Electrically heated mixer assembly for an exhaust aftertreatment system

Patent metadata

Field	Value
Publication number	US-12467396-B1
Application number	US-202418660298-A
Country	US
Kind code	B1
Filing date	May 10, 2024
Priority date	May 10, 2024
Publication date	Nov 11, 2025
Grant date	Nov 11, 2025

Abstract

A mixer assembly for mixing, in a mixing tube of an exhaust aftertreatment system, a reductant with an exhaust gas from an internal combustion engine may include a mixer and an electrically heated heating element. The mixer may be positioned in proximity to the reductant injector. The electrically heated heating element may be positioned in proximity to an impingement surface of the mixer. The reductant may directly impinge, after being injected, on the impingement surface causing the reductant to vaporize and mix with the exhaust gas forming a vaporized reductant and exhaust gas mixtures that flows along a flow path defined by the mixing tube. The vaporized reductant and exhaust gas mixture may be heated and further mixed by the electrically heated heating element.

First claim

The invention claimed is:

1. A mixer assembly for mixing a reductant with exhaust gas in a selective catalytic reduction (SCR) aftertreatment system, the SCR aftertreatment system including an exhaust conduit that permits the exhaust gas to enter a mixing tube of the SCR aftertreatment system and a reductant injector that injects the reductant into the mixing tube, the mixer assembly comprising:
an electrically heated heating element, disposed within the mixing tube and in proximity to the reductant injector that generates heat; and
a body disposed within the mixing tube parallel to and separated from the electrically heated heating element, the body being in proximity to the reductant injector, the body including an impingement surface, wherein the impingement surface is located at a position that enables the impingement surface to be heated by the heat and that enables the reductant, after being injected by the reductant injector, to directly impinge on, and be heated by, the impingement surface causing the reductant to vaporize and become a vaporized reductant that mixes with the exhaust gas forming a vaporized reductant and exhaust gas mixture that flows along a flow path defined by the mixing tube, wherein the electrically heated heating element is located within the flow path,
wherein the vaporized reductant and exhaust gas mixture is heated by the heat and further mixed by the electrically heated heating element.

2. The mixer assembly of claim 1 , further comprising:
a gas-phase mixer disposed within the mixing tube and within the flow path to enable the gas-phase mixer to further mix the vaporized reductant and exhaust gas mixture.

3. The mixer assembly of claim 1 , wherein the electrically heated heating element is heated via a power supply that provides a power output in a range of approximately 1 kilowatt to 1.5 kilowatts.

4. The mixer assembly of claim 1 , wherein the impingement surface is maintained at a constant temperature that is less than approximately 300 degrees Celsius.

5. The mixer assembly of claim 1 ,
wherein the body includes an inlet end and an outlet end,
wherein the electrically heated heating element is positioned at the inlet end of the body, and
wherein the mixer assembly further comprises:
a first aftertreatment component external to the mixing tube and in fluid communication therewith and with an exhaust conduit, the first aftertreatment component including a particulate filter and an oxidation catalyst; and
a second aftertreatment component external to the mixing tube and in fluid communication therewith and with an exhaust stack, the second aftertreatment component including a selective reduction catalyst and an ammonia oxidation catalyst.

6. The mixer assembly of claim 1 , wherein the electrically heated heating element is a spiral coil.

7. The mixer assembly of claim 1 , further comprising at least one of:
a diesel oxidation catalyst (DOC) positioned in proximity to the impingement surface, or a diesel particulate filter (DPF) positioned in proximity to the impingement surface.

8. A method for mixing, in a mixing tube of an exhaust aftertreatment system, a reductant with an exhaust gas from an internal combustion engine, the method comprising:
heating, by an electrically heated heating element parallel to and separated from an impingement surface of a mixer;
accepting the exhaust gas at a first aftertreatment component external to the mixing tube and in fluid communication therewith and with an exhaust conduit;
injecting, by a reductant injector positioned in proximity to the impingement surface, the reductant causing the reductant to directly impinge on the impingement surface, vaporize, and mix with the exhaust gas forming a vaporized reductant and exhaust gas mixtures that flows along a flow path defined by the mixing tube;
heating and mixing, by the electrically heated heating element, the vaporized reductant and exhaust gas mixture before the vaporized reductant and exhaust gas enters a gas phase mixer within the mixing tube; and
accepting the heated exhaust mixture at a second aftertreatment component external to the mixing tube and in fluid communication therewith and with an exhaust stack.

9. The method of claim 8 , further comprising:
mixing, by the gas-phase mixer provided within the flow path, the vaporized reductant and exhaust gas mixture before the vaporized reductant and exhaust gas mixture enters the second aftertreatment component.

10. The method of claim 8 , further comprising:
maintaining, by the electrically heated heating element, the impingement surface at a constant temperature that is less than approximately 300 degrees Celsius.

11. The method of claim 8 , wherein the electrically heated heating element is heated via a power supply that provides a power output in a range of approximately 1 kilowatt to 1.5 kilowatts.

12. The method of claim 8 ,
wherein the mixer includes an inlet end and an outlet end, and
wherein the electrically heated heating element is positioned at the inlet end of the mixer.

13. The method of claim 8 , wherein the electrically heated heating element is a spiral coil.

14. The method of claim 8 , further comprising:
treating the exhaust gas using at least one of:
a diesel oxidation catalyst (DOC) or a diesel particulate filer (DPF) positioned within the first aftertreatment component.

15. A selective catalytic reduction (SCR) aftertreatment system for treating exhaust gas from an internal combustion engine, the SCR aftertreatment system comprising:
a mixing tube including an inlet end, an outlet end, and an opening;
a diesel exhaust fuel (DEF) injector, communicably coupled with the opening, that injects DEF into the mixing tube; and
a mixer assembly including:
an electrically heated heating element disposed within the mixing tube and in proximity to the DEF injector;
a mixer, disposed within the mixing tube parallel to and removed from the electrically heated heating element and the DEF injector, including an impingement surface; and
an SCR catalyst positioned downstream of the electrically heated heating element and in fluid communication with and external to the mixing tube,
wherein the impingement surface is located at a position that enables the electrically heated heating element to heat the impingement surface and that enables direct impingement of the reductant, after being injected, on the impingement surface to vaporize and mix the reductant with the exhaust gas forming a vaporized reductant and exhaust gas mixture that flows along a flow path of the mixing tube, and
wherein the electrically heated heating element is positioned within the flow path to heat and further mix the reductant and exhaust gas mixture before the reductant and exhaust gas mixture enters the SCR catalyst.

16. The SCR aftertreatment system of claim 15 , further comprising:
a gas-phase mixer disposed within the mixing tube and within the flow path to enable the gas-phase mixer to further mix the vaporized reductant and exhaust gas mixture.

17. The SCR aftertreatment system of claim 15 , wherein the electrically heated heating element is heated via a power supply that provides a power output in a range of approximately 1 kilowatt to 1.5 kilowatts.

18. The SCR aftertreatment system of claim 15 , wherein the impingement surface is maintained at a constant temperature that is less than approximately 300 degrees Celsius.

19. The SCR aftertreatment system of claim 15 , further comprising at least one of:
a diesel oxidation catalyst (DOC) pos

Assignees

• Caterpillar Inc

Inventors

• Yi Yong
• Kominkiewicz Ryan James
• Neuhoff Brandon
• Johnson Anna

Classifications

• F01N2610/10

  the substance being heated, e.g. by heating tank or supply line of the added substance · CPC title

• F01N13/009

  having two or more separate purifying devices arranged in series · CPC title

• F01N3/2013

  using electric or magnetic heating means · CPC title

• F01N5/02

  the devices using heat · CPC title

• F01N3/2066

  Selective catalytic reduction [SCR] · CPC title