[go: up one dir, main page]

WO2012008962A1 - Anti-clogging method for exhaust gas treatment - Google Patents

Anti-clogging method for exhaust gas treatment Download PDF

Info

Publication number
WO2012008962A1
WO2012008962A1 PCT/US2010/042091 US2010042091W WO2012008962A1 WO 2012008962 A1 WO2012008962 A1 WO 2012008962A1 US 2010042091 W US2010042091 W US 2010042091W WO 2012008962 A1 WO2012008962 A1 WO 2012008962A1
Authority
WO
WIPO (PCT)
Prior art keywords
exhaust gas
gaseous ammonia
mixing chamber
gas treatment
treatment system
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Ceased
Application number
PCT/US2010/042091
Other languages
French (fr)
Inventor
Brad J. Adelman
Edward M. Derybowski
Shyam Santhanam
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
International Engine Intellectual Property Co LLC
Original Assignee
International Engine Intellectual Property Co LLC
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by International Engine Intellectual Property Co LLC filed Critical International Engine Intellectual Property Co LLC
Priority to PCT/US2010/042091 priority Critical patent/WO2012008962A1/en
Publication of WO2012008962A1 publication Critical patent/WO2012008962A1/en
Anticipated expiration legal-status Critical
Ceased legal-status Critical Current

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F01MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
    • F01NGAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR MACHINES OR ENGINES IN GENERAL; GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR INTERNAL-COMBUSTION ENGINES
    • F01N3/00Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust
    • F01N3/08Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for rendering innocuous
    • F01N3/10Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for rendering innocuous by thermal or catalytic conversion of noxious components of exhaust
    • F01N3/105General auxiliary catalysts, e.g. upstream or downstream of the main catalyst
    • F01N3/106Auxiliary oxidation catalysts
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F01MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
    • F01NGAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR MACHINES OR ENGINES IN GENERAL; GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR INTERNAL-COMBUSTION ENGINES
    • F01N3/00Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust
    • F01N3/08Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for rendering innocuous
    • F01N3/10Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for rendering innocuous by thermal or catalytic conversion of noxious components of exhaust
    • F01N3/18Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for rendering innocuous by thermal or catalytic conversion of noxious components of exhaust characterised by methods of operation; Control
    • F01N3/20Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for rendering innocuous by thermal or catalytic conversion of noxious components of exhaust characterised by methods of operation; Control specially adapted for catalytic conversion
    • F01N3/206Adding periodically or continuously substances to exhaust gases for promoting purification, e.g. catalytic material in liquid form, NOx reducing agents
    • F01N3/208Control of selective catalytic reduction [SCR], e.g. by adjusting the dosing of reducing agent
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F01MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
    • F01NGAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR MACHINES OR ENGINES IN GENERAL; GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR INTERNAL-COMBUSTION ENGINES
    • F01N2610/00Adding substances to exhaust gases
    • F01N2610/02Adding substances to exhaust gases the substance being ammonia or urea
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F01MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
    • F01NGAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR MACHINES OR ENGINES IN GENERAL; GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR INTERNAL-COMBUSTION ENGINES
    • F01N9/00Electrical control of exhaust gas treating apparatus
    • F01N9/002Electrical control of exhaust gas treating apparatus of filter regeneration
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02ATECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A50/00TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE in human health protection, e.g. against extreme weather
    • Y02A50/20Air quality improvement or preservation, e.g. vehicle emission control or emission reduction by using catalytic converters
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02TCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO TRANSPORTATION
    • Y02T10/00Road transport of goods or passengers
    • Y02T10/10Internal combustion engine [ICE] based vehicles
    • Y02T10/12Improving ICE efficiencies

Definitions

  • the present invention relates to an apparatus and method for treating and mixing diesel exhaust in a diesel exhaust system.
  • the present invention provides methods for injecting reagent into a diesel exhaust stream to reduce nitrogen oxides (NO x ) while reducing packaging space, lowering the starting reaction temperature, facilitating certification and preventing clogging of the exhaust gas system.
  • NO x nitrogen oxides
  • Diesel engines are efficient, durable and economical. Diesel exhaust, however, can harm both the environment and people. To reduce this harm, governments, such as the United States and the European Union, have proposed stricter diesel exhaust emission regulations. These environmental regulations require diesel engines to meet the same pollution emission standards as gasoline engines.
  • a lean burning engine provides improved fuel efficiency by operating with an amount of oxygen in excess of the amount necessary for complete combustion of the fuel. Such engines are said to run “lean” or on a “lean mixture.”
  • the increase in fuel efficiency is offset by the creation of undesirable pollution emissions in the form of nitrogen oxides (NO x ).
  • NO x nitrogen oxides
  • Nitrogen oxide emissions are regulated through regular emission testing requirements.
  • One method used to reduce NO x emissions from lean burn internal combustion engines is known as selective catalytic reduction. When used to reduce ⁇ x emissions from a diesel engine, selective catalytic reduction involves injecting atomized urea into the exhaust stream of the engine in relation to one or more selected engine operational parameters and running the stream through a reactor containing a catalyst.
  • urea must first be reacted to form ammonia (NH 3 ) before it can reduce the NO x emissions. Accordingly, packaging length and weight must be great enough to accommodate the intermediate reaction. Further, while NH 3 reacts at a temperature of about 150° C, urea needs to achieve about 180° C to begin reaction.
  • the method comprises the steps of fluidly coupling an exhaust gas treatment system package to an engine exhaust gas system, and then continuously injecting gaseous ammonia into the exhaust gas treatment system package.
  • the exhaust gas treatment system package comprises a mixing chamber for reacting gaseous ammonia with vehicle exhaust gas to reduce NO x in the exhaust gas, a diesel oxidation catalyst (DOC), a diesel particulate filter (DPF), a NO x slip catalyst (NSC) canister, an injection port for adding gaseous ammonia to the package, and a solid ammonia source for supplying gaseous ammonia to the injection port.
  • DOC, DPF, NSC and mixing chamber are all fluidly coupled together.
  • the exhaust gas treatment system package of the engine exhaust gas system is fluidly coupled to the emission diagnostic apparatus, then gaseous ammonia is injected into the exhaust gas treatment system package. Reaction of the gaseous ammonia with engine exhaust gas is begun at a temperature of less than about 180° C, preferably about 150° C, and then the reaction of the gaseous ammonia with the engine exhaust gas is continued during operation of the vehicle.
  • the reaction temperature is about 150° C and the exhaust gas treatment system package includes a mixing chamber for reacting gaseous ammonia with vehicle exhaust gas to reduce NO x in the exhaust gas.
  • FIG. 1 is a schematic illustrating a typical aqueous urea mixer/injector device for a diesel exhaust system
  • FIG. 2 is a schematic illustrating an embodiment of a mixer/NH 3 injection device of the present invention for a diesel exhaust system
  • FIG. 3 is a schematic illustrating another embodiment of a mixer/NH 3 injection device of the present invention in a diesel exhaust system.
  • FIG. 1 there is illustrated a typical exhaust gas treatment system package 110.
  • Exhaust gas is discharged from the diesel engine 100, through conduit such as exhaust piping to the exhaust gas treatment system 1 10.
  • the exhaust gas treatment system 1 10 typically consists of, in order of exhaust gas flow, a diesel oxidation catalyst (DOC) 112, a diesel particulate filter (DPF) 1 14, a mixing chamber 1 16, and a O x slip catalyst (NSC) 1 18.
  • DOC 112, DPF 1 14 and NSC 1 18 are additional exhaust gas treatment structures present in most diesel exhaust gas treatment systems and which form no part of the present system 10. Such structures will be generally referenced herein and identified in the drawing figures but, as each of these additional exhaust treatment structures is commonly understood by those skilled in the art, a detailed discussion of each is avoided for the purpose of focusing discussion on the system 10 as set forth in the appended claims.
  • the mixing chamber 1 16 is shown to include a connection pipe 120 with an injector 122 at the upstream end where aqueous urea is injected into a laminar diesel exhaust flow as it is discharged from the DOC 112 and DPF 114.
  • the urea/exhaust stream proceeds through the mixing chamber 116 where the urea is converted to a gaseous ammonia which is capable of reacting with the NO x of the exhaust gas.
  • a substantial length of pipe 120 is needed to allow for adequate mixing of the two components before the flow enters the NSC 1 18.
  • the mixing chamber 1 16 adds packaging length and weight to the diesel exhaust system 100 which might otherwise be used for other after-treatment substrates.
  • FIGS. 2 - 3 there is illustrated a diesel engine exhaust gas treatment system, generally designated by the numeral 10.
  • the system 10 is shown in two distinct exhaust gas treatment configurations.
  • FIG. 2 illustrates an exhaust gas configuration similar to that of FIG. 1 where the downstream order of components is DOC 12, then DPF 14 and NSC 18 sandwiched about a mixing chamber 216.
  • FIG. 3 illustrates a configuration where the NSC 18 is on the DPF 14— i.e., NO x slip catalyst on diesel particulate filter (NPF) 19— sandwiching the mixing chamber 216 with the DOC 12.
  • NPF diesel particulate filter
  • Other configurations may exist in which the mixing chamber 216 is moved up or downstream in the exhaust flow.
  • the packaging space required for the mixing chamber 216 is substantially reduced from that required for a typical mixing chamber 116 illustrated in FIG. 1.
  • the reduced packaging length is made possible by the injection of gaseous ammonia (NH 3 ) into the mixing chamber, as opposed to injecting aqueous urea which must then react for a length of the mixing chamber 216 to convert to NH 3 .
  • the gaseous ammonia reacts with the exhaust gas to reduce NO x at a lower temperature than is required to convert the urea to gaseous ammonia. Accordingly, particularly after a cold start, the reduction of NO x in the exhaust stream begins much sooner with the present system.
  • FTP Federal Test Procedure
  • improved performance in one area allows for lower performance in other areas without failing the FTP certification.
  • the "cold cycle” component accounts for one-seventh of the overall test while the "hot cycle” component results make up the remaining six-sevenths of the test.
  • the improved lower temperature reaction time in NO x emission control as a result of injecting gaseous ammonia into the exhaust stream, results in improved "cold cycle” test results over prior urea systems.
  • the improvements in the "cold cycle” component provide greater flexibility in the more harsh "hot cycle” component of the test procedure.
  • Successful certification of diesel engine vehicles using the present NO x emission control system 10 is increased as a result.
  • Clogging/blockage and pressure drops in urea systems are also a problem overcome by the present exhaust treatment system 10.
  • the very nature of an exhaust system results in a considerable amount of soot being deposited in various nooks, recesses, corners and other such areas of the system.
  • the injection of liquid urea can mix with the accumulated soot and cake in passages to cause clogging/blockage and critical pressure drops which may result in backflow of exhaust. If not cleaned from the exhaust system, such accumulated caking can increase weight within the exhaust system.
  • a method comprises fluidly coupling an exhaust gas treatment system package to an engine exhaust gas system, and then continuously injecting gaseous ammonia into the exhaust gas treatment system package.
  • the exhaust gas treatment system package comprises a mixing chamber for reacting gaseous ammonia with vehicle exhaust gas to reduce NO x in the exhaust gas, a diesel oxidation catalyst (DOC), a diesel particulate filter (DPF), a NO x slip catalyst (NSC) canister, an injection port for adding gaseous ammonia to the package, and a solid ammonia source for supplying gaseous ammonia to the injection port.
  • the DOC, DPF, NSC and mixing chamber are all fluidly coupled together.
  • the present mixing chamber 216 is comprised of a housing 20 defining a volume 25, an injection tube 22 fed by an exterior injector boss 30 coupled to a supply (not shown), and a mixer 24.
  • FIGS. 2 and 3 illustrate the diameter of the housing 20 (approx. 12 inches (30.5 cm)) is substantially equal to that of the surrounding exhaust gas treatment structures— e.g., DPF 14 and NSC 18.
  • the need for reducers 123 (FIG. 1) is eliminated, further reducing the packaging size of the entire diesel exhaust treatment system.
  • Reagent e.g., gaseous NH 3
  • injection points 23 immediately enters the turbulent diesel exhaust stream as it moves toward the chamber exit 35 (FIGS. 2 and 3).
  • a relatively short distance is needed to provide the necessary mixing time to create a homogonous reagent/diesel exhaust.
  • the homogenous mixture is then exited from the mixing chamber 25 into one of either the NSC 18 (FIG. 2) or the NPF 19 (FIG. 3) for further treatment.

Landscapes

  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Health & Medical Sciences (AREA)
  • Toxicology (AREA)
  • Combustion & Propulsion (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Exhaust Gas After Treatment (AREA)

Abstract

An improved method for preventing clogging in an exhaust gas treatment system for a diesel-engine vehicle is disclosed. An embodiment of the method includes the steps of fluidly coupling an exhaust gas treatment system package to an engine exhaust gas system, and then continuously injecting gaseous ammonia into the exhaust gas treatment system package. Preferably, the exhaust gas treatment system package comprises a mixing chamber for reacting gaseous ammonia with vehicle exhaust gas to reduce NOx in the exhaust gas, a diesel oxidation catalyst (DOC), a diesel particulate filter (DPF), a NOx slip catalyst (NSC) canister, an injection port for adding gaseous ammonia to the package, and a solid ammonia source for supplying gaseous ammonia to the injection port. In an embodiment of the invention, the DOC, DPF, NSC and mixing chamber are all fluidly coupled together.

Description

ANTI-CLOGGING METHOD FOR EXHAUST GAS TREATMENT
TECHNICAL FIELD OF THE INVENTION
[0001] The present invention relates to an apparatus and method for treating and mixing diesel exhaust in a diesel exhaust system. Particularly, the present invention provides methods for injecting reagent into a diesel exhaust stream to reduce nitrogen oxides (NOx) while reducing packaging space, lowering the starting reaction temperature, facilitating certification and preventing clogging of the exhaust gas system.
BACKGROUND OF THE INVENTION
[0002] Diesel engines are efficient, durable and economical. Diesel exhaust, however, can harm both the environment and people. To reduce this harm, governments, such as the United States and the European Union, have proposed stricter diesel exhaust emission regulations. These environmental regulations require diesel engines to meet the same pollution emission standards as gasoline engines.
[0003] Typically, to meet such regulations and standards, diesel engine systems require equipment additions and modifications. Additional equipment can often lead to additional weight and/or additional packaging length.
[0004] For example, a lean burning engine provides improved fuel efficiency by operating with an amount of oxygen in excess of the amount necessary for complete combustion of the fuel. Such engines are said to run "lean" or on a "lean mixture." However, the increase in fuel efficiency is offset by the creation of undesirable pollution emissions in the form of nitrogen oxides (NOx). Nitrogen oxide emissions are regulated through regular emission testing requirements. One method used to reduce NOx emissions from lean burn internal combustion engines is known as selective catalytic reduction. When used to reduce Οx emissions from a diesel engine, selective catalytic reduction involves injecting atomized urea into the exhaust stream of the engine in relation to one or more selected engine operational parameters and running the stream through a reactor containing a catalyst.
[0005] However, selective catalytic reduction and the use of aqueous urea involve many disadvantages. For example, the urea must first be reacted to form ammonia (NH3) before it can reduce the NOx emissions. Accordingly, packaging length and weight must be great enough to accommodate the intermediate reaction. Further, while NH3 reacts at a temperature of about 150° C, urea needs to achieve about 180° C to begin reaction.
Accordingly, reduction of NOx is unnecessarily delayed by the intermediate reaction converting urea to ammonia. The higher required reaction temperature of a urea system may also lead to more difficult engine certification under any Federal Test Procedure (FTP) having a cold cycle component.
[0006] Still another disadvantage of aqueous urea exhaust treatment is the propensity for clogging of the exhaust stream, causing pressure drops which can foul system sensors. When combined with soot prevalent in an exhaust gas stream, the gas/liquid urea will form blockages and add excess weight in the treatment canisters. Finally, the highly corrosiveness and poor lubricity of aqueous urea make it an unsuitable exhaust gas treatment component.
[0007] It would be advantageous to provide methods and apparatus for addressing the regulations and standards without adding weight or length to an already complex diesel exhaust system. Accordingly, it would be advantageous to provide methods and apparatus for injecting a Ox reducing reagent into the diesel exhaust stream of a lean burn engine where little or no added weight or packaging length is required. Further, it would be advantageous to provide an exhaust gas treatment system which improves emission certification and facilitates the reduction of clogging.
[0008] The methods and apparatus of the present invention provide the foregoing and other advantages. SUMMARY OF THE INVENTION
[0009] There is disclosed herein an improved method for preventing clogging in exhaust gas treatment systems used on diesel-engine vehicles.
[0010] Generally speaking, the method comprises the steps of fluidly coupling an exhaust gas treatment system package to an engine exhaust gas system, and then continuously injecting gaseous ammonia into the exhaust gas treatment system package. Preferably, the exhaust gas treatment system package comprises a mixing chamber for reacting gaseous ammonia with vehicle exhaust gas to reduce NOx in the exhaust gas, a diesel oxidation catalyst (DOC), a diesel particulate filter (DPF), a NOx slip catalyst (NSC) canister, an injection port for adding gaseous ammonia to the package, and a solid ammonia source for supplying gaseous ammonia to the injection port. In an embodiment of the invention, the DOC, DPF, NSC and mixing chamber are all fluidly coupled together.
[0011] In an aspect of the invention, the exhaust gas treatment system package of the engine exhaust gas system is fluidly coupled to the emission diagnostic apparatus, then gaseous ammonia is injected into the exhaust gas treatment system package. Reaction of the gaseous ammonia with engine exhaust gas is begun at a temperature of less than about 180° C, preferably about 150° C, and then the reaction of the gaseous ammonia with the engine exhaust gas is continued during operation of the vehicle.
[0012] In an embodiment of the present method, the reaction temperature is about 150° C and the exhaust gas treatment system package includes a mixing chamber for reacting gaseous ammonia with vehicle exhaust gas to reduce NOx in the exhaust gas.
[0013] These and other aspects of the invention may be understood more readily from the following description and the appended drawings. BRIEF DESCRIPTION OF THE DRAWINGS
[0014] For the purpose of facilitating an understanding of the subject matter sought to be protected, there are illustrated in the accompanying drawings embodiments thereof, from an inspection of which, when considered in connection with the following description, the subject matter sought to be protected, its construction and operation, and many of its advantages should be readily understood and appreciated.
[0015] FIG. 1 is a schematic illustrating a typical aqueous urea mixer/injector device for a diesel exhaust system;
[0016] FIG. 2 is a schematic illustrating an embodiment of a mixer/NH3 injection device of the present invention for a diesel exhaust system; and
[0017] FIG. 3 is a schematic illustrating another embodiment of a mixer/NH3 injection device of the present invention in a diesel exhaust system.
DETAILED DESCRIPTION OF THE INVENTION
[0018] While this invention is susceptible of embodiments in many different forms, there is shown in the drawings and will herein be described in detail a preferred embodiment of the invention with the understanding that the present disclosure is to be considered as an exemplification of the principles of the invention and is not intended to limit the broad aspect of the invention to embodiments illustrated.
[0019] Referring to FIG. 1, there is illustrated a typical exhaust gas treatment system package 110. Exhaust gas is discharged from the diesel engine 100, through conduit such as exhaust piping to the exhaust gas treatment system 1 10. The exhaust gas treatment system 1 10 typically consists of, in order of exhaust gas flow, a diesel oxidation catalyst (DOC) 112, a diesel particulate filter (DPF) 1 14, a mixing chamber 1 16, and a Ox slip catalyst (NSC) 1 18. The DOC 112, DPF 1 14 and NSC 1 18 are additional exhaust gas treatment structures present in most diesel exhaust gas treatment systems and which form no part of the present system 10. Such structures will be generally referenced herein and identified in the drawing figures but, as each of these additional exhaust treatment structures is commonly understood by those skilled in the art, a detailed discussion of each is avoided for the purpose of focusing discussion on the system 10 as set forth in the appended claims.
[0020] The mixing chamber 1 16 is shown to include a connection pipe 120 with an injector 122 at the upstream end where aqueous urea is injected into a laminar diesel exhaust flow as it is discharged from the DOC 112 and DPF 114. The urea/exhaust stream proceeds through the mixing chamber 116 where the urea is converted to a gaseous ammonia which is capable of reacting with the NOx of the exhaust gas. A substantial length of pipe 120 is needed to allow for adequate mixing of the two components before the flow enters the NSC 1 18. As such, the mixing chamber 1 16 adds packaging length and weight to the diesel exhaust system 100 which might otherwise be used for other after-treatment substrates.
[0021] Referring to FIGS. 2 - 3, there is illustrated a diesel engine exhaust gas treatment system, generally designated by the numeral 10. The system 10 is shown in two distinct exhaust gas treatment configurations. FIG. 2 illustrates an exhaust gas configuration similar to that of FIG. 1 where the downstream order of components is DOC 12, then DPF 14 and NSC 18 sandwiched about a mixing chamber 216. Alternatively, FIG. 3 illustrates a configuration where the NSC 18 is on the DPF 14— i.e., NOx slip catalyst on diesel particulate filter (NPF) 19— sandwiching the mixing chamber 216 with the DOC 12. Other configurations may exist in which the mixing chamber 216 is moved up or downstream in the exhaust flow.
[0022] Regardless of the specific configuration, it is clear from examination of FIGS. 2 and 3 that the packaging space required for the mixing chamber 216 is substantially reduced from that required for a typical mixing chamber 116 illustrated in FIG. 1. The reduced packaging length is made possible by the injection of gaseous ammonia (NH3) into the mixing chamber, as opposed to injecting aqueous urea which must then react for a length of the mixing chamber 216 to convert to NH3. Further, the gaseous ammonia reacts with the exhaust gas to reduce NOx at a lower temperature than is required to convert the urea to gaseous ammonia. Accordingly, particularly after a cold start, the reduction of NOx in the exhaust stream begins much sooner with the present system.
[0023] Another benefit of the lower temperature NOx reduction relates to Federal Test Procedure (FTP) for emissions on diesel-engine vehicles. FTP certifications are typically cumulative and often have a "cold cycle" component as part of the test procedure.
Accordingly, improved performance in one area allows for lower performance in other areas without failing the FTP certification. For example, in one such FTP engine emission certification process, the "cold cycle" component accounts for one-seventh of the overall test while the "hot cycle" component results make up the remaining six-sevenths of the test. As noted above, the improved lower temperature reaction time in NOx emission control as a result of injecting gaseous ammonia into the exhaust stream, results in improved "cold cycle" test results over prior urea systems. As the test results are cumulative, the improvements in the "cold cycle" component provide greater flexibility in the more harsh "hot cycle" component of the test procedure. Successful certification of diesel engine vehicles using the present NOx emission control system 10 is increased as a result.
[0024] In fact, improved "cold cycle" testing results provide the ability to use less NOx washcoat in exhaust after-treatment canisters. The use of less washcoat is a cost savings over prior art systems.
[0025] Clogging/blockage and pressure drops in urea systems are also a problem overcome by the present exhaust treatment system 10. The very nature of an exhaust system results in a considerable amount of soot being deposited in various nooks, recesses, corners and other such areas of the system. The injection of liquid urea can mix with the accumulated soot and cake in passages to cause clogging/blockage and critical pressure drops which may result in backflow of exhaust. If not cleaned from the exhaust system, such accumulated caking can increase weight within the exhaust system.
[0026] However, with the injection of gaseous ammonia there is no increased risk of caking with the accumulated soot. Instead it is just the contrary, as the ammonia gas entrains the soot and carries it from the present exhaust system 10. Decreased pressure drops, decreased clogging, and decreased weight are the positive result of the ammonia gas injection.
[0027] To prevent clogging, a method comprises fluidly coupling an exhaust gas treatment system package to an engine exhaust gas system, and then continuously injecting gaseous ammonia into the exhaust gas treatment system package. Preferably, the exhaust gas treatment system package comprises a mixing chamber for reacting gaseous ammonia with vehicle exhaust gas to reduce NOx in the exhaust gas, a diesel oxidation catalyst (DOC), a diesel particulate filter (DPF), a NOx slip catalyst (NSC) canister, an injection port for adding gaseous ammonia to the package, and a solid ammonia source for supplying gaseous ammonia to the injection port. In an embodiment of the invention, the DOC, DPF, NSC and mixing chamber are all fluidly coupled together.
[0028] Structurally speaking, the present mixing chamber 216 is comprised of a housing 20 defining a volume 25, an injection tube 22 fed by an exterior injector boss 30 coupled to a supply (not shown), and a mixer 24. FIGS. 2 and 3 illustrate the diameter of the housing 20 (approx. 12 inches (30.5 cm)) is substantially equal to that of the surrounding exhaust gas treatment structures— e.g., DPF 14 and NSC 18. By providing the larger diameter system housing 20 (vs. narrow connecting pipe 120), the need for reducers 123 (FIG. 1) is eliminated, further reducing the packaging size of the entire diesel exhaust treatment system. [0029] Reagent (e.g., gaseous NH3) discharged from injection points 23 immediately enters the turbulent diesel exhaust stream as it moves toward the chamber exit 35 (FIGS. 2 and 3). As stated above, a relatively short distance is needed to provide the necessary mixing time to create a homogonous reagent/diesel exhaust.
[0030] The homogenous mixture is then exited from the mixing chamber 25 into one of either the NSC 18 (FIG. 2) or the NPF 19 (FIG. 3) for further treatment.
[0031] The matter set forth in the foregoing description and accompanying drawings is offered by way of illustration only and not as a limitation. While particular embodiments have been shown and described, it will be apparent to those skilled in the art that changes and modifications may be made without departing from the broader aspects of applicants' contribution. The actual scope of the protection sought is intended to be defined in the following claims when viewed in their proper perspective based on the prior art.

Claims

CLAIMS What is claimed is:
1. A method for minimizing (preventing) clogging in a diesel-engine exhaust gas treatment system, the method comprising the steps of:
fluidly coupling an exhaust gas treatment system package to an engine exhaust gas system, the exhaust gas treatment system package comprising:
a mixing chamber for reacting gaseous ammonia with vehicle exhaust gas to reduce NOx in the exhaust gas;
a diesel oxidation catalyst (DOC);
a diesel particulate filter (DPF);
a NOx slip catalyst (NSC) canister, wherein the DOC, DPF, NSC and mixing chamber are all fluidly coupled together;
an injection port for adding gaseous ammonia to the package; and a source for supplying gaseous ammonia to the injection port; continuously injecting gaseous ammonia into the exhaust gas treatment system package.
2. The method of Claim 1, wherein the gaseous ammonia is injected into the mixing chamber.
3. The method of Claim 2, wherein the gaseous ammonia source comprises a tank of solid ammonium.
4. The method of Claim 1 , wherein the mixing chamber volume is smaller than a volume required for reacting liquid urea with exhaust gas to reduce NOx.
5. The method of Claim 1, wherein the mixing chamber is positioned between the diesel particulate filter (DPF) and the NOx slip catalyst canister.
6. The method of Claim 1 , wherein the mixing chamber achieves an initial temperature at which reaction between the exhaust gas and gaseous ammonia occurs, and the initial reaction temperature is about 150° C.
7. The method of Claim 3, wherein the step of injecting gaseous ammonia occurs in the mixing chamber.
PCT/US2010/042091 2010-07-15 2010-07-15 Anti-clogging method for exhaust gas treatment Ceased WO2012008962A1 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
PCT/US2010/042091 WO2012008962A1 (en) 2010-07-15 2010-07-15 Anti-clogging method for exhaust gas treatment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
PCT/US2010/042091 WO2012008962A1 (en) 2010-07-15 2010-07-15 Anti-clogging method for exhaust gas treatment

Publications (1)

Publication Number Publication Date
WO2012008962A1 true WO2012008962A1 (en) 2012-01-19

Family

ID=45469731

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/US2010/042091 Ceased WO2012008962A1 (en) 2010-07-15 2010-07-15 Anti-clogging method for exhaust gas treatment

Country Status (1)

Country Link
WO (1) WO2012008962A1 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2017092839A1 (en) * 2015-12-02 2017-06-08 Daimler Ag Exhaust gas aftertreatment method and exhaust gas system

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20030213234A1 (en) * 2002-05-07 2003-11-20 Werner Funk Emission control system
US20070224093A1 (en) * 2006-03-24 2007-09-27 Ngk Insulators, Ltd. Exhaust gas purifying system
US20080132405A1 (en) * 2003-08-05 2008-06-05 Joseph Allan Patchett Catalyzed SCR Filter and Emission Treatment System

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20030213234A1 (en) * 2002-05-07 2003-11-20 Werner Funk Emission control system
US20080132405A1 (en) * 2003-08-05 2008-06-05 Joseph Allan Patchett Catalyzed SCR Filter and Emission Treatment System
US20070224093A1 (en) * 2006-03-24 2007-09-27 Ngk Insulators, Ltd. Exhaust gas purifying system

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2017092839A1 (en) * 2015-12-02 2017-06-08 Daimler Ag Exhaust gas aftertreatment method and exhaust gas system

Similar Documents

Publication Publication Date Title
US8122712B2 (en) Exhaust system with improved NOX emission control
CN101839162B (en) Diagnostic systems and methods for selective catalytic reduction (scr) systems based on nox sensor feedback
US20150064072A1 (en) Emissions Cleaning Module
US20090056319A1 (en) Exhaust Aftertreatment System with Pre-Catalysis
US20110219745A1 (en) Method and apparatus for gaseous mixing in a diesel exhaust system
EP2354485A1 (en) Exhaust system for compression-ignition engine
US20110225969A1 (en) Compressor bypass to exhaust for particulate trap regeneration
GB2465151A (en) Engine exhaust treatment unit
EP2813678A1 (en) An exhaust gas sampling device
US20220162971A1 (en) Aftertreatment system and method of treating exhaust gases
US8220252B2 (en) Exhaust gas emissions reactor and method of treating exhaust gas
CN214304012U (en) Exhaust gas aftertreatment device for diesel engine and vehicle
US20130239552A1 (en) Control system for reducing nitrous oxide ("n2o") after selective catalytic reduction ("scr") device light-off
WO2012008948A1 (en) PACKAGING OF DOC+DFP/NH3(g) MIXER/NOx SLIP CATALYST IN EXHAUST SYSTEM
CN114575969A (en) Vehicle exhaust gas treatment system and vehicle
Kowatari et al. A study of a new aftertreatment system (1): a new dosing device for enhancing low temperature performance of urea-SCR
CN114941559B (en) Exhaust gas aftertreatment system
US20250305431A1 (en) Systems including a hydrogen internal combustion engine and aftertreatment system
US11421572B2 (en) Exhaust gas aftertreatment system with a selective catalytic reduction catalyst member upstream of a particulate filter
US20240287928A1 (en) Exhaust gas aftertreatment system
CN211950638U (en) Selective non-catalytic reduction device with 40% methylamine water solution as reducing agent
WO2012008962A1 (en) Anti-clogging method for exhaust gas treatment
US20130216459A1 (en) Lower temperature mixing zone for nh3
US11834978B2 (en) Systems and methods for decreasing time to reach light-off temperature
Zhan et al. Development of a novel device to improve urea evaporation, mixing and distribution to enhance SCR performance

Legal Events

Date Code Title Description
121 Ep: the epo has been informed by wipo that ep was designated in this application

Ref document number: 10854827

Country of ref document: EP

Kind code of ref document: A1

NENP Non-entry into the national phase

Ref country code: DE

122 Ep: pct application non-entry in european phase

Ref document number: 10854827

Country of ref document: EP

Kind code of ref document: A1