255/1023 Palladium
• CPC Class Codes: B01D 2255/1025 Rhodium
• CPC Class Codes: B01D 2255/2063 Lanthanum
• CPC Class Codes: B01D 2255/2073 Manganese
• CPC Class Codes: B01D 2255/912 HC-storage component incorporated in the catalyst
• CPC Class Codes: B01D 2258/012 Diesel engines and lean burn gasoline engines
• CPC Class Codes: B01D 53/945 characterised by a specific catalyst
• CPC Class Codes: B01D 53/9481 Catalyst preceded by an adsorption device without catalytic function for temporary storage of contaminants, e.g. during cold start
• CPC Class Codes: B01D 53/949 for storing sulfur oxides
• CPC Class Codes: B01D 53/9495 Controlling the catalytic process
• CPC Class Codes: F01N 13/011 having two or more purifying devices arranged in parallel
• CPC Class Codes: F01N 2240/16 an electric heater, i.e. a resistance heater
• CPC Class Codes: F01N 3/0807 by using absorbents or adsorbents
• CPC Class Codes: F01N 3/0842 Nitrogen oxides
• CPC Class Codes: F01N 3/085 Sulfur or sulfur oxides
• CPC Class Codes: F01N 3/0871 Regulation of absorbents or adsorbents, e.g. purging by electrically controlling the supply of combustible mixture or its constituents only F02D41/0235
• CPC Class Codes: F01N 3/0878 Bypassing absorbents or adsorbents
• CPC Class Codes: F01N 3/0885 Regeneration of deteriorated absorbents or adsorbents, e.g. desulfurization of NOx traps
• CPC Class Codes: F01N 3/206 : Adding periodically or continuously substances to exhaust gases for promoting purification, e.g. catalytic material in liquid form, NOx reducing agents F01N3/2066 takes precedence
• CPC Class Codes: Y02T 10/12 : Improving ICE efficiencies

Abstract

A new method, system, and apparatus are described for the adsorption and concentration of adsorbable pollutants. The invention allows for simultaneous pollutant adsorption and pollutant concentration. The invention is particularly useful in treating the exhaust of internal combustion engines containing adsorbable pollutants which can be concentrated and then treated to form harmless effluents.

Claims

1. An apparatus for the concentration and abatement of adsorbable pollutants contained in gaseous streams comprising:

(a) an inlet conduit for receiving gases;

(b) a single means for controlling the gases from said inlet conduit and dividing such gases into a high flow stream comprising 70-99% of such gases and a low flow stream comprising 1-30% of such gases between at least a first conduit and a second conduit;

(c) a first pollutant adsorption means in fluid communication with said first conduit, said first pollutant adsorption means having inlet and outlet conduits, said first pollutant adsorption means comprising;

(i) an adsorbent selected from the group consisting of metal oxides, metal hydroxides and mixed metal oxides, (ii) catalytically effective amounts of a metal selected from the group consisting of Pt, Pd, Rh and mixtures of such metals and (iii) means to inject a reductant into the first pollutant adsorption means;

(d) a heating source for heating the first pollutant adsorption means to temperatures sufficient to desorb the adsorbed pollutants;

(e) a second pollutant adsorption means in fluid communication with said second conduit, said second pollutant adsorption means having inlet and outlet conduits, said second pollutant adsorption means comprising;

(i) an adsorbent selected from the group consisting of metal oxides, metal hydroxides and mixed metal oxides, (ii) catalytically effective amounts of a metal selected from the group consisting of Pt, Pd, Rh and mixtures of such metals and (iii) means to inject a reductant into the second pollutant adsorption means; and

(f) a heating source for heating the first and second pollutant adsorption means to temperatures sufficient to desorb the adsorbed pollutants.

2. The apparatus of claim 1, wherein the metal is selected from the group consisting of Group IA and Group IIA metals, lanthanum and manganese.

3. The apparatus of claim 1, wherein the adsorbent is selected from the group consisting of SrO, BaO, CaO, BaTiO₃, BaZrO₃, LaZrO₂, MnO₂, LaMnO_x'"'"', and mixtures of La₂ O₃ and CeO₂ with TiO₂ and ZrO₂ and where x'"'"' is an integer from 2 to 4.

4. The apparatus of claim 1, wherein the adsorbent is strontium oxide, barium oxide, or mixtures thereof.

5. The apparatus of claim 4, wherein the adsorbent contains an absorbency enhancing effective amount of platinum.

6. The apparatus of claim 1, where the metal is selected from the group of mixtures of Pt and Rh and mixtures of Pt, Rh and Pd.

7. The apparatus of claim 1, wherein the position of the metal relative to the adsorbent is an overlayer, as an underlayer, as separately provided behind the adsorbent, or as a homogenous mixture of adsorbent and metal.

8. The apparatus of claim 1 used in treating gaseous streams emanating from gasoline or diesel engines.

9. The apparatus of claim 1, wherein the single means comprises a movable and controllable semicircular slide.

10. The apparatus of claim 1, wherein the single means comprises a movable and controllable semicircular globe.

11. A method for concentrating and abating adsorbable pollutants contained in a gaseous stream comprising the steps of

(a) receiving such stream;

(b) providing a single a single means for dividing said gaseous stream into a high flow stream comprising 70-99% of such gases and a low flow stream comprising 1-30% of such gases;

(c) periodically flowing said high flow stream and said low flow stream in an alternating manner into a first pollutant adsorption means comprising;

(i) an adsorbent selected from the group consisting of metal oxides, metal hydroxides and mixed metal oxides, (ii) catalytically effective amounts of a metal selected from the group consisting of Pt, Pd, Rh and mixtures of such metals and (iii) means to inject a reductant into the first pollutant adsorption means;

(d) periodically flowing said high flow stream and said low flow stream in an alternating manner into a second pollutant adsorption means comprising;

(i) an adsorbent selected from the group consisting of metal oxides, metal hydroxides and mixed metal oxides, (ii) catalytically effective amounts of a metal selected from the group consisting of Pt, Pd, Rh and mixtures of such metals and (iii) means to inject a reductant into the pollutant adsorption means;

(e) adsorbing and abating the pollutants present in said high flow stream and low flow stream in said first and second pollution adsorption means and permitting the resultant streams to exit said first and second pollutant adsorption means;

(f) periodically regenerating said first and second pollutant adsorption means in an alternating manner by desorption of the absorbents by injection of the reductant into the first and second pollutant adsorption means and by supplying heat to the first and second pollutant adsorption means to heat such means to temperatures sufficient to desorb the means; and

(g) periodically cycling the adsorption and abatement, and regenerating functions of steps (e) and (f) between said first and second adsorption means.

12. The method of claim 11, wherein the pollutants are oxides of nitrogen or sulfur.

13. The method of claim 11, wherein the single means comprises a movable and controllable semicircular slide.

14. The method of claim 11, wherein the single means comprises a movable and controllable semicircular globe.

15. A system for the concentration and abatement of adsorbable pollutants in a gas stream which comprises:

(a) an engine which generates such gas stream and emits such gas stream through an exhaust;

(b) an inlet conduit in communication with the engine exhaust;

(c) a single means for dividing such gas stream into a high flow stream comprising 70-99% of the gases and a low flow stream comprising 1-30% of the gases between at least a first conduit and a second conduit in communication with the inlet conduit;

(d) a first pollutant adsorption means in fluid communication with said first conduit, said first pollutant adsorption means having inlet and outlet conduits, said first pollutant adsorption means comprising;

(i) an adsorbent selected from the group consisting of metal oxides, metal hydroxides and mixed metal oxides, (ii) catalytically effective amounts of a metal selected from the group consisting of Pt, Pd, Rh and mixtures of such metals and (iii) means to inject a reductant into the first pollutant adsorption means;

(e) a heating source for heating the first pollutant adsorption means to temperatures sufficient desorb the adsorbed pollutants;

(f) a second pollutant adsorption means in fluid communication with said second conduit, said second pollutant adsorption means having inlet and outlet conduits, said second pollutant adsorption means comprising;

(i) an adsorbent selected from the group consisting of metal oxides, metal hydroxides and mixed metal oxides, (ii) catalytically effective amounts of a metal selected from the group consisting of Pt, Pd, Rh and mixtures of such metals and (iii) means to inject a reductant into the second pollutant adsorption means; and

(g) a heating source for heating the first and second pollutant adsorption means to temperatures sufficient to desorb the adsorbed pollutants.

16. The system of claim 15, wherein the pollutants are oxides of nitrogen or sulfur.

17. The system of claim 15, wherein the single means comprises a movable and controllable semicircular slide.

18. The system of claim 15, wherein the single means comprises a movable and controllable semicircular globe.