Thermally integrated compact aftertreatment system

Patent metadata

Field	Value
Publication number	US-10058819-B2
Application number	US-201514935125-A
Country	US
Kind code	B2
Filing date	Nov 6, 2015
Priority date	Nov 6, 2015
Publication date	Aug 28, 2018
Grant date	Aug 28, 2018

Abstract

A thermally integrated catalyst aftertreatment exhaust system includes a flow channel that directs diesel exhaust through a diesel oxidation catalyst unit that includes a diesel oxidation catalyst, by a doser that introduces DEF into the diesel exhaust, through a mixing chamber that includes a static metallic mixer coated with a DEF hydrolysis catalyst, and through an SCR unit that includes an SCR catalyst. The diesel oxidation catalyst converts a portion of diesel exhaust into water, carbon dioxide, or nitrogen dioxide. The DEF hydrolysis catalyst facilitates hydrolysis of the mixed DEF and diesel exhaust. The SCR catalyst facilitates reduction of NOx in the diesel exhaust. A first portion of the flow channel is in direct thermal contact with a second portion of the flow channel that houses the SCR unit such that heat from the diesel exhaust before the diesel exhaust reaches the doser is passed to the SCR unit.

First claim

The embodiments of the invention in which an exclusive property or privilege is claimed are defined as follows:

1. A thermally integrated catalyst aftertreatment (TICA) exhaust system, comprising:
a diesel oxidation catalyst unit comprising a diesel oxidation catalyst configured to convert a portion of diesel exhaust into one or more of water, carbon dioxide, or nitrogen dioxide;
a doser configured to introduce diesel exhaust fluid (DEF) into the diesel exhaust;
a mixing chamber configured to permit mixing of the DEF with the diesel exhaust, the mixing chamber including a static metallic mixer having a DEF hydrolysis catalyst coated thereon, wherein the DEF hydrolysis catalyst is configured to convert at least some of the DEF to NH 3 ;
a selective catalytic reduction (SCR) unit comprising an SCR catalyst configured to facilitate reduction of nitrogen oxide (NOx) in the diesel exhaust with the NH3; and
a flow channel configured to direct flow of the diesel exhaust from the diesel oxidation catalyst unit, to the doser, to the mixing chamber, and to the SCR unit, wherein a first portion of the flow channel before the diesel exhaust reaches the doser is in direct thermal contact with a second portion of the flow channel that houses the SCR unit such that heat from the diesel exhaust before the diesel exhaust reaches the doser is passed to the SCR unit,
wherein the first portion of the flow channel and the second portion of the flow channel are integrally formed together, and the integrally formed first and second portions of the flow channel are located around a perimeter of the SCR unit such that the flow channel is configured to direct flow of the diesel exhaust around the perimeter of the SCR unit before flow of the diesel exhaust is directed to the doser.

2. The TICA exhaust system of claim 1 , wherein diesel exhaust reaches the first portion of the flow channel after passing through the diesel oxidation catalyst unit.

3. The TICA exhaust system of claim 1 , wherein the SCR unit is integrated with a diesel particulate filter (DPF), wherein the integrated SCR unit and DPF are configured to filter soot and passively oxidize the diesel exhaust simultaneously with NOx reduction.

4. The TICA exhaust system of claim 1 , wherein the SCR catalyst is a binary catalyst.

5. The TICA exhaust system of claim 1 , further comprising:
a heating system configured to heat the static metallic mixer of the mixing chamber.

6. The TICA exhaust system of claim 1 , further comprising:
a supplemental SCR catalyst unit comprising an ammonia slip catalyst (ASC), wherein the flow channel is configured to direct flow of the diesel exhaust from the SCR unit to the supplemental SCR catalyst unit, wherein the ammonia slip catalyst (ASC) is configured to oxidize ammonia to nitrogen.

7. The TICA exhaust system of claim 1 , further comprising:
a supplemental SCR catalyst unit comprising an ammonia slip catalyst (ASC), wherein the flow channel is configured to direct flow of the diesel exhaust from the mixing chamber to the supplemental SCR catalyst unit and then to the SCR unit, wherein the ammonia slip catalyst (ASC) is configured to oxidize ammonia to nitrogen.

8. The TICA exhaust system of claim 1 , wherein the doser is electro-activatable, wherein electro-activation of the doser causes at least one of:
reduction of droplet size of DEF introduced into the diesel exhaust;
vaporization of the DEF to increase concentration of DEF droplets introduced into the diesel exhaust;
formation of one or both of H 2 or NH 3 reductants during dosing of the diesel exhaust;
increased uniformity of mixing of the DEF with the diesel exhaust; or
increased DEF decomposition and reduced DEF deposit formation in the mixing chamber.

9. The TICA exhaust system of claim 1 , wherein the mixing chamber comprises baffles configured to create a swirl flow pattern of the diesel exhaust before introduction of the DEF from the doser.

10. The TICA exhaust system of claim 9 , wherein the baffles are configured such that the diesel exhaust, after being mixed with DEF, continues in the swirl flow pattern into the static metallic mixer of the mixing chamber.

11. The TICA exhaust system of claim 10 , wherein at least a portion of the static metallic mixer of the mixing chamber is coated with the DEF hydrolysis catalyst, and wherein the DEF hydrolysis catalyst coated on the metallic mixer is configured to facilitate hydrolysis of the mixed DEF and diesel exhaust according to the formula:
H 2 NCONH 2 +H 2 O→2NH 3 +CO 2 .

12. The TICA exhaust system of claim 10 , wherein the metallic mixer is configured such that electrical power supplied to the metallic mixer elevates or maintains a temperature of the DEF hydrolysis catalyst.

13. The TICA exhaust system of claim 10 , further comprising:
a control unit configured to control electrical power supplied to the metallic mixer such that the temperature of the DEF hydrolysis catalyst is maintained independent of a temperature of the diesel exhaust.

14. The TICA exhaust system of claim 1 , wherein the doser and the mixing chamber are configured such that the DEF is uniformly mixed in the diesel exhaust when the mixed DEF and diesel exhaust reach the SCR unit, and wherein the SCR unit is configured to filter soot and passively oxidize the diesel exhaust simultaneously with NOx reduction.

15. The TICA exhaust system of claim 1 , wherein the SCR unit has a substrate with a porosity equal to or greater than about 65%, and wherein the SCR catalyst is applied as a washcoat to an internal surface area of the substrate.

16. The TICA exhaust system of claim 15 , wherein the substrate comprises one or more of cordierite, silicon carbide, or aluminum titanate.

17. The TICA exhaust system of claim 1 , wherein the SCR unit has a substrate with a porosity equal to or greater than about 55%, and wherein the SCR catalyst is applied as a washcoat to an internal surface area of the substrate.

18. The TICA exhaust system of claim 1 , wherein the flow channel is further configured to direct flow of the diesel exhaust from the SCR unit to a tailpipe configured to expel the diesel exhaust.

19. A method of treating diesel exhaust, comprising:
providing a thermally integrated catalyst aftertreatment (TICA) exhaust system according to claim 1 ;
directing flow of diesel exhaust through the flow channel such that the diesel exhaust passes through the diesel oxidation catalyst unit, the doser, the mixing chamber, and the selective catalytic reduction (SCR) unit;
converting, by the diesel oxidation catalyst of the diesel oxidation catalyst unit, a portion of diesel exhaust into one or more of water or carbon dioxide;
introducing, by the doser, the diesel exhaust fluid (DEF) into the diesel exhaust;
mixing, by the static metallic mixer in the mixing chamber, the DEF with the diesel exhaust, the static metallic mixer having a DEF hydrolysis catalyst coated thereon, wherein the DEF hydrolysis catalyst is configured to convert at least some of the DEF to NH 3 ;
facilitating, by the SCR catalyst of the SCR unit, reduction of nitrogen oxide (NOx) in the diesel exhaust with the NH3;
wherein the diesel exhaust passes the first portion of the flow channel before the diesel exhaust reaches the doser, wherein the second portion of the flow channel houses the SCR unit, and wherein the first portion of the flow channel is in direct thermal contact with the second portion of the flow channel such that heat from the diesel exhaust before the diesel exhaust reaches the doser is pass

Assignees

• Goffe Randal A
• Paccar Inc

Inventors

• Goffe Randal A

Classifications

• B01D2255/904

  Multiple catalysts · CPC title

• B01D53/9477 Primary

  with catalysts positioned on separate bricks, e.g. exhaust systems · CPC title

• B01D53/9495

  Controlling the catalytic process · CPC title

• F01N2240/20

  a flow director or deflector · CPC title

• F01N2610/1453

  Sprayers or atomisers; Arrangement thereof in the exhaust apparatus · CPC title