US20020001554A1 - Method of reducing NOx emissions using a fluid-cooled injector - Google Patents

Method of reducing NOx emissions using a fluid-cooled injector Download PDF

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US20020001554A1
US20020001554A1 US09/901,180 US90118001A US2002001554A1 US 20020001554 A1 US20020001554 A1 US 20020001554A1 US 90118001 A US90118001 A US 90118001A US 2002001554 A1 US2002001554 A1 US 2002001554A1
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reagent
injector
stream
fluid
orifice
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US09/901,180
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Richard Czarnik
Jeffrey DiCarlo
Curtis Knapper
Thomas Simard
Theodore Tarabulski
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    • 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 ; Methods of operation or control of catalytic converters
    • F01N3/2066Selective catalytic reduction [SCR]
    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61PSPECIFIC THERAPEUTIC ACTIVITY OF CHEMICAL COMPOUNDS OR MEDICINAL PREPARATIONS
    • A61P5/00Drugs for disorders of the endocrine system
    • A61P5/06Drugs for disorders of the endocrine system of the anterior pituitary hormones, e.g. TSH, ACTH, FSH, LH, PRL, GH
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D53/00Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/34Chemical or biological purification of waste gases
    • B01D53/74General processes for purification of waste gases; Apparatus or devices specially adapted therefor
    • B01D53/86Catalytic processes
    • B01D53/8621Removing nitrogen compounds
    • B01D53/8625Nitrogen oxides
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D53/00Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/34Chemical or biological purification of waste gases
    • B01D53/74General processes for purification of waste gases; Apparatus or devices specially adapted therefor
    • B01D53/86Catalytic processes
    • B01D53/90Injecting reactants
    • 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
    • F01N2260/00Exhaust treating devices having provisions not otherwise provided for
    • F01N2260/02Exhaust treating devices having provisions not otherwise provided for for cooling the device
    • F01N2260/024Exhaust treating devices having provisions not otherwise provided for for cooling the device using a liquid
    • 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
    • F01N2610/00Adding substances to exhaust gases
    • F01N2610/11Adding substances to exhaust gases the substance or part of the dosing system being cooled
    • 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
    • F01N2610/14Arrangements for the supply of substances, e.g. conduits
    • F01N2610/1453Sprayers or atomisers; Arrangement thereof in the exhaust apparatus
    • 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
    • Y02CCAPTURE, STORAGE, SEQUESTRATION OR DISPOSAL OF GREENHOUSE GASES [GHG]
    • Y02C20/00Capture or disposal of greenhouse gases
    • Y02C20/10Capture or disposal of greenhouse gases of nitrous oxide (N2O)
    • 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
    • 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
    • Y10TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10TTECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
    • Y10T137/00Fluid handling
    • Y10T137/6416With heating or cooling of the system
    • Y10T137/6552With diversion of part of fluid to heat or cool the device or its contents
    • 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
    • Y10TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10TTECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
    • Y10T137/00Fluid handling
    • Y10T137/6416With heating or cooling of the system
    • Y10T137/6579Circulating fluid in heat exchange relationship

Definitions

  • This invention relates to methods for reducing NO x emissions from internal combustion engines and especially to methods using fluid-cooled injectors wherein the fluid is a liquid reagent and a portion of the reagent is injected as an atomized liquid reagent into the exhaust gas stream of an internal combustion engine.
  • SCR selective catalytic reduction
  • a method used to reduce NO x emissions from internal combustion engines involves injecting an atomized reagent into the exhaust stream of the engine in relation to one or more selected engine operational parameters, such as exhaust gas temperature, engine rpm or engine load as measured by engine fuel flow, turbo boost pressure or exhaust NO x mass flow.
  • the reagent/exhaust gas mixture is passed through a reactor containing a catalyst, such as, for example, activated carbon or metals, such as platinum, vanadium or tungsten, which are capable of reducing the NO x concentration in the presence of the reagent.
  • a catalyst such as, for example, activated carbon or metals, such as platinum, vanadium or tungsten
  • An aqueous solution of urea is known to be an effective reagent in SCR systems for diesel engines but suffers several disadvantages.
  • Urea is highly corrosive and tends to attack mechanical components of the SCR system, such as the injectors used to inject the urea mixture into the exhaust gas stream.
  • Urea also tends to solidify upon prolonged exposure to elevated temperatures, such as encountered in diesel exhaust systems.
  • Solidified urea tends to accumulate in the narrow passageways and orifice openings typically found in injectors. The solidified urea fouls moving parts of the injector and clogs any openings, thus, rendering the injector unusable.
  • aqueous urea is a poor lubricant. This characteristic adversely affects moving parts within the injector and requires that special fits, clearances and tolerances be employed between relatively moving parts within an injector.
  • the method according to the invention concerns reducing emissions of oxides of nitrogen from a combustion process using a temperature sensitive liquid reagent injected into a stream of exhaust gases from the combustion process and passing the exhaust gases and the reagent through a catalytic reactor which reduces the oxides of nitrogen in the presence of the reagent.
  • the steps of the method include providing an injector having an orifice for atomizing the liquid reagent; positioning a portion of the injector having the orifice within the stream of exhaust gases; cooling the injector by continuously circulating the reagent therethrough, thereby keeping both the injector and the reagent within the injector below a critical temperature at which the reagent will solidify; and injecting a portion of the reagent into the exhaust stream upstream of the reactor.
  • the reagent is preferably an aqueous urea solution which is injected into the stream of exhaust gases in proportion to selected engine operating parameters.
  • the urea has a concentration between about 25% and about 35%.
  • the reagent is circulated continuously at a rate which will keep its temperature below about 140° C. and preferably below about 95° C.
  • the invention also provides an injector for delivery of a fluid into a stream of hot gas, the injector being designed to operate effectively with a corrosive, temperature-sensitive reagent, such as aqueous urea.
  • the injector is mounted on an exhaust conduit of an internal combustion engine where it injects the reagent into the exhaust gas stream.
  • the injector comprises a valve and a means for actuating the valve between a closed position and an open position.
  • Acceptable actuating means include, for example, a solenoid-type actuator.
  • the components of the valve exposed to extreme heat or corrosive reagents like urea are made of a corrosion resistant material such as stainless steel.
  • the valve includes an orifice through which the reagent is expelled when the valve is in the open position. Regardless of the state of the valve (i.e., open or closed), the reagent is continuously circulated through it when the system is in operation, at least a portion of the circulating reagent being expelled when the valve is opened.
  • the circulation of the reagent cools the valve and minimizes the dwell time of the reagent within the valve, thereby minimizing exposure of the reagent to heat and the creation of urea deposits.
  • aqueous urea for example, can be effectively used with such an injector without the characteristic fouling and clogging of the injector.
  • Means independent of the valve actuating means are provided for continuously circulating the reagent through the valve, as described in detail below.
  • the valve comprises a valve body which has an elongated cylindrical chamber therein in fluid communication with the orifice.
  • a valve seat is positioned within the chamber surrounding the orifice.
  • An elongated valve plunger is slidably mounted within the chamber. One end of the plunger is sealingly interengagable with the valve seat to close the orifice.
  • the plunger is connected with the actuating means and is movable from the closed position where the plunger end sealingly engages the valve seat and the open position where the plunger end is removed from sealing interengagement with the valve seat to open the orifice.
  • the means for independently circulating fluid through the valve comprises a portion of the plunger which is arranged adjacent to the plunger end. This portion of the plunger has a diameter less than the chamber diameter and forms an annular fluid space or passageway within the valve adjacent to the valve seat and the orifice.
  • the annular passageway thus, allows for both the continuous circulation of fluid through the valve and the expelling of a portion of the fluid through the orifice when the valve is in the open position.
  • the independent fluid circulating means further comprises a fluid inlet and a fluid outlet arranged within the valve body in fluid communication with the annular passageway.
  • Fluid such as the aqueous urea reagent
  • the valve plunger is moved to the open position, and a portion of the fluid is expelled from the chamber through the orifice.
  • a heat shield is preferably interposed between the valve and the stream of hot gas.
  • the heat shield has an aperture which is aligned with the orifice.
  • the heat shield aperture allows fluid expelled from the valve to pass through the heat shield and into the hot gas stream.
  • the heat shield preferably comprises a metal plate and a layer of insulating material interposed between the plate and the valve. The heat shield aperture passes through both the layer of insulating material, as well as the metal plate.
  • an atomizing hook is preferably mounted on the valve.
  • the atomizing hook has an end surface which is positioned in a spaced apart relation with the orifice. Liquid reagent expelled through the orifice impinges on the hook end surface where further atomization of the reagent occurs.
  • the shape and position of the hook end surface directly affect the dispersion characteristics of the injected reagent.
  • FIG. 1 shows a schematic diagram of a pollution emission control system using an injector according to the invention
  • FIG. 2 shows a longitudinal cross-sectional view of an injector according to the invention.
  • FIG. 3 shows a side view of the valve body of the injector according to the invention.
  • FIG. 1 illustrates a pollution control system as might be used to reduce NO x emissions from the exhaust of a diesel engine 3 .
  • the system includes an engine exhaust conduit 4 in fluid communication with a catalytic reactor 5 , a reagent reservoir 6 holding reagent 7 , a central processing unit 8 and an injector 10 .
  • Injector 10 is mounted on exhaust conduit 4 and fed reagent, for example, a solution of aqueous urea via supply line 9 extending from reservoir 7 to the injector.
  • a pump 11 is used to pump the reagent to the injector at a predetermined pressure.
  • Reagent 7 is circulated back to the reservoir via return line 12 , the circulation of the reagent being shown by the arrows 7 a.
  • signals 13 representing engine operational parameters such as exhaust gas temperature, engine speed and fuel flow rate are monitored by central processing unit 8 .
  • central processing unit 8 sends control signals 14 and 15 to injector 10 and pump 11 respectively, the control signals commanding pump 11 to circulate reagent and injector 10 to inject or cease injecting reagent into exhaust gases 16 within the exhaust conduit 4 .
  • the reagent is atomized upon injection into the conduit and forms a mixture with the exhaust gases.
  • This mixture enters the catalytic reactor 5 which contains a catalyst, such as activated carbon, or metals, such as platinum, tungsten or vanadium, which reduces NO x in the exhaust gases in the presence of the reagent.
  • the exhaust exits the conduit 4 and passes to the atmosphere.
  • reagent 7 is circulated continuously between the reservoir 6 and the injector 10 to cool the injector and minimize the dwell time of the reagent in the injector so that the reagent remains cool.
  • Continuous reagent circulation is necessary for temperature-sensitive reagents, such as aqueous urea, which tend to solidify upon exposure to elevated temperatures of 300° C. to 650° C. as would be experienced in an engine exhaust system. It has been found to be important to keep the urea mixture below 140° C. and preferably in a lower operating range between 5° C. and 95° C. to provide a margin of safety ensuring that solidification of the urea is prevented.
  • FIG. 2 shows a cross-sectional view of the preferred embodiment of the injector 10 according to the invention.
  • the injector is shown mounted on an exhaust gas conduit 4 , only partially depicted, in cross-section.
  • Injector 10 comprises a valve body 18 having an elongated cylindrical chamber 20 disposed therein. Chamber 20 is in fluid communication with an orifice 22 which opens onto the exhaust gases within conduit 4 .
  • a valve seat 24 Surrounding orifice 22 is a valve seat 24 which can have any practical shape but is preferably conical.
  • a valve member in the form of an elongated valve plunger 26 is slidably mounted within chamber 20 .
  • Valve plunger 26 has an end 28 formed to sealingly interengage valve seat 24 , as seen in FIG. 2, thereby closing orifice 22 from fluid communication with chamber 20 .
  • Valve plunger 26 is movable within the chamber between the closed position shown in FIG. 2 and an open position wherein end 28 is removed from sealing interengagement with valve seat 24 . In the open position, orifice 22 is opened to fluid communication with chamber 20 .
  • the chamber 20 and the valve plunger 26 provide a means for circulating fluid, such as the reagent, through the valve for cooling the valve and for minimizing the dwell time of the reagent within the valve.
  • the circulating means comprises an annular fluid passageway 30 formed between the relatively larger inner diameter of chamber 20 and the relatively smaller outer diameter of a section 32 of the valve plunger 26 .
  • plunger section 32 is arranged adjacent to plunger end 28 and close to valve seat 24 and orifice 22 . Positioning fluid passageway 30 close to the orifice allows the circulating fluid to directly cool an otherwise hot part of the valve body most sensitive to the adverse effects of heat.
  • aqueous urea when used with this cooled valve, will not solidify anywhere within chamber 20 . If allowed to solidify, the urea could prevent plunger 26 from seating properly or could cause the plunger to seize in either the open or closed position and/or the orifice 22 could become clogged. By directly cooling this region of the valve, however, the detrimental effects of elevated temperature on the reagent, the moving parts, and the openings of the valve are avoided.
  • plunger 26 further comprises a guide section 33 disposed adjacent to section 32 of the valve plunger.
  • Guide section 33 preferably has a polygonal cross-section formed by a plurality of flats 33 a intersecting at a plurality of corners 33 b .
  • Flats 33 a provide fluid circulation spaces adjacent to the chamber 20 and augment the cooling function of the fluid passageway 30 .
  • the flats also provide space for any debris formed within or brought into chamber 20 to wash out of the chamber with the circulating fluid.
  • the corners 33 b of the guide section 33 provide a stabilizing and a guiding function for plunger 26 .
  • the corners are toleranced to ride close to or in light contact with the wall of chamber 20 to provide support points which guide the plunger within the chamber to ensure proper seating of plunger end 28 .
  • a reduced circular cross-section 35 of plunger 26 Immediately above guide section 33 is a reduced circular cross-section 35 of plunger 26 . Reduced section 35 provides an annular space for fluid to flow into the chamber through an inlet, described in detail below. Above the reduced section is a circular guide section 37 . Circular guide section 37 provides the main guiding function for sliding motion of the plunger 26 within the chamber 20 . The tolerance between the circular guide section and the chamber is sufficient to allow relative motion and lubrication of the plunger while still guiding the plunger's motion and forming a partial hydraulic seal between the plunger and the chamber.
  • valve plunger and the chamber will vary according to the operating temperature, operating pressure, the desired flow rate and circulation rate of the reagent, the tribological properties of the reagent and the materials chosen for the valve plunger and valve body.
  • the tolerances for optimum injector performance are best obtained experimentally by a few field trials.
  • the cooling fluid is delivered to the annular fluid passageway 30 through fluid inlet 34 .
  • Fluid inlet 34 is arranged within valve body 18 in fluid communication with chamber 20 and is externally connected to supply line 9 (FIG. 1). It is preferred that the fluid inlet be positioned to deliver fluid to chamber 20 in a region removed from the valve seat 24 adjacent to reduced section 25 and guide section 33 , as shown in FIG. 2. Positioning the fluid inlet upstream from the seat, as shown, allows the fluid to contact valve plunger 26 over a substantial length before it encounters the valve seat, thereby enhancing the cooling function of the fluid. Fluid, such as reagent 7 , is pumped via pump 11 at a predetermined pressure into the fluid inlet 34 from which it flows along valve plunger 26 into annular fluid passageway 30 .
  • a fluid outlet 36 is provided to remove the fluid from the annular fluid passageway.
  • Fluid outlet 36 is arranged within valve body 18 in fluid communication with chamber 20 .
  • fluid outlet 36 is positioned as shown in FIG. 2 for removing fluid from chamber 20 in the region of the valve seat 24 .
  • Fluid outlet 36 is externally connected to return line 12 (FIG. 1), thus permitting the fluid (such as reagent 7 ) to circulate from reservoir 6 , through supply line 9 , through fluid inlet 34 , into annular fluid passageway 30 , through fluid outlet 36 , through return line 12 and back into reservoir 6 .
  • This circulation keeps critical regions of the valve body 18 cool and minimizes the dwell time of the fluid in the injector.
  • valve plunger 26 When the valve plunger 26 is moved from the closed position, shown in FIG. 2, to an open position, plunger end 28 is removed from sealing interengagement with seat 24 . This action opens orifice 22 and allows at least a portion of the circulating fluid to be expelled through the orifice and into exhaust conduit 4 .
  • actuating means are provided, preferably in the form of solenoid 38 mounted atop valve body 18 . Solenoid 38 has an armature 40 connected to valve plunger 26 . When the solenoid is energized, the armature 40 is drawn upward, thereby sliding valve plunger 26 within chamber 20 from the closed position to the open position.
  • the solenoid would be energized, for example, in response to a signal 14 (see FIG. 1) from central processing unit 8 , which decides, based upon sensor input signals 13 and its preprogrammed algorithms, when reagent is needed for effective selective catalytic reduction of NO x emissions in the exhaust stream.
  • valve plunger 26 is biased in the closed position by a biasing member, preferably in the form of a coil spring 42 coaxially disposed about valve plunger 26 .
  • the valve plunger has a shoulder 44 which serves as a lower spring seat against which the spring can push to bias the valve plunger.
  • An upper plate 46 is fixed to the valve body 18 and serves as the upper spring seat, as well as a stop to limit the upward travel of the valve plunger.
  • Spring 42 is located within a spring chamber 48 which is isolated from chamber 20 by seal 50 .
  • Seal 50 is preferably made of carbon reinforced Teflon® or glass reinforced Teflon® and prevents any corrosive reagent from entering the spring chamber and possibly attacking or fouling the spring and the solenoid.
  • Injector 10 is shown mounted on exhaust conduit 4 by means of sleeve 52 which is welded to an opening in the conduit by weldment 54 .
  • valve body 18 has external threads 19 which engage matching internal threads 53 in sleeve 52 to attach the injector to the sleeve.
  • the external threads 19 are not continuous around the circumference of valve body 18 but interrupted or discontinuous, as seen in FIG. 3.
  • the thread contact area is minimized by using intermittent arcs of threads subtending angles on the order of 20° arranged circumferentially around valve body 18 , with flat regions 21 arranged between each thread arc.
  • the flats have an across-the-flat dimension which is less than the root diameter of the thread on valve body 18 and, therefore, make no contact with sleeve 52 .
  • Heat shield 56 includes an outer metal plate 58 and a layer of insulating material in the form of a thermal gasket 60 interposed between outer plate 58 and valve body 18 .
  • outer plate 58 is made of stainless steel to resist the corrosive environment within the exhaust conduit.
  • Gasket 60 is preferably made of a flexible graphite foil material whose low thermal conductivity serves to isolate valve body 18 from outer plate 58 , reducing conductive heat transfer to the injector and thereby helping to keep the fluid circulating within the valve cool.
  • Heat shield 56 surrounds the orifice 22 and has an aperture 62 which passes through both the outer plate and the insulating thermal gasket and permits fluid expelled from the injector to pass through the heat shield and into the conduit.
  • the heat shield has a substantially planar surface which is preferably oriented perpendicular to the jet of fluid expelled from the injector.
  • a radiant heat reflector 70 seen edge on in FIG. 2.
  • Reflector 70 is preferably a round disc of polished aluminum having an outer diameter of sufficient extent such that the surface 70 a of the disc blocks radiant heat transfer from exhaust conduit 4 to parts of the injector which have a direct line of sight to the conduit.
  • the reflector has a centrally positioned aperture 72 which fits around valve body 18 and sits atop sleeve 52 to mount the reflector between the exposed parts of the injector and the conduit 4 .
  • Reflector 70 is retained in position by a nut 74 which threads onto valve body 18 .
  • injection pressure relatively low to prevent the fluid jet or plume from the injector from over-penetrating into the exhaust gas stream and impinging on the sidewall of the conduit. Injection pressures within a range of 30 to 100 psi have been found to prevent over-penetration. An injection pressure of 67 psi is preferred for the injector according to the invention.
  • an atomization hook 64 is provided. It is an advantage of the invention that no secondary atomization fluid is required.
  • Hook 64 is mounted on the valve, preferably on the metal plate 58 of heat shield 56 as seen in FIG. 2.
  • the hook is made of stainless steel to withstand the corrosive environment within the exhaust conduit. Mounting the hook on the heat shield serves to thermally isolate the hook from the valve body 18 . Because the hook extends into the exhaust stream, it will be hot, and being metal, it will tend to conduct heat readily. However, by mounting the hook on the heat shield heat conducted by the hook will be blocked by the thermal gasket 60 , and heat transfer from the hook to the valve body will be minimized by this preferred mounting of the hook 64 .
  • Hook 64 has an end surface 66 which is positioned in a spaced-apart relation facing orifice 22 .
  • the valve plunger 26 When the valve plunger 26 is actuated into its open position by solenoid 38 , expelling fluid at a predetermined pressure from orifice 22 , the fluid jet will impinge on end surface 66 . This impingement will cause further atomization of the fluid.
  • the dispersion characteristics of the fluid are a function of the shape of the end surface, which is tuned to a particular size and shape of the exhaust stream to ensure maximum dispersion and penetration of the fluid without over-penetration.
  • An injector wherein critical valve components are directly cooled by circulating fluid provides a component for a pollution control system which allows a corrosive and heat-sensitive reagent, such as aqueous urea, to be effectively employed to reduce NO x emissions and thereby ultimately attain greater fuel efficiency without the adverse effects of increased undesired emissions.
  • a corrosive and heat-sensitive reagent such as aqueous urea

Abstract

A method for reducing emissions of oxides of nitrogen from a combustion process using a temperature sensitive liquid reagent injected into a stream of exhaust gases from the combustion process and passing the exhaust gases and the reagent through a catalytic reactor which reduces the oxides of nitrogen in the presence of the reagent is disclosed. The steps of the method include providing an injector having an orifice for atomizing the liquid reagent; positioning a portion of the injector having the orifice within the stream of exhaust gases; cooling the injector by continuously circulating the reagent therethrough, thereby keeping both the injector and the reagent within the injector below a critical temperature at which the reagent will solidify; and injecting a portion of the reagent into the exhaust stream upstream of the reactor.

Description

    RELATED APPLICATION
  • This is a divisional application based on U.S. application Ser. No. 09/164,304, filed Oct. 1, 1998.[0001]
  • FIELD OF INVENTION
  • This invention relates to methods for reducing NO[0002] x emissions from internal combustion engines and especially to methods using fluid-cooled injectors wherein the fluid is a liquid reagent and a portion of the reagent is injected as an atomized liquid reagent into the exhaust gas stream of an internal combustion engine.
  • BACKGROUND OF INVENTION
  • Improved fuel efficiency for vehicles having internal combustion engines can be achieved by using diesel engines or gasoline engines operated with an excess of oxygen over 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 economy, however, is offset by undesired pollution emissions, specifically in the form of oxides of nitrogen (NO[0003] x).
  • One method used to reduce NO[0004] x emissions from internal combustion engines is known as selective catalytic reduction (SCR). SCR, when used, for example, to reduce NOx emissions from a diesel engine, involves injecting an atomized reagent into the exhaust stream of the engine in relation to one or more selected engine operational parameters, such as exhaust gas temperature, engine rpm or engine load as measured by engine fuel flow, turbo boost pressure or exhaust NOx mass flow. The reagent/exhaust gas mixture is passed through a reactor containing a catalyst, such as, for example, activated carbon or metals, such as platinum, vanadium or tungsten, which are capable of reducing the NOx concentration in the presence of the reagent. An SCR system of this type is disclosed in U.S. patent application Ser. No. 08/831,209, hereby incorporated by reference.
  • An aqueous solution of urea is known to be an effective reagent in SCR systems for diesel engines but suffers several disadvantages. Urea is highly corrosive and tends to attack mechanical components of the SCR system, such as the injectors used to inject the urea mixture into the exhaust gas stream. Urea also tends to solidify upon prolonged exposure to elevated temperatures, such as encountered in diesel exhaust systems. Solidified urea tends to accumulate in the narrow passageways and orifice openings typically found in injectors. The solidified urea fouls moving parts of the injector and clogs any openings, thus, rendering the injector unusable. [0005]
  • Furthermore, if the urea mixture is not finely atomized, urea deposits will form in the catalytic reactor, inhibiting the action of the catalyst and thereby reducing the SCR system effectiveness. High injection pressures are one way of dealing with the problem of insufficient atomization of the urea mixture, but high injection pressures often result in over-penetration of the injector spray plume into the exhaust stream, causing the plume to impinge on the inner surface of the exhaust pipe opposite the injector. Over-penetration leads to inefficient use of the urea mixture and reduces the range over which the vehicle can operate with reduced NO[0006] x emissions. Like fuel for the vehicle, only a finite amount of aqueous urea can be carried and what is carried should be used efficiently to maximize vehicle range and reduce the need for frequent fill ups of the reagent.
  • Additionally, aqueous urea is a poor lubricant. This characteristic adversely affects moving parts within the injector and requires that special fits, clearances and tolerances be employed between relatively moving parts within an injector. [0007]
  • SUMMARY AND OBJECTS OF INVENTION
  • The method according to the invention concerns reducing emissions of oxides of nitrogen from a combustion process using a temperature sensitive liquid reagent injected into a stream of exhaust gases from the combustion process and passing the exhaust gases and the reagent through a catalytic reactor which reduces the oxides of nitrogen in the presence of the reagent. The steps of the method include providing an injector having an orifice for atomizing the liquid reagent; positioning a portion of the injector having the orifice within the stream of exhaust gases; cooling the injector by continuously circulating the reagent therethrough, thereby keeping both the injector and the reagent within the injector below a critical temperature at which the reagent will solidify; and injecting a portion of the reagent into the exhaust stream upstream of the reactor. [0008]
  • The reagent is preferably an aqueous urea solution which is injected into the stream of exhaust gases in proportion to selected engine operating parameters. Preferably the urea has a concentration between about 25% and about 35%. The reagent is circulated continuously at a rate which will keep its temperature below about 140° C. and preferably below about 95° C. [0009]
  • The invention also provides an injector for delivery of a fluid into a stream of hot gas, the injector being designed to operate effectively with a corrosive, temperature-sensitive reagent, such as aqueous urea. When used in the method according to the invention for reducing NO[0010] x emissions, the injector is mounted on an exhaust conduit of an internal combustion engine where it injects the reagent into the exhaust gas stream.
  • The injector comprises a valve and a means for actuating the valve between a closed position and an open position. Acceptable actuating means include, for example, a solenoid-type actuator. Preferably, the components of the valve exposed to extreme heat or corrosive reagents like urea are made of a corrosion resistant material such as stainless steel. [0011]
  • The valve includes an orifice through which the reagent is expelled when the valve is in the open position. Regardless of the state of the valve (i.e., open or closed), the reagent is continuously circulated through it when the system is in operation, at least a portion of the circulating reagent being expelled when the valve is opened. The circulation of the reagent cools the valve and minimizes the dwell time of the reagent within the valve, thereby minimizing exposure of the reagent to heat and the creation of urea deposits. Thus, aqueous urea, for example, can be effectively used with such an injector without the characteristic fouling and clogging of the injector. Means independent of the valve actuating means are provided for continuously circulating the reagent through the valve, as described in detail below. [0012]
  • Preferably, the valve comprises a valve body which has an elongated cylindrical chamber therein in fluid communication with the orifice. A valve seat is positioned within the chamber surrounding the orifice. An elongated valve plunger is slidably mounted within the chamber. One end of the plunger is sealingly interengagable with the valve seat to close the orifice. The plunger is connected with the actuating means and is movable from the closed position where the plunger end sealingly engages the valve seat and the open position where the plunger end is removed from sealing interengagement with the valve seat to open the orifice. [0013]
  • The means for independently circulating fluid through the valve comprises a portion of the plunger which is arranged adjacent to the plunger end. This portion of the plunger has a diameter less than the chamber diameter and forms an annular fluid space or passageway within the valve adjacent to the valve seat and the orifice. The annular passageway, thus, allows for both the continuous circulation of fluid through the valve and the expelling of a portion of the fluid through the orifice when the valve is in the open position. [0014]
  • Preferably, the independent fluid circulating means further comprises a fluid inlet and a fluid outlet arranged within the valve body in fluid communication with the annular passageway. Fluid, such as the aqueous urea reagent, is supplied from a reservoir and flows into the valve through the inlet, continues through the annular passageway and exits the valve via the outlet, thereby cooling the injector. When the valve is opened by the actuator, the valve plunger is moved to the open position, and a portion of the fluid is expelled from the chamber through the orifice. [0015]
  • In order to provide additional heat protection for the injector, a heat shield is preferably interposed between the valve and the stream of hot gas. The heat shield has an aperture which is aligned with the orifice. The heat shield aperture allows fluid expelled from the valve to pass through the heat shield and into the hot gas stream. The heat shield preferably comprises a metal plate and a layer of insulating material interposed between the plate and the valve. The heat shield aperture passes through both the layer of insulating material, as well as the metal plate. [0016]
  • To improve atomization of liquid reagents, especially at relatively low injection pressures, an atomizing hook is preferably mounted on the valve. The atomizing hook has an end surface which is positioned in a spaced apart relation with the orifice. Liquid reagent expelled through the orifice impinges on the hook end surface where further atomization of the reagent occurs. The shape and position of the hook end surface directly affect the dispersion characteristics of the injected reagent. [0017]
  • It is an object of the invention to provide a method for reducing NO[0018] x emissions from a combustion process by injecting a temperature sensitive liquid reagent into a stream of exhaust gases from the combustion process.
  • It is another object of the invention to provide a method which uses urea as the liquid reagent. [0019]
  • It is still another object of the invention to provide a method which uses aqueous urea at relatively high concentrations. [0020]
  • It is yet another object of the invention to provide a method which uses an injector to inject the reagent into the exhaust stream. [0021]
  • It is again another object of the invention to provide a method wherein the reagent is continuously circulated through the injector to keep both the reagent and the injector below a temperature at which the urea will solidify. [0022]
  • It is an object of the invention to provide an injector for injecting a fluid into a stream of hot gas. [0023]
  • It is another object of the invention to provide an injector useable with corrosive liquids such as aqueous urea. [0024]
  • It is yet another object of the invention to provide an injector in which aqueous urea will not solidify when the injector is exposed to heat. [0025]
  • It is still another object of the invention to provide an injector which achieves fine atomization of liquid reagents at relatively low injection pressures. [0026]
  • It is a further object of the invention to provide an injector wherein a portion of the fluid being injected is also continuously circulated through the injector to cool the injector. [0027]
  • It is yet a further object of the invention to provide an injector wherein the dwell time of the fluid within the injector is minimized. [0028]
  • It is still a further object of the invention to provide an injector useable in a pollution control system for reducing NO[0029] x emissions of internal combustion engines.
  • These and other objects will become apparent from a consideration of the following drawings and detailed description of the invention.[0030]
  • BRIEF DESCRIPTION OF THE DRAWINGS
  • FIG. 1 shows a schematic diagram of a pollution emission control system using an injector according to the invention; [0031]
  • FIG. 2 shows a longitudinal cross-sectional view of an injector according to the invention; and [0032]
  • FIG. 3 shows a side view of the valve body of the injector according to the invention.[0033]
  • DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENT
  • FIG. 1 illustrates a pollution control system as might be used to reduce NO[0034] x emissions from the exhaust of a diesel engine 3. The system includes an engine exhaust conduit 4 in fluid communication with a catalytic reactor 5, a reagent reservoir 6 holding reagent 7, a central processing unit 8 and an injector 10. Injector 10 is mounted on exhaust conduit 4 and fed reagent, for example, a solution of aqueous urea via supply line 9 extending from reservoir 7 to the injector. A pump 11 is used to pump the reagent to the injector at a predetermined pressure. Reagent 7 is circulated back to the reservoir via return line 12, the circulation of the reagent being shown by the arrows 7 a.
  • In operation, signals [0035] 13, representing engine operational parameters such as exhaust gas temperature, engine speed and fuel flow rate are monitored by central processing unit 8. In response to these signals and preprogrammed algorithms, central processing unit 8 sends control signals 14 and 15 to injector 10 and pump 11 respectively, the control signals commanding pump 11 to circulate reagent and injector 10 to inject or cease injecting reagent into exhaust gases 16 within the exhaust conduit 4. The reagent is atomized upon injection into the conduit and forms a mixture with the exhaust gases. This mixture enters the catalytic reactor 5 which contains a catalyst, such as activated carbon, or metals, such as platinum, tungsten or vanadium, which reduces NOx in the exhaust gases in the presence of the reagent. The exhaust exits the conduit 4 and passes to the atmosphere.
  • During system operation, regardless of whether or not the injector is releasing reagent into the [0036] exhaust gases 16, reagent 7 is circulated continuously between the reservoir 6 and the injector 10 to cool the injector and minimize the dwell time of the reagent in the injector so that the reagent remains cool. Continuous reagent circulation is necessary for temperature-sensitive reagents, such as aqueous urea, which tend to solidify upon exposure to elevated temperatures of 300° C. to 650° C. as would be experienced in an engine exhaust system. It has been found to be important to keep the urea mixture below 140° C. and preferably in a lower operating range between 5° C. and 95° C. to provide a margin of safety ensuring that solidification of the urea is prevented. Solidified urea, if allowed to form, would foul the moving parts and openings of the injector, eventually rendering the injector useless. In the case of a 310-horsepower diesel engine with a baseline NOx emissions level of 8 grams/bHp-hr at full load, circulation rates of aqueous urea between 0.5 gallons per minute and 0.75 gallons per minute through an injector according to the invention have been found to effectively cool the aqueous urea and prevent solidification. It will be recognized that flow rates will depend on engine size and NOx levels. It is an advantage of the invention that more concentrated solutions can be utilized, i.e., 25-35%, because throughout the system, the solution is not subject to conditions which would cause significant hydrolysis or solubility problems.
  • FIG. 2 shows a cross-sectional view of the preferred embodiment of the [0037] injector 10 according to the invention. The injector is shown mounted on an exhaust gas conduit 4, only partially depicted, in cross-section. Injector 10 comprises a valve body 18 having an elongated cylindrical chamber 20 disposed therein. Chamber 20 is in fluid communication with an orifice 22 which opens onto the exhaust gases within conduit 4. Surrounding orifice 22 is a valve seat 24 which can have any practical shape but is preferably conical. A valve member in the form of an elongated valve plunger 26 is slidably mounted within chamber 20. Valve plunger 26 has an end 28 formed to sealingly interengage valve seat 24, as seen in FIG. 2, thereby closing orifice 22 from fluid communication with chamber 20.
  • [0038] Valve plunger 26 is movable within the chamber between the closed position shown in FIG. 2 and an open position wherein end 28 is removed from sealing interengagement with valve seat 24. In the open position, orifice 22 is opened to fluid communication with chamber 20.
  • Together, the [0039] chamber 20 and the valve plunger 26 provide a means for circulating fluid, such as the reagent, through the valve for cooling the valve and for minimizing the dwell time of the reagent within the valve. The circulating means comprises an annular fluid passageway 30 formed between the relatively larger inner diameter of chamber 20 and the relatively smaller outer diameter of a section 32 of the valve plunger 26. Preferably, plunger section 32 is arranged adjacent to plunger end 28 and close to valve seat 24 and orifice 22. Positioning fluid passageway 30 close to the orifice allows the circulating fluid to directly cool an otherwise hot part of the valve body most sensitive to the adverse effects of heat. Thus, for example, aqueous urea, when used with this cooled valve, will not solidify anywhere within chamber 20. If allowed to solidify, the urea could prevent plunger 26 from seating properly or could cause the plunger to seize in either the open or closed position and/or the orifice 22 could become clogged. By directly cooling this region of the valve, however, the detrimental effects of elevated temperature on the reagent, the moving parts, and the openings of the valve are avoided.
  • As seen in FIG. 2, [0040] plunger 26 further comprises a guide section 33 disposed adjacent to section 32 of the valve plunger. Guide section 33 preferably has a polygonal cross-section formed by a plurality of flats 33 a intersecting at a plurality of corners 33 b. Flats 33 a provide fluid circulation spaces adjacent to the chamber 20 and augment the cooling function of the fluid passageway 30. The flats also provide space for any debris formed within or brought into chamber 20 to wash out of the chamber with the circulating fluid.
  • The corners [0041] 33 b of the guide section 33 provide a stabilizing and a guiding function for plunger 26. The corners are toleranced to ride close to or in light contact with the wall of chamber 20 to provide support points which guide the plunger within the chamber to ensure proper seating of plunger end 28.
  • Immediately above [0042] guide section 33 is a reduced circular cross-section 35 of plunger 26. Reduced section 35 provides an annular space for fluid to flow into the chamber through an inlet, described in detail below. Above the reduced section is a circular guide section 37. Circular guide section 37 provides the main guiding function for sliding motion of the plunger 26 within the chamber 20. The tolerance between the circular guide section and the chamber is sufficient to allow relative motion and lubrication of the plunger while still guiding the plunger's motion and forming a partial hydraulic seal between the plunger and the chamber.
  • Generally, the specific tolerances required at the various sections between the valve plunger and the chamber will vary according to the operating temperature, operating pressure, the desired flow rate and circulation rate of the reagent, the tribological properties of the reagent and the materials chosen for the valve plunger and valve body. The tolerances for optimum injector performance are best obtained experimentally by a few field trials. [0043]
  • The cooling fluid is delivered to the [0044] annular fluid passageway 30 through fluid inlet 34. Fluid inlet 34 is arranged within valve body 18 in fluid communication with chamber 20 and is externally connected to supply line 9 (FIG. 1). It is preferred that the fluid inlet be positioned to deliver fluid to chamber 20 in a region removed from the valve seat 24 adjacent to reduced section 25 and guide section 33, as shown in FIG. 2. Positioning the fluid inlet upstream from the seat, as shown, allows the fluid to contact valve plunger 26 over a substantial length before it encounters the valve seat, thereby enhancing the cooling function of the fluid. Fluid, such as reagent 7, is pumped via pump 11 at a predetermined pressure into the fluid inlet 34 from which it flows along valve plunger 26 into annular fluid passageway 30.
  • A fluid outlet [0045] 36 is provided to remove the fluid from the annular fluid passageway. Fluid outlet 36 is arranged within valve body 18 in fluid communication with chamber 20. Preferably, fluid outlet 36 is positioned as shown in FIG. 2 for removing fluid from chamber 20 in the region of the valve seat 24. Fluid outlet 36 is externally connected to return line 12 (FIG. 1), thus permitting the fluid (such as reagent 7) to circulate from reservoir 6, through supply line 9, through fluid inlet 34, into annular fluid passageway 30, through fluid outlet 36, through return line 12 and back into reservoir 6. This circulation keeps critical regions of the valve body 18 cool and minimizes the dwell time of the fluid in the injector.
  • When the [0046] valve plunger 26 is moved from the closed position, shown in FIG. 2, to an open position, plunger end 28 is removed from sealing interengagement with seat 24. This action opens orifice 22 and allows at least a portion of the circulating fluid to be expelled through the orifice and into exhaust conduit 4. To effect the opening and closing of the orifice, actuating means are provided, preferably in the form of solenoid 38 mounted atop valve body 18. Solenoid 38 has an armature 40 connected to valve plunger 26. When the solenoid is energized, the armature 40 is drawn upward, thereby sliding valve plunger 26 within chamber 20 from the closed position to the open position. The solenoid would be energized, for example, in response to a signal 14 (see FIG. 1) from central processing unit 8, which decides, based upon sensor input signals 13 and its preprogrammed algorithms, when reagent is needed for effective selective catalytic reduction of NOx emissions in the exhaust stream.
  • As seen in FIG. 2, [0047] valve plunger 26 is biased in the closed position by a biasing member, preferably in the form of a coil spring 42 coaxially disposed about valve plunger 26. The valve plunger has a shoulder 44 which serves as a lower spring seat against which the spring can push to bias the valve plunger. An upper plate 46 is fixed to the valve body 18 and serves as the upper spring seat, as well as a stop to limit the upward travel of the valve plunger.
  • [0048] Spring 42 is located within a spring chamber 48 which is isolated from chamber 20 by seal 50. Seal 50 is preferably made of carbon reinforced Teflon® or glass reinforced Teflon® and prevents any corrosive reagent from entering the spring chamber and possibly attacking or fouling the spring and the solenoid.
  • [0049] Injector 10 is shown mounted on exhaust conduit 4 by means of sleeve 52 which is welded to an opening in the conduit by weldment 54. Preferably, valve body 18 has external threads 19 which engage matching internal threads 53 in sleeve 52 to attach the injector to the sleeve. In order to minimize conductive heat transfer between the sleeve and the valve body, the external threads 19 are not continuous around the circumference of valve body 18 but interrupted or discontinuous, as seen in FIG. 3. Preferably, the thread contact area is minimized by using intermittent arcs of threads subtending angles on the order of 20° arranged circumferentially around valve body 18, with flat regions 21 arranged between each thread arc. The flats have an across-the-flat dimension which is less than the root diameter of the thread on valve body 18 and, therefore, make no contact with sleeve 52.
  • In the configuration shown, hot exhaust gases within the conduit are prevented from impinging directly upon the [0050] valve body 18 by the interposition of a heat shield 56 between the valve body and the exhaust gases. Heat shield 56 includes an outer metal plate 58 and a layer of insulating material in the form of a thermal gasket 60 interposed between outer plate 58 and valve body 18. Preferably, outer plate 58 is made of stainless steel to resist the corrosive environment within the exhaust conduit. Gasket 60 is preferably made of a flexible graphite foil material whose low thermal conductivity serves to isolate valve body 18 from outer plate 58, reducing conductive heat transfer to the injector and thereby helping to keep the fluid circulating within the valve cool.
  • [0051] Heat shield 56 surrounds the orifice 22 and has an aperture 62 which passes through both the outer plate and the insulating thermal gasket and permits fluid expelled from the injector to pass through the heat shield and into the conduit. The heat shield has a substantially planar surface which is preferably oriented perpendicular to the jet of fluid expelled from the injector.
  • Further thermal protection for the injector is provided by a [0052] radiant heat reflector 70 seen edge on in FIG. 2. Reflector 70 is preferably a round disc of polished aluminum having an outer diameter of sufficient extent such that the surface 70 a of the disc blocks radiant heat transfer from exhaust conduit 4 to parts of the injector which have a direct line of sight to the conduit. The reflector has a centrally positioned aperture 72 which fits around valve body 18 and sits atop sleeve 52 to mount the reflector between the exposed parts of the injector and the conduit 4. Reflector 70 is retained in position by a nut 74 which threads onto valve body 18.
  • It is desired to keep the injection pressure relatively low to prevent the fluid jet or plume from the injector from over-penetrating into the exhaust gas stream and impinging on the sidewall of the conduit. Injection pressures within a range of 30 to 100 psi have been found to prevent over-penetration. An injection pressure of 67 psi is preferred for the injector according to the invention. [0053]
  • However, lower injection pressures might not atomize the injected fluid to a sufficiently fine size for effective catalytic reduction of the NO[0054] x. To assist dispersion and atomization of the fluid within the conduit and yet maintain reasonably low injection pressures, an atomization hook 64 is provided. It is an advantage of the invention that no secondary atomization fluid is required.
  • [0055] Hook 64 is mounted on the valve, preferably on the metal plate 58 of heat shield 56 as seen in FIG. 2. Preferably, the hook is made of stainless steel to withstand the corrosive environment within the exhaust conduit. Mounting the hook on the heat shield serves to thermally isolate the hook from the valve body 18. Because the hook extends into the exhaust stream, it will be hot, and being metal, it will tend to conduct heat readily. However, by mounting the hook on the heat shield heat conducted by the hook will be blocked by the thermal gasket 60, and heat transfer from the hook to the valve body will be minimized by this preferred mounting of the hook 64.
  • [0056] Hook 64 has an end surface 66 which is positioned in a spaced-apart relation facing orifice 22. When the valve plunger 26 is actuated into its open position by solenoid 38, expelling fluid at a predetermined pressure from orifice 22, the fluid jet will impinge on end surface 66. This impingement will cause further atomization of the fluid. The dispersion characteristics of the fluid are a function of the shape of the end surface, which is tuned to a particular size and shape of the exhaust stream to ensure maximum dispersion and penetration of the fluid without over-penetration.
  • An injector wherein critical valve components are directly cooled by circulating fluid according to the invention provides a component for a pollution control system which allows a corrosive and heat-sensitive reagent, such as aqueous urea, to be effectively employed to reduce NO[0057] x emissions and thereby ultimately attain greater fuel efficiency without the adverse effects of increased undesired emissions.

Claims (15)

What is claimed is:
1. A method of reducing emissions of oxides of nitrogen from a combustion process using a temperature sensitive liquid reagent injected into a stream of exhaust gases from said combustion process and passing said exhaust gases and said reagent through a catalytic reactor which reduces the oxides of nitrogen in the presence of the reagent, said method comprising the steps of:
providing an injector having an orifice for atomizing said liquid reagent;
positioning a portion of said injector having said orifice within said stream of exhaust gases;
cooling said injector by continuously circulating said reagent therethrough, thereby keeping both said injector and said reagent within said injector below a critical temperature at which said reagent will solidify; and
injecting a portion of said reagent into said exhaust stream upstream of said reactor.
2. A method according to claim 1, wherein said reagent is an aqueous urea solution.
3. A method according to claim 2, wherein said urea has a concentration between about 25% and about 35%.
4. A method according to claim 1, further comprising the steps of providing a surface facing said orifice within said exhaust gas stream, and further atomizing said reagent injected into said exhaust gas stream by impinging said reagent onto said surface.
5. A method according to claim 1, wherein said combustion process occurs within an internal combustion engine.
6. A method according to claim 5, wherein said engine is a diesel engine.
7. A method according to claim 6, wherein said reagent is injected into said stream of exhaust gases in proportion to selected engine operating parameters.
8. A method of reducing emissions of oxides of nitrogen from a combustion process using a liquid reagent injected through an injector into a stream of exhaust gases from said combustion process, wherein at least a portion of said injector being positioned within said stream of exhaust gases, said method comprising the steps of:
(1) continuously circulating said reagent through said injector to keep both said injector and said reagent within said injector below a critical temperature;
(2) injecting at least a portion of said reagent through said injector into said exhaust stream; and
(3) passing said exhaust gases and said reagent injected therein through a catalytic reactor to reduce the oxides of nitrogen.
9. A method according to claim 8, wherein said reagent is an aqueous urea solution.
10. A method according to claim 8, wherein said urea has a concentration between about 25% and about 35%.
11. A method according to claim 8, wherein said injector has an orifice for atomizing said liquid reagent, and further comprising the steps of providing a surface facing said orifice within said exhaust gas stream, and further atomizing said reagent injected into said exhaust gas stream by impinging said reagent onto said surface.
12. A method according to claim 8, wherein said combustion process occurs within an internal combustion engine.
13. A method according to claim 8, wherein said engine is a diesel engine.
14. A method according to claim 8, wherein said reagent is injected into said stream of exhaust gases in proportion to selected engine operating parameters.
15. A method according to claim 9, wherein said critical temperature is between about 95° C. and about 140° C.
US09/901,180 1998-10-01 2001-07-09 Method of reducing NOx emissions using a fluid-cooled injector Abandoned US20020001554A1 (en)

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Cited By (36)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2005005799A1 (en) * 2003-07-09 2005-01-20 Robert Bosch Gmbh Cooled device for metering reducing agent to the exhaust gas of a combustion engine
EP1751407A2 (en) * 2004-04-26 2007-02-14 Combustion Components Associates, Inc. Methods and apparatus for injecting atomized fluid
WO2007124779A1 (en) * 2006-05-03 2007-11-08 Purem Abgassysteme Gmbh & Co. Kg Process and device for dosing a reducing agent in an exhaust system of an internal combustion engine
US20090179087A1 (en) * 2004-04-26 2009-07-16 Martin Scott M Method and apparatus for injecting atomized fluids
US20090229258A1 (en) * 2008-03-05 2009-09-17 Hydraulik-Ring Gmbh Exhaust-Gas Aftertreatment Device
US20110023466A1 (en) * 2009-08-03 2011-02-03 Hydraulik-Ring Gmbh SCR exhaust gas aftertreatment device
US20110192140A1 (en) * 2010-02-10 2011-08-11 Keith Olivier Pressure swirl flow injector with reduced flow variability and return flow
US8074673B2 (en) 2004-05-18 2011-12-13 Hydraulik-Ring Gmbh Freeze-resistant metering valve
US20120110990A1 (en) * 2009-07-27 2012-05-10 Robert Bosch Gmbh Mounting unit for fastening an injection member to an exhaust gas tract
US8266892B2 (en) 2007-01-25 2012-09-18 Friedrich Zapf Calibrated dosing unit, especially of an exhaust gas treatment unit
US8438839B2 (en) 2010-10-19 2013-05-14 Tenneco Automotive Operating Company Inc. Exhaust gas stream vortex breaker
US8677738B2 (en) 2011-09-08 2014-03-25 Tenneco Automotive Operating Company Inc. Pre-injection exhaust flow modifier
US8740113B2 (en) 2010-02-10 2014-06-03 Tenneco Automotive Operating Company, Inc. Pressure swirl flow injector with reduced flow variability and return flow
US8875502B2 (en) 2010-12-14 2014-11-04 Cummins Ltd. SCR exhaust gas aftertreatment device
US8910884B2 (en) 2012-05-10 2014-12-16 Tenneco Automotive Operating Company Inc. Coaxial flow injector
US8973895B2 (en) 2010-02-10 2015-03-10 Tenneco Automotive Operating Company Inc. Electromagnetically controlled injector having flux bridge and flux break
US8978364B2 (en) 2012-05-07 2015-03-17 Tenneco Automotive Operating Company Inc. Reagent injector
US9222391B2 (en) 2013-10-02 2015-12-29 Denso Corporation Exhaust gas purification system
US9347355B2 (en) 2011-09-08 2016-05-24 Tenneco Automotive Operating Company Inc. In-line flow diverter
US9475004B2 (en) 2014-06-06 2016-10-25 Clean Diesel Technologies, Inc. Rhodium-iron catalysts
US9511350B2 (en) 2013-05-10 2016-12-06 Clean Diesel Technologies, Inc. (Cdti) ZPGM Diesel Oxidation Catalysts and methods of making and using same
US9511353B2 (en) 2013-03-15 2016-12-06 Clean Diesel Technologies, Inc. (Cdti) Firing (calcination) process and method related to metallic substrates coated with ZPGM catalyst
US9511358B2 (en) 2013-11-26 2016-12-06 Clean Diesel Technologies, Inc. Spinel compositions and applications thereof
CN106285854A (en) * 2015-05-07 2017-01-04 浙江福爱电子有限公司 A kind of SCR liquid injection apparatus
US9545626B2 (en) 2013-07-12 2017-01-17 Clean Diesel Technologies, Inc. Optimization of Zero-PGM washcoat and overcoat loadings on metallic substrate
US9555400B2 (en) 2013-11-26 2017-01-31 Clean Diesel Technologies, Inc. Synergized PGM catalyst systems including platinum for TWC application
US9683472B2 (en) 2010-02-10 2017-06-20 Tenneco Automotive Operating Company Inc. Electromagnetically controlled injector having flux bridge and flux break
US9700841B2 (en) 2015-03-13 2017-07-11 Byd Company Limited Synergized PGM close-coupled catalysts for TWC applications
US9726063B2 (en) 2011-09-08 2017-08-08 Tenneco Automotive Operating Company Inc. In-line flow diverter
US9731279B2 (en) 2014-10-30 2017-08-15 Clean Diesel Technologies, Inc. Thermal stability of copper-manganese spinel as Zero PGM catalyst for TWC application
US9771534B2 (en) 2013-06-06 2017-09-26 Clean Diesel Technologies, Inc. (Cdti) Diesel exhaust treatment systems and methods
US9861964B1 (en) 2016-12-13 2018-01-09 Clean Diesel Technologies, Inc. Enhanced catalytic activity at the stoichiometric condition of zero-PGM catalysts for TWC applications
US9951706B2 (en) 2015-04-21 2018-04-24 Clean Diesel Technologies, Inc. Calibration strategies to improve spinel mixed metal oxides catalytic converters
US10265684B2 (en) 2017-05-04 2019-04-23 Cdti Advanced Materials, Inc. Highly active and thermally stable coated gasoline particulate filters
US10533472B2 (en) 2016-05-12 2020-01-14 Cdti Advanced Materials, Inc. Application of synergized-PGM with ultra-low PGM loadings as close-coupled three-way catalysts for internal combustion engines
US10704444B2 (en) 2018-08-21 2020-07-07 Tenneco Automotive Operating Company Inc. Injector fluid filter with upper and lower lip seal

Families Citing this family (91)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US7389792B2 (en) * 1998-12-24 2008-06-24 Nl Technologies, Ltd. Dip tube valve assembly
DE19919426C1 (en) * 1999-04-28 2000-03-30 Siemens Ag Valve mounting for dosing valve of IC engine exhaust gas catalyser
DE10107618A1 (en) * 2001-02-17 2002-08-29 Pierburg Ag Valve arrangement for pressure control of the fuel supply in an internal combustion engine
US6669057B2 (en) * 2001-10-31 2003-12-30 Nordson Corporation High-speed liquid dispensing modules
CA2466181A1 (en) * 2001-11-09 2003-05-15 Clean Diesel Technologies, Inc. Continuously-variable control of pollution reducing chemicals for combustion sources
US6814303B2 (en) * 2002-04-03 2004-11-09 Cleaire Advanced Emission Controls Fluid-cooled mount for an injector
US6996976B2 (en) * 2002-04-03 2006-02-14 Cleaire Advanced Emmision Controls Apparatus and method for mounting a device to a pipe
US7497076B2 (en) * 2002-05-07 2009-03-03 Extengine Transport Systems Emission control system
AU2003273138A1 (en) * 2002-05-07 2003-12-12 Extengine Transport Systems Emission control system
US6887284B2 (en) * 2002-07-12 2005-05-03 Dannie B. Hudson Dual homogenization system and process for fuel oil
US6941746B2 (en) * 2002-11-21 2005-09-13 Combustion Components Associates, Inc. Mobile diesel selective catalytic reduction systems and methods
US7337607B2 (en) * 2003-06-12 2008-03-04 Donaldson Company, Inc. Method of dispensing fuel into transient flow of an exhaust system
EP2426328B1 (en) * 2003-09-19 2013-04-10 Nissan Diesel Motor Co., Ltd. Exhaust gas purification device of engine
WO2005028827A1 (en) * 2003-09-19 2005-03-31 Nissan Diesel Motor Co., Ltd. Exhaust gas clarification apparatus for engine
EP1676985B1 (en) * 2003-09-30 2008-07-23 Nissan Diesel Motor Co., Ltd. Exhaust gas purification device of engine
US7186396B2 (en) * 2003-11-26 2007-03-06 Asemblon, Inc. Method for hydrogen storage and delivery
WO2005073527A1 (en) 2004-02-02 2005-08-11 Nissan Diesel Motor Co., Ltd. Device for purifying exhaust gas of internal combustion engine
EP2383444B1 (en) * 2004-02-02 2012-12-19 Nissan Diesel Motor Co., Ltd. Exhaust emission purifying apparatus for engine
DE102004015805B4 (en) * 2004-03-29 2007-07-26 J. Eberspächer GmbH & Co. KG Device for introducing a liquid into an exhaust gas line
DE102004048336A1 (en) * 2004-10-01 2006-04-13 J. Eberspächer GmbH & Co. KG Exhaust system for an internal combustion engine
JP3714559B1 (en) * 2004-11-05 2005-11-09 日産ディーゼル工業株式会社 Exhaust purification device
DE102004056791B4 (en) * 2004-11-24 2007-04-19 J. Eberspächer GmbH & Co. KG exhaust system
DE102004058542A1 (en) * 2004-12-03 2006-06-08 Nordson Corporation, Westlake Rotary applicator head and label applicator for applying labels
US20060196172A1 (en) * 2005-03-02 2006-09-07 Johnson Jeffery S Injection device for the treatment of exhaust fumes from motor vehicles
US7771556B2 (en) 2005-07-01 2010-08-10 Nordson Corporation Apparatus and process to apply adhesive during labeling operations
JP2007032472A (en) * 2005-07-28 2007-02-08 Hitachi Ltd Exhaust gas treatment device using urea water
DE102005061145A1 (en) * 2005-12-21 2007-06-28 Robert Bosch Gmbh Automotive exhaust pipe is shaped to maximize or minimize release of heat to adjacent reduction agent dosing valve upstream from catalytic converter
US20070210926A1 (en) * 2006-03-08 2007-09-13 Chavez Jon P Apparatus and Method for Communicating Cues During a Musical Performance
CN100446838C (en) * 2006-03-29 2008-12-31 宝山钢铁股份有限公司 Atomization jetting device of washing tower
US20070228191A1 (en) * 2006-03-31 2007-10-04 Caterpillar Inc. Cooled nozzle assembly for urea/water injection
US7735756B2 (en) * 2006-04-12 2010-06-15 Combustion Components Associates, Inc. Advanced mechanical atomization for oil burners
JP4662886B2 (en) * 2006-05-26 2011-03-30 ボッシュ株式会社 Exhaust gas purification device for internal combustion engine
US20070277505A1 (en) * 2006-05-30 2007-12-06 Ford Global Technologies, Llc Venting of on-board vehicle emissions treatment system
KR101460967B1 (en) * 2006-05-31 2014-11-13 테네코 오토모티브 오퍼레이팅 컴파니 인코포레이티드 Method and apparatus for reducing emissions in diesel engines
US20070289288A1 (en) * 2006-06-19 2007-12-20 Ford Global Technologies, Llc Venting of on-board vehicle emissions treatment system with pressure assist
JP4804242B2 (en) * 2006-06-26 2011-11-02 Udトラックス株式会社 Engine exhaust purification system
JP4799289B2 (en) * 2006-06-26 2011-10-26 Udトラックス株式会社 Engine exhaust purification system
ATE512300T1 (en) 2006-07-12 2011-06-15 Delphi Tech Holding Sarl DOSING PUMP FOR A REDUCING AGENT
US7497077B2 (en) * 2006-07-26 2009-03-03 Southwest Research Institute System and method for dispensing an aqueous urea solution into an exhaust gas stream
JP4888171B2 (en) * 2006-07-27 2012-02-29 株式会社デンソー Exhaust purification device
US8109077B2 (en) * 2006-10-11 2012-02-07 Tenneco Automotive Operating Company Inc. Dual injector system for diesel emissions control
JP4656039B2 (en) * 2006-10-19 2011-03-23 株式会社デンソー Engine exhaust purification system
US9151201B2 (en) * 2006-11-08 2015-10-06 Continental Automotive Systems, Inc. Laser welded automotive diesel exhaust HC dosing valve
DE102006053485A1 (en) * 2006-11-14 2008-05-15 Robert Bosch Gmbh Method for operating a reagent metering valve and device for carrying out the method
DE102006062491A1 (en) * 2006-12-28 2008-07-03 Robert Bosch Gmbh Fuel dosing device for exhaust gas system of internal combustion engine i.e. diesel engine, has damping device provided for damping pressure oscillation and connected with fuel inlet that is fed from low pressure system of injection system
US8171721B2 (en) 2007-01-22 2012-05-08 International Engine Intellectual Property Company, Llc Closed loop control of exhaust system fluid dosing
EP2121144B1 (en) * 2007-03-08 2012-11-21 Mack Trucks, Inc. Aftertreatment injector anti-fouling device
US7818960B2 (en) 2007-03-14 2010-10-26 Gm Global Technology Operations, Inc. SCR cold start heating system for a diesel exhaust
EP2538048B1 (en) * 2007-03-30 2015-03-04 Continental Automotive Systems US, Inc. Reductant delivery unit for selective catalytic reduction
US7797932B2 (en) * 2007-04-30 2010-09-21 Cummins, Inc Apparatus and system for enhancing aftertreatment regeneration
JP4174685B1 (en) * 2007-05-31 2008-11-05 三菱自動車工業株式会社 Exhaust gas purification device for internal combustion engine
US8056326B2 (en) 2007-05-31 2011-11-15 Caterpillar Inc. Regeneration device having cooled injection housing
EP2014885B1 (en) * 2007-07-09 2010-11-17 Delphi Technologies Holding S.à.r.l. A reagent dosing system
JP5001793B2 (en) * 2007-11-13 2012-08-15 三菱ふそうトラック・バス株式会社 Exhaust purification device
US20090137350A1 (en) * 2007-11-26 2009-05-28 Jason Lenig Game Ball with Enhanced in Flight Movement
US8127538B2 (en) * 2008-03-21 2012-03-06 Ford Global Technologies, Llc Liquid injector assembly with a flanged connector connection
EP2105592B1 (en) * 2008-03-28 2010-03-24 Magneti Marelli S.p.A. Mounting device for an injector in an exhaust system of an internal combustion engine
US8499550B2 (en) * 2008-05-20 2013-08-06 Cummins Ip, Inc. Apparatus, system, and method for controlling particulate accumulation on an engine filter during engine idling
DE102008049097A1 (en) * 2008-09-26 2010-04-01 Daimler Ag A motor vehicle with a system for supplying liquid into another medium, in particular for supplying a reducing agent into the exhaust gas of an internal combustion engine
US7980483B2 (en) * 2008-10-13 2011-07-19 Eaton Corporation Injector for a fluid injection system
US8459012B2 (en) * 2008-11-19 2013-06-11 Caterpillar Inc. Method for purging a dosing system
US7966979B2 (en) * 2009-01-26 2011-06-28 Caterpillar Inc. Mounting and cooling device for emissions system electronics
CN102301124B (en) * 2009-02-02 2014-12-24 坦尼科汽车营业公司 Injector mounting system
US8517284B2 (en) 2009-05-13 2013-08-27 Caterpillar Inc. System and method for internal cooling of a fuel injector
FR2949532B1 (en) * 2009-09-03 2011-09-23 Air Liquide CALORIFYING THE PIPES OF A CRYOGENIC FLUID JET WORKPLACE
US8429903B2 (en) * 2009-12-22 2013-04-30 Caterpillar Inc. Radial mounting for regeneration device
US8789361B2 (en) * 2010-01-26 2014-07-29 Deere & Company Diesel aftertreatment regeneration system and method
SE536873C2 (en) * 2010-06-21 2014-10-14 Scania Cv Ab HC dosing system for exhaust gas purification and method of cooling thereof
SE534974C2 (en) * 2010-06-21 2012-03-06 Scania Cv Ab Method and apparatus for determining the minimum level of a reducing agent container in an SCR system based on the cooling needs of a dosing unit
US8549840B2 (en) 2010-11-12 2013-10-08 Cummins Cal Pacific, Llc Fluid injector
CN101988412A (en) * 2010-11-12 2011-03-23 无锡市凯龙汽车设备制造有限公司 SCR (selective catalyst reduction) injector head of diesel engine
CN103649479A (en) * 2011-04-04 2014-03-19 马克卡车公司 Fluid cooled injector and exhaust aftertreatment system, vehicle, and method using a fluid cooled injector
DE102011075381A1 (en) * 2011-05-06 2012-11-08 Robert Bosch Gmbh Injector for metering reducing agent to the exhaust gas of an internal combustion engine
US8910882B2 (en) 2011-06-23 2014-12-16 Caterpillar Inc. Fuel injector having reduced armature cavity pressure
US20130126644A1 (en) * 2011-11-22 2013-05-23 Jeremy Popovich Threaded Injector Mount
US20140054394A1 (en) * 2012-08-27 2014-02-27 Continental Automotive Systems Us, Inc. Reductant delivery unit for automotive selective catalytic reduction systems - active cooling
DE102013211684A1 (en) * 2013-06-20 2014-12-24 Robert Bosch Gmbh Heat sink for injector
JP6111948B2 (en) * 2013-09-19 2017-04-12 トヨタ自動車株式会社 Exhaust gas purification device for internal combustion engine
JP6177641B2 (en) * 2013-09-26 2017-08-09 株式会社ニフコ Lid mounting member
DE102014215084C5 (en) * 2014-07-31 2023-10-05 Purem GmbH Injection device and associated manufacturing process
JP6345628B2 (en) * 2015-05-26 2018-06-20 コベルコ建機株式会社 Gasket for reducing agent injector and exhaust gas aftertreatment device having the same
US10605213B2 (en) * 2015-08-21 2020-03-31 Cummins Inc. Nozzle combustion shield and sealing member with improved heat transfer capabilities
DE102016209269A1 (en) * 2016-05-30 2017-11-30 Robert Bosch Gmbh Heatsink for an injection / metering valve
US11111836B2 (en) 2017-05-29 2021-09-07 Liebherr-Components Colmar Sas Reductant injection system
US10753252B2 (en) * 2017-06-14 2020-08-25 Vitesco Technologies USA, LLC. Thermally isolated reductant dosing unit with hermetic seal
US10738256B1 (en) 2017-12-22 2020-08-11 TerSol, LLC Fuel additive systems, compositions, and methods
JP2020176602A (en) * 2019-04-22 2020-10-29 株式会社デンソー Fluid injection device and fluid injection system
US11261775B2 (en) 2019-04-26 2022-03-01 Liebherr-Components Colmar Sas Reductant dosing system for an SCR catalyst
US11268417B2 (en) 2019-06-26 2022-03-08 Cummins Emission Solutions Inc. Liquid only lance injector
US11225716B2 (en) 2019-11-27 2022-01-18 Tokyo Electron Limited Internally cooled multi-hole injectors for delivery of process chemicals
CN115246662A (en) * 2021-04-27 2022-10-28 邢台旭阳煤化工有限公司 Treatment device and treatment method for benzene hydrogenation wastewater

Citations (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2540663A (en) * 1946-11-25 1951-02-06 Merit Engineering And Mfg Co Spray device
US3680537A (en) * 1969-04-17 1972-08-01 Nippon Denso Co Fuel supply device for internal combustion engines
US4964471A (en) * 1989-09-01 1990-10-23 Cominco Ltd. Sprinkler system and sprinkler assembly therefor
US5021227A (en) * 1989-02-02 1991-06-04 Nippon Shokubai Kagaku Kogyo Co., Ltd. Method of removing nitrogen oxides in exhaust gases from a diesel engine
US5184462A (en) * 1991-03-19 1993-02-09 Oskar Schatz Method and an apparatus for the treatment of exhaust gas from an IC engine
US5189876A (en) * 1990-02-09 1993-03-02 Toyota Jidosha Kabushiki Kaisha Exhaust gas purification system for an internal combustion engine
US5209061A (en) * 1991-03-13 1993-05-11 Toyota Jidosha Kabushiki Kaisha Exhaust gas purification system for an internal combustion engine
US5260042A (en) * 1989-10-24 1993-11-09 Martin Gmbh Fur Umwelt-Und Energietechnik Method for introducing a treatment medium into the waste gas flow in combustion processes
US5522218A (en) * 1994-08-23 1996-06-04 Caterpillar Inc. Combustion exhaust purification system and method
US5620142A (en) * 1992-07-23 1997-04-15 Elkas; Michael V. Jeweled orifice fog nozzle
US5753188A (en) * 1995-07-13 1998-05-19 Hino Motors, Ltd. Apparatus for purifying the exhaust gas of diesel engines
US5976475A (en) * 1997-04-02 1999-11-02 Clean Diesel Technologies, Inc. Reducing NOx emissions from an engine by temperature-controlled urea injection for selective catalytic reduction

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE2644135A1 (en) * 1976-09-30 1978-04-06 Daimler Benz Ag Fuel injection valve cooled by fuel - has supply sealed from return by spring loaded ring between fixed tube and hollow valve needle

Patent Citations (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2540663A (en) * 1946-11-25 1951-02-06 Merit Engineering And Mfg Co Spray device
US3680537A (en) * 1969-04-17 1972-08-01 Nippon Denso Co Fuel supply device for internal combustion engines
US5021227A (en) * 1989-02-02 1991-06-04 Nippon Shokubai Kagaku Kogyo Co., Ltd. Method of removing nitrogen oxides in exhaust gases from a diesel engine
US4964471A (en) * 1989-09-01 1990-10-23 Cominco Ltd. Sprinkler system and sprinkler assembly therefor
US5260042A (en) * 1989-10-24 1993-11-09 Martin Gmbh Fur Umwelt-Und Energietechnik Method for introducing a treatment medium into the waste gas flow in combustion processes
US5189876A (en) * 1990-02-09 1993-03-02 Toyota Jidosha Kabushiki Kaisha Exhaust gas purification system for an internal combustion engine
US5209061A (en) * 1991-03-13 1993-05-11 Toyota Jidosha Kabushiki Kaisha Exhaust gas purification system for an internal combustion engine
US5184462A (en) * 1991-03-19 1993-02-09 Oskar Schatz Method and an apparatus for the treatment of exhaust gas from an IC engine
US5620142A (en) * 1992-07-23 1997-04-15 Elkas; Michael V. Jeweled orifice fog nozzle
US5522218A (en) * 1994-08-23 1996-06-04 Caterpillar Inc. Combustion exhaust purification system and method
US5753188A (en) * 1995-07-13 1998-05-19 Hino Motors, Ltd. Apparatus for purifying the exhaust gas of diesel engines
US5976475A (en) * 1997-04-02 1999-11-02 Clean Diesel Technologies, Inc. Reducing NOx emissions from an engine by temperature-controlled urea injection for selective catalytic reduction

Cited By (50)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2005005799A1 (en) * 2003-07-09 2005-01-20 Robert Bosch Gmbh Cooled device for metering reducing agent to the exhaust gas of a combustion engine
EP1751407A4 (en) * 2004-04-26 2009-04-01 Tenneco Automotive Operating Methods and apparatus for injecting atomized fluid
US8047452B2 (en) 2004-04-26 2011-11-01 Tenneco Automotive Operating Company Inc. Method and apparatus for injecting atomized fluids
US20090179087A1 (en) * 2004-04-26 2009-07-16 Martin Scott M Method and apparatus for injecting atomized fluids
EP1751407A2 (en) * 2004-04-26 2007-02-14 Combustion Components Associates, Inc. Methods and apparatus for injecting atomized fluid
US8074673B2 (en) 2004-05-18 2011-12-13 Hydraulik-Ring Gmbh Freeze-resistant metering valve
WO2007124791A1 (en) * 2006-05-03 2007-11-08 Purem Abgassysteme Gmbh & Co. Kg Method and device for metering a reducing agent into the exhaust system of an internal combustion engine
WO2007124779A1 (en) * 2006-05-03 2007-11-08 Purem Abgassysteme Gmbh & Co. Kg Process and device for dosing a reducing agent in an exhaust system of an internal combustion engine
US8266892B2 (en) 2007-01-25 2012-09-18 Friedrich Zapf Calibrated dosing unit, especially of an exhaust gas treatment unit
US8875491B2 (en) 2007-01-25 2014-11-04 Cummins Ltd. Exhaust gas aftertreatment system and method
US20090229258A1 (en) * 2008-03-05 2009-09-17 Hydraulik-Ring Gmbh Exhaust-Gas Aftertreatment Device
US8959895B2 (en) 2008-03-05 2015-02-24 Cummins Ltd. Exhaust-gas aftertreatment device
US8201393B2 (en) 2008-03-05 2012-06-19 Hilite Germany Gmbh Exhaust-gas aftertreatment device
US20120110990A1 (en) * 2009-07-27 2012-05-10 Robert Bosch Gmbh Mounting unit for fastening an injection member to an exhaust gas tract
US8776510B2 (en) * 2009-07-27 2014-07-15 Robert Bosch Gmbh Mounting unit for fastening an injection member to an exhaust gas tract
US20110023466A1 (en) * 2009-08-03 2011-02-03 Hydraulik-Ring Gmbh SCR exhaust gas aftertreatment device
US8938949B2 (en) 2009-08-03 2015-01-27 Cummins Ltd. SCR exhaust gas aftertreatment device
US8998114B2 (en) 2010-02-10 2015-04-07 Tenneco Automotive Operating Company, Inc. Pressure swirl flow injector with reduced flow variability and return flow
US8740113B2 (en) 2010-02-10 2014-06-03 Tenneco Automotive Operating Company, Inc. Pressure swirl flow injector with reduced flow variability and return flow
US8973895B2 (en) 2010-02-10 2015-03-10 Tenneco Automotive Operating Company Inc. Electromagnetically controlled injector having flux bridge and flux break
US20110192140A1 (en) * 2010-02-10 2011-08-11 Keith Olivier Pressure swirl flow injector with reduced flow variability and return flow
US9683472B2 (en) 2010-02-10 2017-06-20 Tenneco Automotive Operating Company Inc. Electromagnetically controlled injector having flux bridge and flux break
US8438839B2 (en) 2010-10-19 2013-05-14 Tenneco Automotive Operating Company Inc. Exhaust gas stream vortex breaker
US8875502B2 (en) 2010-12-14 2014-11-04 Cummins Ltd. SCR exhaust gas aftertreatment device
US10077702B2 (en) 2011-09-08 2018-09-18 Tenneco Automotive Operating Company Inc. In-line flow diverter
US8677738B2 (en) 2011-09-08 2014-03-25 Tenneco Automotive Operating Company Inc. Pre-injection exhaust flow modifier
US9726063B2 (en) 2011-09-08 2017-08-08 Tenneco Automotive Operating Company Inc. In-line flow diverter
US9347355B2 (en) 2011-09-08 2016-05-24 Tenneco Automotive Operating Company Inc. In-line flow diverter
US10465582B2 (en) 2012-05-07 2019-11-05 Tenneco Automotive Operating Company Inc. Reagent injector
US8978364B2 (en) 2012-05-07 2015-03-17 Tenneco Automotive Operating Company Inc. Reagent injector
US9759113B2 (en) 2012-05-10 2017-09-12 Tenneco Automotive Operating Company Inc. Coaxial flow injector
US8910884B2 (en) 2012-05-10 2014-12-16 Tenneco Automotive Operating Company Inc. Coaxial flow injector
US9511353B2 (en) 2013-03-15 2016-12-06 Clean Diesel Technologies, Inc. (Cdti) Firing (calcination) process and method related to metallic substrates coated with ZPGM catalyst
US9511350B2 (en) 2013-05-10 2016-12-06 Clean Diesel Technologies, Inc. (Cdti) ZPGM Diesel Oxidation Catalysts and methods of making and using same
US9771534B2 (en) 2013-06-06 2017-09-26 Clean Diesel Technologies, Inc. (Cdti) Diesel exhaust treatment systems and methods
US9545626B2 (en) 2013-07-12 2017-01-17 Clean Diesel Technologies, Inc. Optimization of Zero-PGM washcoat and overcoat loadings on metallic substrate
US9222391B2 (en) 2013-10-02 2015-12-29 Denso Corporation Exhaust gas purification system
US9511358B2 (en) 2013-11-26 2016-12-06 Clean Diesel Technologies, Inc. Spinel compositions and applications thereof
US9555400B2 (en) 2013-11-26 2017-01-31 Clean Diesel Technologies, Inc. Synergized PGM catalyst systems including platinum for TWC application
US9475004B2 (en) 2014-06-06 2016-10-25 Clean Diesel Technologies, Inc. Rhodium-iron catalysts
US9475005B2 (en) 2014-06-06 2016-10-25 Clean Diesel Technologies, Inc. Three-way catalyst systems including Fe-activated Rh and Ba-Pd material compositions
US9579604B2 (en) 2014-06-06 2017-02-28 Clean Diesel Technologies, Inc. Base metal activated rhodium coatings for catalysts in three-way catalyst (TWC) applications
US9731279B2 (en) 2014-10-30 2017-08-15 Clean Diesel Technologies, Inc. Thermal stability of copper-manganese spinel as Zero PGM catalyst for TWC application
US9700841B2 (en) 2015-03-13 2017-07-11 Byd Company Limited Synergized PGM close-coupled catalysts for TWC applications
US9951706B2 (en) 2015-04-21 2018-04-24 Clean Diesel Technologies, Inc. Calibration strategies to improve spinel mixed metal oxides catalytic converters
CN106285854A (en) * 2015-05-07 2017-01-04 浙江福爱电子有限公司 A kind of SCR liquid injection apparatus
US10533472B2 (en) 2016-05-12 2020-01-14 Cdti Advanced Materials, Inc. Application of synergized-PGM with ultra-low PGM loadings as close-coupled three-way catalysts for internal combustion engines
US9861964B1 (en) 2016-12-13 2018-01-09 Clean Diesel Technologies, Inc. Enhanced catalytic activity at the stoichiometric condition of zero-PGM catalysts for TWC applications
US10265684B2 (en) 2017-05-04 2019-04-23 Cdti Advanced Materials, Inc. Highly active and thermally stable coated gasoline particulate filters
US10704444B2 (en) 2018-08-21 2020-07-07 Tenneco Automotive Operating Company Inc. Injector fluid filter with upper and lower lip seal

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US6279603B1 (en) 2001-08-28
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CN1483924A (en) 2004-03-24
EP1117469A4 (en) 2002-06-05

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