Patent Grant
11828214
The present disclosure relates generally to aftertreatment systems for treating constituents of an exhaust gas produced by the engine.
Exhaust aftertreatment systems are used to receive and treat exhaust gas generated by internal combustion engines. Generally exhaust gas aftertreatment systems include any of several different components to reduce the levels of harmful exhaust emissions present in the exhaust gas. For example, certain exhaust gas aftertreatment systems for diesel-powered internal combustion engines include a selective catalytic reduction (SCR) system including a catalyst formulated to convert NOx (NO and NO2 in some fraction) into harmless nitrogen gas (N2) and water vapor (H2O) in the presence of ammonia (NH3). Generally in such aftertreatment systems, an exhaust reductant, (e.g., a diesel exhaust fluid such as urea) is injected into the SCR system to provide a source of ammonia, and mixed with the exhaust gas to partially reduce the NOx gases. The reduction byproducts of the exhaust gas are then fluidly communicated to the catalyst included in the SCR system to decompose substantially all of the NOx gases into relatively harmless byproducts, which are expelled out of the aftertreatment system. Mounting of aftertreatment systems that include various components on structures such as vehicle chassis is dictated by the amount of space available. Specifically, increasing emission regulations have made it challenging to incorporate a plurality of aftertreatment components in limited space available on mounting structures.
Embodiments described herein relate generally to aftertreatment systems and architectures that include a housing within which the various aftertreatment components of the aftertreatment system are disposed. In particular, various embodiments of the aftertreatment system described herein include a housing defining two or more internal volumes that are fluidly isolated from each other. A plurality of aftertreatment legs are disposed within the housing, each leg including one or more aftertreatment components. Exhaust gas is emitted by at least one of the aftertreatment legs into one of the fluidly isolated internal volumes before being transmitted to a downstream aftertreatment leg.
In some embodiments, an aftertreatment system for treating constituents of an exhaust gas, comprises: a housing defining at least a first internal volume and a second internal volume that is fluidly isolated from the first internal volume; a first aftertreatment leg extending from the first internal volume to the second internal volume, the first aftertreatment leg comprising: a temperature control aftertreatment component extending along a first axis and configured to receive at least a portion of the exhaust gas via an inlet conduit fluidly coupled to the temperature control aftertreatment component, and an oxidation catalyst disposed downstream of the temperature control aftertreatment component and axially aligned with the temperature control aftertreatment component, an outlet of the oxidation catalyst being disposed in the second internal volume; a second aftertreatment leg extending from the second internal volume to the first internal volume, the second aftertreatment leg comprising: a filter extending along a second axis that is offset from the first axis, the filter configured to receive the exhaust gas from the oxidation catalyst through the second internal volume, an outlet of the filter disposed within the first internal volume and configured to emit exhaust gas into the first internal volume after passing through the filter; a third aftertreatment leg extending from the first internal volume to the second internal volume, the third aftertreatment leg comprising: at least one selective catalytic reduction (SCR) catalyst disposed in at least the first internal volume and extending along a SCR axis that is offset from the first axis and the second axis, an inlet of the at least one SCR catalyst being disposed in the second internal volume; a decomposition tube extending from the first internal volume to the second internal volume along an axis that is offset from each of the first and second axis, an inlet of the decomposition tube being disposed in the first internal volume such that the decomposition tube is configured to receive the exhaust gas emitted into the first internal volume, and to communicate the exhaust gas from the first internal volume to the inlet of the at least one SCR catalyst in the second internal volume; and a reductant injection inlet proximate to the inlet of the decomposition tube and configured to allow reductant to be injected into the decomposition tube.
In some embodiments, the inlet of the decomposition tube is oriented at an angle that is perpendicular to the axis of the decomposition tube and located proximate to the outlet of the filter.
In some embodiments, the inlet of the decomposition tube comprises: a flat end face on which the reductant injector is mounted; and a plurality of pores defined through a wall of the decomposition tube at the inlet of the decomposition tube and configured to allow the exhaust gas to enter the decomposition tube.
In some embodiments, the at least one SCR catalyst comprises: a first SCR catalyst extending along a first SCR axis, and a second SCR catalyst extending along a second SCR axis that is parallel to and offset from the first SCR axis, and the aftertreatment system further comprises a SCR inlet plenum disposed in the first internal volume and fluidly coupled to respective inlets of the first and second SCR catalysts, an outlet of the decomposition tube is fluidly coupled to the SCR inlet plenum, and the SCR inlet plenum is configured to redirect exhaust gas flowing therein towards respective inlets of the first and second SCR catalysts.
In some embodiments, an SCR outlet plenum is disposed in the second internal volume and coupled to respective outlets of the first and second SCR catalysts, the SCR outlet plenum defining an outlet conduit that extends through a sidewall of the housing.
In some embodiments, the at least one SCR catalyst comprises: a first SCR catalyst extending along a first SCR axis, and a second SCR catalyst extending along a second SCR axis that is parallel to and offset from the first SCR axis, wherein a first linear distance from the first axis to the first SCR axis is substantially equal to a second linear distance from the first axis to the second SCR axis, the aftertreatment system further comprises a SCR inlet plenum disposed in the first internal volume and fluidly coupled to each of the first and second SCR catalysts, a linear distance from the first axis to the axis of the decomposition tube is greater than the first linear distance and the second linear distance, and the outlet of the decomposition tube is fluidly coupled to the SCR inlet plenum.
In some embodiments, the aftertreatment system further comprises: an SCR outlet plenum disposed in the second internal volume and fluidly coupled to respective outlets of each of the first and second SCR catalysts, the SCR outlet plenum having an outlet that is fluidly coupled to the first internal volume and configured to emit treated exhaust gas into the first internal volume; and an outlet conduit coupled to a sidewall of the housing forming the first internal volume and configured to expel the treated exhaust gas into the environment.
In some embodiments, a groove is defined in a sidewall of the SCR outlet plenum that is perpendicular to the first and second SCR axes, a portion of the inlet of the decomposition tube being disposed in the groove.
In some embodiments, the at least one SCR catalyst comprises: a first SCR catalyst extending along a first SCR axis, a second SCR catalyst extending along a second SCR axis that is parallel to and offset from the first SCR axis, and a third SCR catalyst extending along a third SCR axis that is parallel to and offset from the first SCR axis and the second SCR axis, and the aftertreatment system further comprises a SCR inlet plenum disposed in the first internal volume and fluidly coupled to each of the first, second, and third SCR catalysts, the decomposition tube is disposed proximate to a central portion of the housing, and the outlet of the decomposition tube being fluidly coupled to the SCR inlet plenum.
In some embodiments, the aftertreatment system further comprises: an SCR outlet plenum disposed in the second internal volume and coupled to respective outlets of each of the first, second, and third SCR catalysts, the SCR outlet plenum having an outlet that is fluidly coupled to the first internal volume and configured to release treated exhaust gas into the first internal volume; and an outlet conduit coupled to a sidewall of the housing forming the first internal volume and configured to expel the treated exhaust gas into the environment
In some embodiments, the oxidation catalyst is a first oxidation catalyst and the filter is a first filter, and the first aftertreatment leg further comprises: a second oxidation catalyst extending along a second axis that is parallel to the first axis, a first aftertreatment leg inlet plenum disposed in the first internal volume, the first aftertreatment leg inlet plenum coupled to an inlet of each of the first oxidation catalyst, the second oxidation catalyst, and the inlet conduit, the first aftertreatment leg inlet plenum configured to communicate a first portion of the exhaust gas to the first oxidation catalyst and a second portion of the exhaust gas to the second oxidation catalyst, and a second filter disposed downstream of the second oxidation catalyst and axially aligned with the second oxidation catalyst, an outlet of the second filter disposed in the second internal volume, wherein: the first filter is configured to emit the first portion of the exhaust gas and the second filter is configured to emit the second portion of the exhaust gas into the second internal volume, respectively, and the decomposition tube is configured to receive each of the first portion and the second portion of the exhaust gas.
In some embodiments, the at least one SCR catalyst comprises: a first SCR catalyst extending along a first SCR axis, and a second SCR catalyst extending along a second SCR axis that is parallel to and offset from the first SCR axis, the first SCR axis is parallel to and offset from the first axis, and the second SCR axis is parallel to and offset from the second axis.
In some embodiments, the aftertreatment system further comprises: a SCR inlet plenum disposed in the first internal volume and fluidly coupled to respective inlets of each of the first and second SCR catalysts, the SCR inlet plenum configured to redirect exhaust gas flowing therein towards respective inlets of each of the first and second SCR catalysts, wherein the decomposition tube is disposed proximate to a central portion of the housing such that the decomposition tube is surrounded by the first aftertreatment leg and the second aftertreatment leg, the outlet of the decomposition tube being fluidly coupled to the SCR inlet plenum.
In some embodiments, the aftertreatment system further comprises: an SCR outlet plenum disposed in the second internal volume and coupled to respective outlets of each of the first and second SCR catalysts, the SCR outlet plenum having an outlet that is fluidly coupled to the first internal volume and configured to release treated exhaust gas into the first internal volume; and an outlet conduit coupled to a sidewall of the housing forming the first internal volume and configured to expel the treated exhaust gas into the environment.
In some embodiments, the inlet conduit comprises an inlet cone that has a constantly expanding cross-section from an upstream end to a downstream end thereof, the downstream end coupled to the first aftertreatment leg.
In some embodiments, an aftertreatment system for treating constituents of an exhaust gas, comprises: a housing defining at least a first internal volume and a second internal volume that is fluidly isolated from the first internal volume; a first aftertreatment leg extending from the first internal volume to the second internal volume, the first aftertreatment leg comprising: a temperature control aftertreatment component extending along a first axis and configured to receive at least a portion of the exhaust gas via an inlet conduit fluidly coupled to the temperature control aftertreatment component, and an oxidation catalyst disposed downstream of the temperature control aftertreatment component and axially aligned with the temperature control aftertreatment component, an outlet of the oxidation catalyst being disposed in the second internal volume; a second aftertreatment leg extending from the second internal volume to the first internal volume parallel to the first aftertreatment leg, the second aftertreatment leg comprising: a filter configured to receive the exhaust gas from the oxidation catalyst through the second internal volume, an outlet of the filter disposed within the first internal volume and configured to emit exhaust gas into the first internal volume after passing through the filter; a third aftertreatment leg extending from the first internal volume to the second internal volume, the third aftertreatment leg comprising: at least one SCR catalyst disposed in at least the first internal volume and extending along a SCR axis that is parallel to and offset from the first axis, an inlet of the at least one SCR catalyst being disposed in the second internal volume; a decomposition tube extending from the first internal volume to the second internal volume along an axis that is parallel to and offset from each of the first and second axis, an inlet of the decomposition tube being disposed in the first internal volume such that the decomposition tube is configured to receive the exhaust gas emitted into the first internal volume, and to communicate the exhaust gas from the first internal volume to the inlet of the at least one SCR catalyst in the second internal volume; and a reductant injection inlet proximate to the inlet of the decomposition tube and configured to allow reductant to be injected into the decomposition tube.
In some embodiments, the at least one SCR catalyst comprises: a first SCR catalyst extending along a first SCR axis, and a second SCR catalyst extending along a second SCR axis that is parallel to and offset from the first SCR axis, the first SCR axis is parallel to the first axis, and the second SCR axis is parallel to the second axis.
In some embodiments, the aftertreatment system further comprises: a SCR inlet plenum disposed in the second internal volume and fluidly coupled to each of the first and second SCR catalysts, the SCR inlet plenum configured to redirect exhaust gas flowing therein towards respective inlets of each of the first and second SCR catalysts, wherein the decomposition tube is disposed proximate to a central portion of the housing such that the decomposition tube is surrounded by the first aftertreatment leg and the second aftertreatment leg, the outlet of the decomposition tube being fluidly coupled to the SCR inlet plenum.
In some embodiments, the temperature control aftertreatment component comprises a Vanadium SCR catalyst.
In some embodiments, the aftertreatment system further comprises a hydrocarbon injector disposed on the first aftertreatment leg and configured to insert hydrocarbons into the exhaust gas downstream of the temperature control aftertreatment component and upstream of the oxidation catalyst.
It should be appreciated that all combinations of the foregoing concepts and additional concepts discussed in greater detail below (provided such concepts are not mutually inconsistent) are contemplated as being part of the inventive subject matter disclosed herein. In particular, all combinations of claimed subject matter appearing at the end of this disclosure are contemplated as being part of the inventive subject matter disclosed herein.
The foregoing and other features of the present disclosure will become more fully apparent from the following description and appended claims, taken in conjunction with the accompanying drawings. Understanding that these drawings depict only several implementations in accordance with the disclosure and are therefore, not to be considered limiting of its scope, the disclosure will be described with additional specificity and detail through use of the accompanying drawings.
Reference is made to the accompanying drawings throughout the following detailed description. In the drawings, similar symbols typically identify similar components, unless context dictates otherwise. The illustrative implementations described in the detailed description, drawings, and claims are not meant to be limiting. Other implementations may be utilized, and other changes may be made, without departing from the spirit or scope of the subject matter presented here. It will be readily understood that the aspects of the present disclosure, as generally described herein, and illustrated in the figures, can be arranged, substituted, combined, and designed in a wide variety of different configurations, all of which are explicitly contemplated and made part of this disclosure.
Embodiments described herein relate generally to aftertreatment systems and architectures that include a housing within which the various aftertreatment components of the aftertreatment system are disposed. In particular, various embodiments of the aftertreatment system described herein include a housing defining two or more internal volumes that are fluidly isolated from each other. A plurality of aftertreatment legs are disposed within the housing, each leg including one or more aftertreatment components. Exhaust gas is emitted by at least one of the aftertreatment legs into one of the fluidly isolated internal volumes before being transmitted to a downstream aftertreatment leg.
Various embodiments of the aftertreatment systems described herein may provide one or more benefits including, for example: 1) allowing packaging of a plurality of aftertreatment components into a compact space within a housing reducing space required for mounting the aftertreatment system; 2) allowing for increased catalyst frontal area while supporting various architectures; 3) providing configurable legs or sections in the main flow path allowing for packing various aftertreatment components or subcomponents; and 4) meeting emission regulations while meeting space demands.
It should be appreciated that various outer surfaces are shown as being transparent in the figures, this is solely to allow the internal components of the system to be seen. The outer surfaces may be opaque, translucent, transparent, or a combination thereof.
The housing 170 is configured to house each of the components of the aftertreatment system 100. The housing 170 may be formed from a rigid, heat-resistant and corrosion-resistant material, for example stainless steel, iron, aluminum, metals, ceramics, or any other suitable material. The housing 170 may have any suitable cross-section, for example, circular, square, rectangular, oval, elliptical, polygonal, or any other suitable shape. In various embodiments, the housing 170 may be divided into at least a first internal volume and a second internal volume that are fluidly isolated from each other. The various components of the aftertreatment system 100 may extend across the first and second internal volumes and may release exhaust gas into or uptake exhaust gas from one of the first or second internal volumes. The various components may be disposed in a horizontal, vertical, or any other orientation within the housing 170 and may be oriented parallel or perpendicular to one another.
The aftertreatment system 100 includes an inlet conduit 102 configured to receive the exhaust gas from the engine and communicate the exhaust gas to the oxidation catalyst 110 disposed within the housing 170. One or more sensors may be positioned in the inlet conduit 102. These may include, for example, a NOx sensor (e.g., a physical or virtual NOx sensor), an oxygen sensor, a particulate matter sensor, a carbon monoxide sensor, a temperature sensor, a pressure sensor, any other sensor or a combination thereof configured to measure one or more operational parameters of the exhaust gas. Such operating parameters may include, for example, an amount of NOx gases in the exhaust gas, a temperature of the exhaust gas, a flow rate and/or pressure of the exhaust gas. Furthermore, an outlet conduit 104 may be coupled to an outlet of the housing 170 and structured to expel treated exhaust gas into the environment (e.g., treated to remove particulate matter such as soot by the filter 120 and/or reduce constituents of the exhaust gas such as NOx gases, CO, unburnt hydrocarbons, etc. included in the exhaust gas by the SCR catalyst 150 and the oxidation catalyst 110). Various sensors may include a second NOx sensor disposed in the outlet conduit, which is configured to determine an amount of NOx gases expelled into the environment after passing through the aftertreatment components. Others sensors may include, for example, a particulate matter sensor configured to determine an amount of particulate matter (e.g., soot included in the exhaust gas exiting the filter 140) in the exhaust gas being expelled into the environment, or an ammonia sensor configured to measure an amount of ammonia in the exhaust gas flowing out of the SCR catalyst 150, i.e., determine the ammonia slip.
The oxidation catalyst 110 (e.g., a diesel oxidation catalyst) is configured to decompose unburnt hydrocarbons present in the exhaust gas and/or oxidize CO to CO2. In some embodiments, the aftertreatment system 100 may also include a hydrocarbon insertion assembly 116 configured to selectively insert hydrocarbons (e.g., diesel) into the oxidation catalyst 110. The hydrocarbons combust across the oxidation catalyst 110 and increase the temperature of the exhaust gas to a temperature (e.g., greater than 500 degrees Celsius), for example, to regenerate the filter 120 and/or the SCR catalyst 150. A first heater 108 may be operatively coupled to the oxidation catalyst 110 and configured to heat the oxidation catalyst 110 to a light off temperature of the oxidation catalyst at which the oxidation catalyst 110 catalyzes the combustion of the inserted hydrocarbons for increasing the temperature of the exhaust gas.
The filter 120 is disposed downstream of the oxidation catalyst 110 and upstream of the SCR catalyst 150 and configured to remove particulate matter (e.g., soot, debris, inorganic particles, etc.) from the exhaust gas. In various embodiments, the filter 120 may include a ceramic filter. In some embodiments, the filter 120 may include a cordierite or silicon carbide filter which can, for example, be an asymmetric filter. In yet other embodiments, the filter 120 may be catalyzed. In some embodiments, a second heater 122 (e.g., an electric heater) may be coupled to the filter 120 and configured to heat the filter 120 to a regeneration temperature to remove particular matter accumulated on the filter 120.
A mixer 130 is disposed between the filter 120 and the SCR catalyst 150. The mixer 130 may include baffles or veins that are configured to mix reductant inserted into the exhaust gas with the exhaust gas before the exhaust gas is communicated into the SCR catalyst 150. In various embodiments, the mixer 130 may be disposed within a decomposition tube.
In some embodiments, the aftertreatment system 100 includes a reductant storage tank 112 that contains a reductant formulated to facilitate reduction of the constituents of the exhaust gas (e.g., NOx gases) by the SCR catalyst 150. In embodiments in which the exhaust gas is a diesel exhaust gas, the reductant may include a diesel exhaust fluid (DEF) which provides a source of ammonia. Suitable DEFs can include urea, aqueous solution of urea or any other DEF (e.g., the DEF available under the tradename ADBLUE®). In particular embodiments, the reductant includes an aqueous urea solution containing 32.5 wt % urea and 67.5 wt % de-ionized water. In other embodiments, the reductant includes aqueous urea solution containing 40 wt % urea and 60 wt % de-ionized water.
The reductant insertion assembly 114 is fluidly coupled to the reductant storage tank 112 and is configured to provide the reductant to a reductant injector 156 positioned upstream of or mounted on the mixer 130. In various embodiments, the reductant injector 156 may comprise a nozzle having a predetermined diameter. In various embodiments, the reductant injector 156 may be positioned in a reductant port and structured to deliver a stream or a jet of the reductant into the internal volume of the housing 170 so as to deliver the reductant to the SCR catalyst 150.
The reductant insertion assembly 114 may comprise various structures to facilitate receipt of the reductant from the reductant storage tank 112 and delivery to the reductant injector 156 for insertion into the mixer 130. The reductant insertion assembly 114 may include one or more pumps (e.g., a diaphragm pump, a positive displacement pump, a centrifugal pump, a vacuum pump, etc.) for delivering the reductant to the reductant injector 156 at an operating pressure and/or flow rate. The reductant insertion assembly 114 may also include filters and/or screens (e.g., to prevent solid particles of the reductant or contaminants from flowing into the one or more pumps) and/or valves (e.g., check valves) configured to draw reductant from the reductant storage tank 112. Screens, check valves, pulsation dampers, or other structures may also be positioned downstream of the one or more pumps of the reductant insertion assembly 114 and configured to remove contaminants and/or facilitate delivery of the reductant to the reductant injector 156.
The SCR catalyst 150 is disposed downstream of the mixer 130 and is configured to receive and treat the exhaust gas (e.g., a diesel exhaust gas) flowing through the SCR catalyst 150 in the presence of ammonia. In some embodiments, the SCR catalyst 150 may comprise a selective catalytic reduction filter (SCRF), or any other aftertreatment component configured to decompose constituents of the exhaust gas (e.g., NOx gases such as nitrous oxide, nitric oxide, nitrogen dioxide, etc.), flowing through the SCR catalyst 150 in the presence of a reductant, as described herein. Any suitable SCR catalyst 150 can be used such as, for example, platinum, palladium, rhodium, cerium, iron, manganese, copper, vanadium based catalysts (including combinations thereof). In particular embodiments, the SCR catalyst 150 includes a copper zeolite catalyst.
The SCR catalyst 150 can be disposed on a suitable substrate such as, for example, a ceramic (e.g., cordierite or silicon carbide) or metallic (e.g., kanthal) monolith core which can, for example, define a honeycomb structure. A washcoat can also be used as a carrier material for the SCR catalyst 150. Such washcoat materials can include, for example, aluminum oxide, titanium dioxide, silicon dioxide, any other suitable washcoat material, or a combination thereof. The exhaust gas can flow over and about the SCR catalyst 150 such that NOx gases included in the exhaust gas are further reduced to yield an exhaust gas which is substantially free of carbon monoxide and NOx gases. In some embodiments, an ammonia oxidation catalyst 160 may be disposed downstream of the SCR catalyst 150 and formulated to decompose any unreacted ammonia in the exhaust gas downstream of the SCR catalyst 150 (i.e., reduce ammonia slip).
Exhaust gas entering the housing 170 flows first into the upstream SCR catalyst 240. In some embodiments, the upstream SCR catalyst 240 includes a copper zeolite catalyst. A heater 208 (e.g., an electric heater) is operatively coupled to the upstream SCR catalyst 240 and is configured to heat the upstream SCR catalyst 240, for example, to an operative temperature of the SCR catalyst 240. The filter 120 is disposed downstream of the upstream SCR catalyst 240 and configured to filter particulate matter from the exhaust gas. In some embodiments, the filter 120 may include a catalyzed filter. Similar to the aftertreatment system 100, the mixer 130, the SCR catalyst 150, and the ammonia oxidation catalyst 160 are disposed downstream of the filter 120. The reductant injector 156 is disposed on the mixer 130 and configured to insert reductant into the mixer 130, as previously described herein. The combination of the upstream SCR catalyst 240 and the SCR catalyst 150 enhance NOx conversion efficiency of the aftertreatment system 200 by providing two stage NOx reduction. In some embodiments, additional NOx sensors, ammonia sensors, temperature sensor, a combination NOx and ammonia sensor, and/or any other sensors may be disposed between the upstream SCR catalyst 240 and the SCR catalyst 150. Information received from these sensors may be used to control an amount of reductant inserted by the reductant injector 156 into the exhaust gas.
Exhaust gas entering the housing 470 flows first into SCRF 422. The SCRF 422 performs the dual function of treating constituents of the exhaust gas (e.g., decompose NOx gases included in the exhaust gas), as well as filter particulate matter present in the exhaust gas. The exhaust gas then flows into the mixer 130 where reductant is inserted into the mixer 130, and then communicated to the SCR catalyst 150 for further treating the constituents of the exhaust gas. The SCRF 422 located upstream of the SCR catalyst 150 provides pretreatment of the exhaust gas (e.g., reducing NOx constituents of the exhaust gas) before the exhaust gas is communicated to the SCR catalyst 150. The combination of the SCRF 422 and the SCR catalyst 150 increase NOx conversion efficiency of the aftertreatment system 400 by providing two stage NOx reduction, while also reducing space claim by allowing removal of a filter from aftertreatment system 400. In some embodiments, additional NOx sensors, ammonia sensors, temperature sensor, a combination NOx and ammonia sensor, and/or any other sensors may be disposed between the SCRF 422 and the SCR catalyst 150. Information received from these sensors may be used to control an amount of reductant inserted by the reductant injector 156 into the exhaust gas.
An upstream reductant injector 506 is disposed upstream of the vSCR catalyst 505 and configured to insert reductant into the exhaust gas. The vSCR catalyst 505 is formulated to operate at lower temperatures and causes an increase in the temperature of the exhaust gas as it catalyzes the reduction of NOx constituents included in the exhaust gas (e.g., in an exothermic reaction). The vSCR catalyst 505 may increase a temperature of the exhaust gas to an operating temperature of the oxidation catalyst 110 such that a separate heater is not needed. Inserting the reductant upstream of the filter 120 may reduce amount of particulate matter emitted by aftertreatment system 500. A hydrocarbon injector 508 is disposed downstream of the vSCR catalyst 505 and configured to selectively insert hydrocarbons (e.g., provided by the reductant insertion assembly 114) into the exhaust gas before the exhaust gas enters the oxidation catalyst 110. In some embodiments, additional NOx sensors, ammonia sensors, temperature sensor, a combination NOx and ammonia sensor, and/or any other sensors may be disposed between the vSCR catalyst 505 and the SCR catalyst 150 (e.g. in the inlet conduit 102 downstream of the vSCR 505). Information received from these sensors may be used to control an amount of reductant inserted by the reductant injector 156 into the exhaust gas.
A first aftertreatment leg 710′ extends from the first internal volume 772 to the second internal volume 774, for example, in a direction parallel to a minor axis of the housing 770. For example, the first aftertreatment leg 710′ may extend along a shortest dimension of the housing 770. Corresponding openings may be defined in the plate 773 to allow the first aftertreatment leg 710′ from the first internal volume 772 to the second internal volume 774. Additional plates may also be disposed parallel the plate 773, and may serve as brackets to support the first aftertreatment leg 710′, the second aftertreatment leg 750′, and the decomposition tube 780.
The first aftertreatment leg 710′ includes an oxidation catalyst 710 extending along a first axis AL1 that may be parallel to the minor axis of the housing 770. The oxidation catalyst 710 is configured to receive at least a portion of the exhaust gas via an inlet conduit 702 fluidly coupled to the oxidation catalyst 710. The oxidation catalyst 710 may have a diameter in a range of 300 mm to 350 mm, inclusive and a length in a range of 90 mm to 110 mm, inclusive. In some embodiments, the inlet conduit 702 comprises an inlet cone 704 that has a constantly expanding cross-section from an upstream end to a downstream end of the inlet conduit 702. The downstream end of the inlet cone 704 is coupled to the first aftertreatment leg 710′. The inlet cone 704 may serve as a diffuser to decrease a flow velocity of the exhaust gas and spread the exhaust gas flow across a face of the oxidation catalyst 710.
A filter 720 (e.g., a diesel particulate filter) is disposed downstream of the oxidation catalyst 710 and axially aligned with the oxidation catalyst 710. An outlet 722 of the filter 720 is disposed within the second internal volume 774 and is configured to emit exhaust gas into the second internal volume 774 after the exhaust gas has passed through the first aftertreatment leg 710′. As shown in
The second aftertreatment leg 750′ comprises at least one SCR catalyst disposed in at least the first internal volume and extending along a second axis that is parallel to and offset from the first axis such that an inlet of the at least one SCR catalyst is disposed in the first internal volume 772. For example, as shown in
The decomposition tube 780 extends from the second internal volume 774 to the first internal volume 772 along an axis that is parallel to and offset from the first axis AL1, the first SCR axis ASCR1 and the second SCR axis ASCR2. In the particular embodiment of
In some embodiments, the inlet 782 of decomposition tube 780 is oriented at an angle that is perpendicular to the axis of the decomposition tube 780 and located proximate to the outlet 722 of the filter 720. In some embodiments, the inlet 782 of the decomposition tube 780 includes a flat end face 783 on which the reductant injector 756 is mounted. A plurality of pores 785 are defined through a wall of the decomposition tube 780 at the inlet 782 of the decomposition tube 780 and configured to allow the exhaust gas to enter the decomposition tube 780.
The aftertreatment system 700 further comprises a SCR inlet plenum 784 disposed in the first internal volume 772 and fluidly coupled to respective inlets of each of the two SCR catalysts 750a and 750b. An outlet of the decomposition tube 780 is fluidly coupled to the SCR inlet plenum 784. The decomposition tube 780 receives exhaust gas from the second internal volume 774 and communicates the exhaust gas to the SCR inlet plenum 784 in a second direction that is substantially opposite the first direction (e.g., oriented at an angle of 180±10 degrees with respect to the first direction). The SCR inlet plenum 784 is configured to redirect exhaust gas flowing therein towards respective inlets of each of the two SCR catalysts 750a and 750b such that the exhaust gas flows in a third direction through the second aftertreatment leg 750′. The third direction is substantially opposite the second direction, i.e., in the same direction as the first direction. An SCR outlet plenum 786 is disposed in the second internal volume 774 and coupled to respective outlets of each of the two SCR catalysts 750a and 750b. The SCR outlet plenum 786 defines an outlet conduit 788 that extends through a sidewall of the housing 770, and emits treated exhaust gas into the environment.
A first aftertreatment leg 810′ extends from the first internal volume 872 to the second internal volume 874 in a direction parallel to a minor axis of the housing 870. For example, the first aftertreatment leg 810′ may extend along a shortest dimension of the housing 870. Corresponding openings may be defined in the plate 873 to allow the first aftertreatment leg 810′ to extend from the first internal volume 872 to the second internal volume 874. Additional plates may also be disposed parallel the plate 873, and may serve as brackets to support the first aftertreatment leg 810′, the second aftertreatment leg 850′, and the decomposition tube 880.
The first aftertreatment leg 810′ includes an oxidation catalyst 810 extending along a first axis AL1 that may be parallel to the minor axis of the housing 870. The oxidation catalyst 810 is configured to receive at least a portion of the exhaust gas via an inlet conduit 802 fluidly coupled to the oxidation catalyst 810. The oxidation catalyst 810 may have a diameter in a range of 300 mm to 350 mm, inclusive, and a length in a range of 90 mm to 110 mm, inclusive. In some embodiments, the inlet conduit 802 comprises an inlet cone 804 that has a constantly expanding cross-section from an upstream end to a downstream end of the inlet conduit 802, as described with respect to the inlet conduit 702.
A filter 820 (e.g., a diesel particulate filter) is disposed downstream of the oxidation catalyst 810 and axially aligned with the oxidation catalyst 810. An outlet 822 of the filter 820 is disposed within the second internal volume 874 and is configured to emit exhaust gas into the second internal volume 874 after passing through the first aftertreatment leg 810′. The outlet 822 of the filter 820 includes a plurality of circumferential slits defined in a housing of the filter 820 at an end thereof that is located in the second internal volume 874. Exhaust gas flows in a first direction through the first aftertreatment leg 810′ and is released into the second internal volume 874. The filter 820 may have a diameter in range of 300 mm to 350 mm, inclusive and a length in a range of 150 mm to 200 mm, inclusive.
The second aftertreatment leg 850′ comprises three SCR catalysts 850a, 850b, and 850c. A first SCR catalyst 850a of the three SCR catalysts 850a, 850b, 850c is parallel to a second SCR catalyst 850b of the three SCR catalysts 850a, 850b, 850c. Moreover, a third SCR catalyst 850c of the three SCR catalysts 850a, 850b, 850c is disposed parallel to the second SCR catalyst 850b. The first SCR catalyst 850a extends along a first SCR axis ASCR1, the second SCR catalyst 850b extends along a second SCR axis ASCR2, and the third SCR catalyst 850c extends along a third SCR axis ASCR3, each of which is parallel to the first axis AL1. Each of the three SCR catalysts may have a diameter in a range of 200 mm to 250 mm, inclusive and a length in a range of 200 mm to 230 mm, inclusive.
The decomposition tube 880 extends from the second internal volume 874 to the first internal volume 872 along an axis that is parallel to and offset from each of the first axis AL1, the first SCR axis ASCR1, the second SCR axis ASCR2, and the third SCR axis ASCR3. As shown in
In some embodiments, the inlet 882 of decomposition tube 880 is oriented at an angle that is perpendicular to the axis of the decomposition tube 880 and located proximate to the outlet 822 of the filter 820. The inlet 882 of the decomposition tube 880 includes a flat end face 883 on which the reductant injector 856 is mounted. A plurality of pores 885 are defined through a wall of the decomposition tube 880 at the inlet 882 of the decomposition tube 880 and configured to allow the exhaust gas to enter the decomposition tube 880. The decomposition tube 880 is disposed proximate to a central portion of the housing 870 such that the decomposition tube 880 is surrounded by the three SCR catalysts 850a/b/c and the first aftertreatment leg 810′.
The aftertreatment system 800 further comprises a SCR inlet plenum 884 disposed in the first internal volume 872 and fluidly coupled to respective inlets of each of the first SCR catalyst 850a, the second SCR catalyst 850b, and the third SCR catalyst 850c. An outlet of the decomposition tube 880 is fluidly coupled to the SCR inlet plenum 884. The decomposition tube 880 receives exhaust gas from the second internal volume 874 and communicates the exhaust gas to the SCR inlet plenum 884 in a second direction that is substantially opposite the first direction. The SCR inlet plenum 884 is configured to redirect exhaust gas flowing therein towards respective inlets of each of the three SCR catalysts 850a, 850b and 850c such that the exhaust gas flows in a third direction through the second aftertreatment leg 850′. The third direction is opposite the second direction, i.e., in the same direction as the first direction.
An SCR outlet plenum 886 is disposed in the second internal volume 874 and coupled to respective outlets of each of the first, second and third SCR catalysts 850a, 850b, and 850c. The SCR outlet plenum 886 defines an outlet 889 that is fluidly coupled to the first internal volume 872 and is configured to release treated exhaust gas into the first internal volume 872. An outlet conduit 888 is coupled to a sidewall of the housing 870 forming the first internal volume 872 and is configured to expel the treated exhaust gas that is communicated into the first internal volume 872 via the SCR outlet plenum 886, into the environment. A groove 891 is defined in a sidewall of the SCR outlet plenum 886 that is perpendicular to the axes ASCR1, ASCR2, and ASCR3 of the first, second, and third SCR catalysts 850a, 850b, 850c, respectively. A portion of the inlet 882 of the decomposition tube 880 is disposed in the groove 891.
The first aftertreatment leg 910′ extends from the first internal volume 972 to the second internal volume 974 in a direction parallel to a minor axis of the housing 970. For example, the first aftertreatment leg 910′ may extend along a shortest dimension of the housing 970. Corresponding openings may be defined in the plate 973 to allow the first aftertreatment leg 910′ to extend from the first internal volume 972 to the second internal volume 974. Additional plates may also be disposed parallel to the plate 973, and may serve as brackets to support the first aftertreatment leg 910′, the second aftertreatment leg 950′, and the decomposition tube 980.
The first aftertreatment leg 910′ includes an oxidation catalyst 910 extending along a first axis AL1 that may be parallel to the minor axis of the housing 970. The oxidation catalyst 910 is configured to receive at least a portion of the exhaust gas via an inlet conduit 902 fluidly coupled to the oxidation catalyst 910. The oxidation catalyst 910 may have a diameter in a range of 300 mm to 350 mm, inclusive and a length in a range of 150 mm to 200 mm, inclusive. In some embodiments, the inlet conduit 902 comprises an inlet cone 904 that has a constantly expanding cross-section from an upstream end to a downstream end of the inlet conduit 902, as described with respect to the inlet conduit 702, 802.
A filter 920 (e.g., a diesel particulate filter) is disposed downstream of the oxidation catalyst 910 and axially aligned with the oxidation catalyst 910. An outlet 922 of the filter 920 is disposed within the second internal volume 974 and is configured to emit exhaust gas into the second internal volume 974 after passing through the first aftertreatment leg 910′. The outlet 922 of the filter 920 includes a plurality of circumferential slits defined in a housing of the filter 920 at an end thereof that is located in the second internal volume 974. Exhaust gas flows in a first direction through the first aftertreatment leg 910′ and is released into the second internal volume 974. The filter 920 may have a diameter in range of 300 mm to 350 mm, inclusive and a length in a range of 150 mm to 200 mm, inclusive.
The second aftertreatment leg 950′ comprises two SCR catalysts, a first SCR catalyst 950a and the second SCR catalyst 950b that are disposed parallel to and offset from each other as well as the first axis AL1. A first linear distance d1 from the first axis AL1 to a first SCR axis ASCR1 of the first SCR catalyst 950a is substantially equal to a second linear distance d2 from the first axis AL1 to a second SCR axis ASCR2 of the second SCR catalyst 950b. Each of the first SCR catalyst 950a and the second SCR catalyst 950b may have a diameter in a range of 250 mm to 300 mm, inclusive and a length in range of 220 mm to 260 mm, inclusive.
The decomposition tube 980 extends from the second internal volume 974 to the first internal volume 972 along an axis that is parallel to and offset from each of the first axis AL1, the first SCR axis ASCR1, and the second SCR axis ASCR2. As shown in
An inlet 982 of the decomposition tube 980 is disposed in the second internal volume 974 such that the decomposition tube 980 is configured to receive the exhaust gas emitted into the second internal volume 974, and communicate the exhaust gas from the second internal volume 974 to the inlet of the SCR catalysts 950a and 950b in the first internal volume. In some embodiments, the inlet 982 of decomposition tube 980 is oriented at an angle that is perpendicular to the axis of the decomposition tube 980 such that the decomposition tube 980 forms an elbow tube. The inlet 982 is located proximate to the outlet 922 of the filter 920. A reductant injection inlet is defined proximate to the inlet 982 of the decomposition tube 980 and configured to allow reductant to be injected into the decomposition tube 982. A reductant injector 956 is mounted on the decomposition tube 980 proximate to the inlet 982 of the decomposition tube 980 and configured to insert a reductant into the decomposition tube 980 via the reductant injection inlet. For example, the reductant injector 956 may be mounted on a bend defined in the decomposition tube 980 downstream of the inlet 982.
The aftertreatment system 900 further comprises a SCR inlet plenum 984 disposed in the first internal volume 972 and fluidly coupled to respective inlets of each of the first SCR catalyst 950a, and the second SCR catalyst 950b. An outlet of the decomposition tube 980 is fluidly coupled to the SCR inlet plenum 984. The decomposition tube 980 receives exhaust gas from the second internal volume 974 and communicates the exhaust gas to the SCR inlet plenum 984 in a second direction that is substantially opposite the first direction. The SCR inlet plenum 984 is configured to redirect exhaust gas flowing therein towards respective inlets of each of the two SCR catalysts 950a and 950b such that the exhaust gas flows in a third direction through the second aftertreatment leg 950′. The third direction is opposite the second direction, i.e., in the same direction as the first direction.
An SCR outlet plenum 986 is disposed in the second internal volume 974 and coupled to respective outlets of each of the SCR catalysts 950a and 950b. The SCR outlet plenum 985 defines an outlet 989 that is fluidly coupled to the first internal volume 972 and configured to release treated exhaust gas into the first internal volume 972. An outlet conduit 988 is coupled to a sidewall of the housing 970 forming the first internal volume 972 and is configured to expel the treated exhaust gas that is communicated into the first internal volume 972 via the SCR outlet plenum 986, into the environment. A groove 991 is defined in a sidewall of the SCR outlet plenum 986 that is perpendicular to the first and second SCR axes ASCR1 and ASCR2 of the two SCR catalysts 950a and 950b, respectively. A portion of the inlet 982 of the decomposition tube 980 is disposed in the groove 991.
The first aftertreatment leg 1110′ extends from the first internal volume 1172 to the second internal volume 1174 in a direction parallel to a minor axis of the housing 1170. For example, the first aftertreatment leg 1110′ may extend along a shortest dimension of the housing 1170. Corresponding openings may be defined in the plate 1173 to allow the first aftertreatment leg 1110′ to extend from the first internal volume 1172 to the second internal volume 1174. Additional plates may also be disposed parallel to the plate 1173, and may serve as brackets to support the first aftertreatment leg 1110′, the second aftertreatment leg 1150′, and the decomposition tube 1180.
The first aftertreatment leg 1110′ extends from the first internal volume to the second internal volume and includes a first segment extending along a first axis AL1 that is parallel to a minor axis of the housing 1170 and a second segment that extends along a second axis AL2 that is parallel to the first axis AL1. The first segment includes a first oxidation catalyst 1110a and a first filter 1120a disposed downstream of the first oxidation catalyst 1110a and axially aligned with the first oxidation catalyst 1110a. An outlet of the first filter 1120a is disposed in the second internal volume. The second segment includes a second oxidation catalyst 1110b disposed parallel to the first oxidation catalyst 1110a and horizontally aligned with the first oxidation catalyst 1110a. A second filter 1120b is disposed downstream of the second oxidation catalyst 1110b and axially aligned with second oxidation catalyst 1110b. Each of the first oxidation catalyst 1110a and the second oxidation catalyst 1110b may have a diameter in a range of 240 mm to 280 mm, inclusive and a length in range of 70 mm to 120 mm, inclusive. Moreover, each of the first filter 1120a and the second filter 1120b may have a diameter in a range of 240 mm to 280 mm, inclusive, and a length in a range of 110 mm to 150 mm, inclusive.
A first aftertreatment leg inlet plenum 1106 is disposed in the first internal volume 1172. The first aftertreatment leg inlet plenum 1106 is coupled to an inlet of each of the first oxidation catalyst 1110a and the second oxidation catalyst 1110b, and to an inlet conduit 1102. The first aftertreatment leg inlet plenum 1106 is configured to communicate a first portion of the exhaust gas to the first oxidation catalyst 1110a and a second portion of the exhaust gas to the second oxidation catalyst 1110b. In some embodiments, the inlet conduit 1102 comprises an inlet cone 1104 that has a constantly expanding cross-section from an upstream end to a downstream end of the inlet conduit 1102, as described with respect to the inlet conduit 702, 802, 902.
The first filter 1120a is configured to emit the first portion of the exhaust gas via a first filter outlet 1122a and the second filter 1120b is configured to emit the second portion of the exhaust gas via a second filter outlet 1122b into the second internal volume, respectively. Each of the first filter outlet 1122a and second filter outlet 1122b include a plurality of circumferential slits defined in respective housings of the filters 1120a and 1120b at respective ends thereof that is located in the second internal volume 1174. Exhaust gas flows in a first direction through the first aftertreatment leg 1110′ and is released into the second internal volume 1174.
The second aftertreatment leg 1150′ includes two SCR catalyst, a first SCR catalyst 1150a extending along a first SCR axis ASCR1 and a second SCR catalyst 1150b extending along a second SCR axis ASCR2. The first SCR catalyst 1150a and the second SCR catalyst 1150b are disposed parallel to each other and are horizontally aligned with each other. In some embodiments, the first SCR catalyst 1150a is disposed parallel to and vertically aligned with the first oxidation catalyst 1110a. Moreover the second SCR catalyst 1150b is disposed parallel to and vertically aligned with the second oxidation catalyst 1110b. Each of the SCR catalysts 1150a and 1150b may have a diameter in a range of 240 mm to 280 mm, inclusive, and a length in a range of 220 mm to 260 mm, inclusive.
A decomposition tube 1180 is disposed within the housing 1170 from the second internal volume 1174 to the first internal volume 1172 and extends along an axis that is parallel to and offset from each of the first axis AL1, the second axis AL2, the first SCR axis ASCR1, and the second SCR axis ASCR2. An inlet of the decomposition tube 1180 is disposed in the second internal volume 1174 and configured to receive each of the first portion and the second portion of the exhaust gas from the second internal volume, and communicate the exhaust gas from the second internal volume 1174 to inlets of the SCR catalysts 1150a and 1150b in the first internal volume. An inlet of the decomposition tube 1180 may be located proximate to the outlets 1022a and 1022b of the filters 1020a and 1020b, respectively. A reductant injection inlet is defined proximate to the inlet 1182 of the decomposition tube 1180 and configured to allow reductant to be injected into the decomposition tube 1180. A reductant injector 1156 is mounted on the decomposition tube 1180 proximate to the inlet of the decomposition tube 1180 and configured to insert a reductant into the decomposition tube 1180 via the reductant injection inlet. As shown in
The aftertreatment system 1100 further comprises a SCR inlet plenum 1184 disposed in the first internal volume 1172 and fluidly coupled to respective inlets of each of the first SCR catalysts 1150a, and the second SCR catalyst 1150b. The SCR inlet plenum 1184 is configured to redirect exhaust gas flowing therein towards respective inlets of each of the two SCR catalysts 1150a and 1150b. An outlet of the decomposition tube 1180 is fluidly coupled to the SCR inlet plenum 1184. The decomposition tube 1180 receives exhaust gas from the second internal volume 1174 and communicates the exhaust gas to the SCR inlet plenum 1184 in a second direction that is substantially opposite the first direction. The SCR inlet plenum 1184 is configured to redirect exhaust gas flowing therein towards respective inlets of each of the two SCR catalysts 1150a and 1150b such that the exhaust gas flows in a third direction through the second aftertreatment leg 1150′. The third direction is opposite the second direction, i.e., in the same direction as the first direction.
An SCR outlet plenum 1186 is disposed in the second internal volume 1174 and coupled to respective outlets of each of the SCR catalysts 1150a and 1150b. The SCR outlet plenum 1186 may define an outlet that is fluidly coupled to the first internal volume 1172 and configured to release treated exhaust gas into the first internal volume 1172. An outlet conduit 1188 is coupled to a sidewall of the housing 1170 forming the first internal volume 1172 and is configured to expel the treated exhaust gas that is communicated into the first internal volume 1172 via the SCR outlet plenum 1186, into the environment.
The first aftertreatment leg 1210′ extends from the first internal volume 1272 to the second internal volume 1274 in a direction parallel to a minor axis of the housing 1270. For example, the first aftertreatment leg 1210′ may extend along a shortest dimension of the housing 1270. Corresponding openings may be defined in the plate 1273 to allow the first aftertreatment leg 1210′ to extend from the first internal volume 1272 to the second internal volume 1274. Additional plates may also be disposed parallel to the plate 1273, and may serve as brackets to support the first aftertreatment leg 1210′, the second aftertreatment leg 1220′, the third aftertreatment leg 1250′ and the decomposition tube 1280.
As shown in
An oxidation catalyst 1210 is disposed downstream of the temperature control aftertreatment component 1209 and axially aligned with the temperature control aftertreatment component 1209. In some embodiments, a hydrocarbon injector 1218 is disposed on the first aftertreatment leg 1210′ between the temperature control aftertreatment component 1209 and the oxidation catalyst 1210. The hydrocarbon injector 1218 is mounted on a hydrocarbon injection inlet 1207 (
In some embodiments, the temperature control aftertreatment component 1209 may include a vSCR catalyst. The vSCR catalyst may be configured to catalyze decomposition of constituents of the exhaust gas (e.g., NOx gases) in the presence of a reductant in an exothermic reaction, which increases a temperature of the exhaust gas. This may be beneficial during cold start operation of the aftertreatment system 1200 because the temperature of the exhaust gas may increase after passing through the vSCR thereby, causing a temperature of the downstream oxidation catalyst 1210 and SCR catalysts 1250a and 1250b to increase. In such embodiments, a mixing tube 1201 may be disposed upstream of the inlet conduit 1202. A first reductant injector 1206 may be disposed on the mixing tube 1201, for example, at an end thereof that is opposite to an end which is coupled to the inlet conduit 1202, and configured to insert a reductant into the exhaust gas. The mixing tube 1201 may have a sufficient length or include internal structures (e.g., baffle plates, veins, blades, etc.) to facilitate mixing of the reductant with the exhaust gas. In other embodiments, the temperature control aftertreatment component 1209 may include a heater (e.g., a 10 kW electric heater) configured to selectively heat the exhaust gas flowing into the oxidation catalyst 1210. In such embodiments, the mixing tube 1201 and the first reductant injector 1206 may be excluded.
A second aftertreatment leg 1220′ extends from the second internal volume 1274 to the first internal volume 1272 parallel to the first aftertreatment leg 1210′ and horizontally aligned with the first aftertreatment leg 1210′. The second aftertreatment leg includes a filter 1220 disposed parallel to the oxidation catalyst 1210 and extending along a second axis AL2 that is parallel to and offset from the first axis AL1. The filter 1220 is configured to receive exhaust gas from the oxidation catalyst 1210 through the second internal volume 1274. An outlet of the filter 1220 is disposed within the first internal volume 1272 and configured to emit exhaust gas into the first internal volume 1272 after passing through the filter 1220. The filter may have a diameter in a range of 250 mm to 300 mm, inclusive and a length in a range of 220 mm to 280 mm, inclusive. The aftertreatment system 1200 includes a transition plenum 1208 fluidly coupling the outlet of the oxidation catalyst 1210 to an inlet of the filter 1220. The exhaust gas flows through the first aftertreatment leg 1210′ in a first direction, and then through the second aftertreatment leg 1220′ in a second direction that is opposite the first direction.
The third aftertreatment leg 1250′ includes two SCR catalyst, a first SCR catalyst 1250a extending along a first SCR axis ASCR1 and a second SCR catalyst 1250b extending along a second SCR axis ASCR2. The first SCR catalyst 1250a and the second SCR catalyst 1250b are disposed parallel to offset from each other. In some embodiments, the first SCR catalyst 1250a is disposed parallel to the first aftertreatment leg 1210′. Moreover the second catalyst 1250b is disposed parallel to the second aftertreatment leg 1220′. Each of the SCR catalysts 1250a and 1250b may have a diameter in a range of 250 mm to 300 mm, inclusive and a length in a range of 220 mm to 260 mm, inclusive.
A decomposition tube 1280 is disposed within the housing 1270 and extends from the first internal volume 1272 to the second internal volume 1274 along an axis that is parallel to and offset from each of the first axis AL1, the second axis AL2, the first SCR axis ASCR1, and the second SCR axis ASCR2. As shown in
The aftertreatment system 1200 further comprises a SCR inlet plenum 1284 disposed in the second internal volume 1274 and fluidly coupled to respective inlets of each of the first SCR catalysts 1250a, and the second SCR catalyst 1250b. The SCR inlet plenum 1284 is configured to redirect exhaust gas flowing therein towards respective inlets of each of the two SCR catalysts 1250a and 1250b. An outlet of the decomposition tube 1280 is fluidly coupled to the SCR inlet plenum 1284. The decomposition tube 1280 receives exhaust gas from the second internal volume 1274 and communicates the exhaust gas to the SCR inlet plenum 1284 in a third direction that is substantially opposite the second direction but in the same direction as the first direction. The SCR inlet plenum 1284 is configured to redirect exhaust gas flowing therein towards respective inlets of each of the first and second SCR catalysts 1250a and 1250b such that the exhaust gas flows in a fourth direction through the third aftertreatment leg 1250′. The fourth direction is opposite the third and the first direction, i.e., in the same direction as the second direction.
An SCR outlet plenum 1286 is disposed in the first internal volume 1272 and coupled to respective outlets of each of the SCR catalysts 1250a and 1250b. The SCR outlet plenum 1286 may define an outlet that is configured to emit exhaust gas into the second internal volume 1274. An outlet conduit 1288 is coupled to a sidewall of the housing 1270 forming the second internal volume 1274 and configured to expel the treated exhaust gas, that is communicated into the second internal volume 1274 via the SCR outlet plenum 1286, into the environment.
It should be noted that the term “example” as used herein to describe various embodiments is intended to indicate that such embodiments are possible examples, representations, and/or illustrations of possible embodiments (and such term is not intended to connote that such embodiments are necessarily extraordinary or superlative examples).
The terms “coupled,” and the like as used herein mean the joining of two members directly or indirectly to one another. Such joining may be stationary (e.g., permanent) or moveable (e.g., removable or releasable). Such joining may be achieved with the two members or the two members and any additional intermediate members being integrally formed as a single unitary body with one another or with the two members or the two members and any additional intermediate members being attached to one another.
As used herein, the term “about” generally mean plus or minus 10% of the stated value. For example, about 0.5 would include 0.45 and 0.55, about 10 would include 9 to 11, about 1000 would include 900 to 1100.
It is important to note that the construction and arrangement of the various exemplary embodiments are illustrative only. Although only a few embodiments have been described in detail in this disclosure, those skilled in the art who review this disclosure will readily appreciate that many modifications are possible (e.g., variations in sizes, dimensions, structures, shapes and proportions of the various elements, values of parameters, mounting arrangements, use of materials, colors, orientations, etc.) without materially departing from the novel teachings and advantages of the subject matter described herein. Additionally, it should be understood that features from one embodiment disclosed herein may be combined with features of other embodiments disclosed herein as one of ordinary skill in the art would understand. Other substitutions, modifications, changes and omissions may also be made in the design, operating conditions and arrangement of the various exemplary embodiments without departing from the scope of the present invention.
While this specification contains many specific implementation details, these should not be construed as limitations on the scope of any inventions or of what may be claimed, but rather as descriptions of features specific to particular implementations of particular inventions. Certain features described in this specification in the context of separate implementations can also be implemented in combination in a single implementation. Conversely, various features described in the context of a single implementation can also be implemented in multiple implementations separately or in any suitable subcombination. Moreover, although features may be described above as acting in certain combinations and even initially claimed as such, one or more features from a claimed combination can in some cases be excised from the combination, and the claimed combination may be directed to a subcombination or variation of a subcombination.
The present application is a national stage of PCT Application No. PCT/US2021/029282, filed Apr. 27, 2021, which claims the benefit of U.S. Provisional Application No. 63/022,057, filed May 8, 2020. The contents of these applications are incorporated herein by reference in their entireties.
| Filing Document | Filing Date | Country | Kind |
|---|---|---|---|
| PCT/US2021/029282 | 4/27/2021 | WO |
| Publishing Document | Publishing Date | Country | Kind |
|---|---|---|---|
| WO2021/225824 | 11/11/2021 | WO | A |
| Number | Name | Date | Kind |
|---|---|---|---|
| 1104963 | Coanda | Jul 1914 | A |
| 4424777 | Klomp | Jan 1984 | A |
| 7581387 | Bui et al. | Sep 2009 | B2 |
| 7793490 | Amon et al. | Sep 2010 | B2 |
| 8033101 | Amon et al. | Oct 2011 | B2 |
| 8230678 | Aneja et al. | Jul 2012 | B2 |
| 8375708 | Forster et al. | Feb 2013 | B2 |
| 8460610 | Silver et al. | Jun 2013 | B2 |
| 8607555 | Kaiser et al. | Dec 2013 | B2 |
| 8615984 | Kornherr et al. | Dec 2013 | B2 |
| 8789363 | Iverson et al. | Jul 2014 | B2 |
| 9021794 | Goss et al. | May 2015 | B2 |
| 9133744 | Birkby et al. | Sep 2015 | B2 |
| 9248404 | Brunel et al. | Feb 2016 | B2 |
| 9266075 | Chapman et al. | Feb 2016 | B2 |
| 9267417 | Baldwin et al. | Feb 2016 | B2 |
| 9328640 | Iverson et al. | May 2016 | B2 |
| 9346017 | Greber | May 2016 | B2 |
| 9352276 | Sampath | May 2016 | B2 |
| 9453444 | Fischer et al. | Sep 2016 | B2 |
| 9464546 | Perrot et al. | Oct 2016 | B2 |
| 9581067 | Guilbaud et al. | Feb 2017 | B2 |
| 9605573 | Solbrig et al. | Mar 2017 | B2 |
| 9664081 | Rusch et al. | May 2017 | B2 |
| 9714598 | Alano et al. | Jul 2017 | B2 |
| 9726064 | Alano | Aug 2017 | B2 |
| 9737908 | Hornback et al. | Aug 2017 | B2 |
| 9995193 | Alano et al. | Jun 2018 | B2 |
| 10024217 | Johnson et al. | Jul 2018 | B1 |
| 10030564 | Cossard et al. | Jul 2018 | B2 |
| 10174658 | Dimpelfeld et al. | Jan 2019 | B2 |
| 10190465 | Alano et al. | Jan 2019 | B2 |
| 10215075 | Chapman et al. | Feb 2019 | B2 |
| 10247081 | Niaz | Apr 2019 | B2 |
| 10273853 | Golin | Apr 2019 | B2 |
| 10287948 | Moulieres et al. | May 2019 | B1 |
| 10287954 | Chapman et al. | May 2019 | B2 |
| 10294843 | Alano et al. | May 2019 | B2 |
| 10316721 | Moulieres et al. | Jun 2019 | B1 |
| 10337379 | Dimpelfeld et al. | Jul 2019 | B2 |
| 10337380 | Willats et al. | Jul 2019 | B2 |
| 10422268 | Niaz | Sep 2019 | B2 |
| 10533478 | Alano | Jan 2020 | B2 |
| 10577995 | Ker et al. | Mar 2020 | B2 |
| 10612443 | Li et al. | Apr 2020 | B2 |
| 10731536 | Chenoweth et al. | Aug 2020 | B1 |
| 10787946 | Rohde et al. | Sep 2020 | B2 |
| 10808587 | Ottaviani et al. | Oct 2020 | B2 |
| 10823032 | Willats et al. | Nov 2020 | B2 |
| 10907522 | Poinsot et al. | Feb 2021 | B2 |
| 10914218 | Chapman et al. | Feb 2021 | B1 |
| 10920635 | Kozakiewicz | Feb 2021 | B2 |
| 10920642 | Wang et al. | Feb 2021 | B2 |
| 10933387 | Cvelbar | Mar 2021 | B2 |
| 10967329 | Alano et al. | Apr 2021 | B2 |
| 11085346 | Tucker et al. | Aug 2021 | B2 |
| 11105241 | Tucker et al. | Aug 2021 | B2 |
| 11193412 | Cvelbar et al. | Dec 2021 | B2 |
| 11230958 | Tucker et al. | Jan 2022 | B2 |
| 11242788 | Kinnaird | Feb 2022 | B2 |
| 11242790 | Chapman et al. | Feb 2022 | B2 |
| 11300028 | Meunier | Apr 2022 | B2 |
| 11313266 | Tucker et al. | Apr 2022 | B2 |
| 11428140 | Kinnaird et al. | Aug 2022 | B1 |
| 11459927 | Rajashekharaiah et al. | Oct 2022 | B2 |
| 11459929 | Dimpelfeld et al. | Oct 2022 | B2 |
| 11506101 | Levato | Nov 2022 | B2 |
| 11591943 | Hornback | Feb 2023 | B2 |
| 20040112883 | Bowden et al. | Jun 2004 | A1 |
| 20040237511 | Ripper et al. | Dec 2004 | A1 |
| 20050172615 | Mahr | Aug 2005 | A1 |
| 20050262843 | Monty | Dec 2005 | A1 |
| 20060150614 | Cummings | Jul 2006 | A1 |
| 20060153748 | Huthwohl et al. | Jul 2006 | A1 |
| 20060191254 | Bui et al. | Aug 2006 | A1 |
| 20060260104 | Himi | Nov 2006 | A1 |
| 20060283181 | Crawley et al. | Dec 2006 | A1 |
| 20070144126 | Ohya et al. | Jun 2007 | A1 |
| 20070163241 | Meingast et al. | Jul 2007 | A1 |
| 20070245718 | Cheng et al. | Oct 2007 | A1 |
| 20070283683 | Bellinger | Dec 2007 | A1 |
| 20080087013 | Crawley et al. | Apr 2008 | A1 |
| 20080121179 | Park et al. | May 2008 | A1 |
| 20080127635 | Hirata et al. | Jun 2008 | A1 |
| 20080314033 | Aneja et al. | Dec 2008 | A1 |
| 20090000283 | Endicott et al. | Jan 2009 | A1 |
| 20090019843 | Levin et al. | Jan 2009 | A1 |
| 20090031717 | Blaisdell | Feb 2009 | A1 |
| 20090049829 | Kaiser et al. | Feb 2009 | A1 |
| 20090084094 | Goss et al. | Apr 2009 | A1 |
| 20090145119 | Farrell et al. | Jun 2009 | A1 |
| 20090158717 | Kimura et al. | Jun 2009 | A1 |
| 20090158722 | Kojima et al. | Jun 2009 | A1 |
| 20090180937 | Nohl et al. | Jul 2009 | A1 |
| 20090229254 | Gibson | Sep 2009 | A1 |
| 20100083641 | Makartchouk et al. | Apr 2010 | A1 |
| 20100146942 | Mayr et al. | Jun 2010 | A1 |
| 20100146948 | Dacosta et al. | Jun 2010 | A1 |
| 20100187383 | Olsen et al. | Jul 2010 | A1 |
| 20100251719 | Mancini et al. | Oct 2010 | A1 |
| 20100319329 | Khadiya | Dec 2010 | A1 |
| 20110005232 | Williams et al. | Jan 2011 | A1 |
| 20110079003 | Sun et al. | Apr 2011 | A1 |
| 20110094206 | Liu et al. | Apr 2011 | A1 |
| 20110099978 | Davidson et al. | May 2011 | A1 |
| 20110146237 | Adelmann et al. | Jun 2011 | A1 |
| 20110194987 | Hodgson et al. | Aug 2011 | A1 |
| 20120003955 | Gabriel | Jan 2012 | A1 |
| 20120124983 | Hong | May 2012 | A1 |
| 20120204541 | Li et al. | Aug 2012 | A1 |
| 20120204542 | Norris et al. | Aug 2012 | A1 |
| 20120204544 | Uhrich et al. | Aug 2012 | A1 |
| 20120216513 | Greber et al. | Aug 2012 | A1 |
| 20130067891 | Hittle et al. | Mar 2013 | A1 |
| 20130097819 | Kojima | Apr 2013 | A1 |
| 20130333363 | Joshi et al. | Dec 2013 | A1 |
| 20140033686 | Fischer et al. | Feb 2014 | A1 |
| 20140230418 | Perrot et al. | Aug 2014 | A1 |
| 20140260209 | Goss et al. | Sep 2014 | A1 |
| 20140325967 | Kimura | Nov 2014 | A1 |
| 20150016214 | Mueller | Jan 2015 | A1 |
| 20150089923 | Henderson et al. | Apr 2015 | A1 |
| 20150110681 | Ferront et al. | Apr 2015 | A1 |
| 20150121855 | Munnannur et al. | May 2015 | A1 |
| 20150218996 | Brandl et al. | Aug 2015 | A1 |
| 20150360176 | Bui et al. | Dec 2015 | A1 |
| 20160061090 | Anand | Mar 2016 | A1 |
| 20160083060 | Kassianoff | Mar 2016 | A1 |
| 20160090887 | Mitchell et al. | Mar 2016 | A1 |
| 20160115847 | Chapman et al. | Apr 2016 | A1 |
| 20160138454 | Alano et al. | May 2016 | A1 |
| 20160158714 | Li et al. | Jun 2016 | A1 |
| 20160175784 | Harmon et al. | Jun 2016 | A1 |
| 20160194991 | Clayton, Jr | Jul 2016 | A1 |
| 20160243510 | Denton et al. | Aug 2016 | A1 |
| 20160251990 | Dimpelfeld et al. | Sep 2016 | A1 |
| 20160332126 | Nande et al. | Nov 2016 | A1 |
| 20160361694 | Brandl et al. | Dec 2016 | A1 |
| 20170067387 | Khaled | Mar 2017 | A1 |
| 20170107882 | Chiruta et al. | Apr 2017 | A1 |
| 20170152778 | Li et al. | Jun 2017 | A1 |
| 20170361273 | Zoran | Dec 2017 | A1 |
| 20170370262 | Zoran et al. | Dec 2017 | A1 |
| 20180078912 | Yadav et al. | Mar 2018 | A1 |
| 20180087428 | Barr | Mar 2018 | A1 |
| 20180142604 | Niaz | May 2018 | A1 |
| 20180266300 | Liu | Sep 2018 | A1 |
| 20180306083 | Sampath et al. | Oct 2018 | A1 |
| 20180313247 | Bauknecht et al. | Nov 2018 | A1 |
| 20190063294 | Johnson et al. | Feb 2019 | A1 |
| 20200102873 | Ramolivo et al. | Apr 2020 | A1 |
| 20200123955 | Liu et al. | Apr 2020 | A1 |
| 20200332696 | Chapman | Oct 2020 | A1 |
| 20210039056 | De Rudder et al. | Feb 2021 | A1 |
| 20210095587 | Cvelbar et al. | Apr 2021 | A1 |
| 20210301704 | Hornback | Sep 2021 | A1 |
| 20210301710 | Cvelbar et al. | Sep 2021 | A1 |
| 20210363907 | Poinsot et al. | Nov 2021 | A1 |
| 20210404367 | Alano et al. | Dec 2021 | A1 |
| 20220065148 | Sudries et al. | Mar 2022 | A1 |
| 20220162975 | Cvelbar et al. | May 2022 | A1 |
| 20220162976 | Alano et al. | May 2022 | A1 |
| 20220184567 | Geant | Jun 2022 | A1 |
| 20220349330 | Chapman et al. | Nov 2022 | A1 |
| 20220379272 | Alano | Dec 2022 | A1 |
| Number | Date | Country |
|---|---|---|
| 101815851 | Aug 2010 | CN |
| 102242662 | Nov 2011 | CN |
| 103429864-1 | Dec 2013 | CN |
| 106377919 | Feb 2017 | CN |
| 206144632 | May 2017 | CN |
| 206144633 | May 2017 | CN |
| 107435576 | Dec 2017 | CN |
| 108194176 | Jun 2018 | CN |
| 109477413 | Mar 2019 | CN |
| 208982145 | Jun 2019 | CN |
| 106014560 | Jul 2019 | CN |
| 209179849 | Jul 2019 | CN |
| 209855888 | Dec 2019 | CN |
| 110761876 | Feb 2020 | CN |
| 210195855 | Mar 2020 | CN |
| 210686097 | Jun 2020 | CN |
| 210858906 | Jun 2020 | CN |
| 211082028 | Jul 2020 | CN |
| 211116205 | Jul 2020 | CN |
| 211573625 | Sep 2020 | CN |
| 212130586 | Dec 2020 | CN |
| 212130587 | Dec 2020 | CN |
| 212296579 | Jan 2021 | CN |
| 212744129 | Mar 2021 | CN |
| 214304014 | Sep 2021 | CN |
| 214836650 | Nov 2021 | CN |
| 214887318 | Nov 2021 | CN |
| 215109110 | Dec 2021 | CN |
| 215719044 | Feb 2022 | CN |
| 215719045 | Feb 2022 | CN |
| 216157745 | Apr 2022 | CN |
| 216617626 | May 2022 | CN |
| 217872989 | Nov 2022 | CN |
| 10021166 | Nov 2001 | DE |
| 10312212 | Nov 2003 | DE |
| 10 2004 043 931 | Mar 2006 | DE |
| 10 2010 014 037 | Nov 2010 | DE |
| 11 2009 000 650 | Jan 2011 | DE |
| 11 2010 002 589 | Nov 2012 | DE |
| 10 2014 101 889 | Aug 2015 | DE |
| 10 2014 101 889 | Aug 2015 | DE |
| 10 2014 102 798 | Sep 2015 | DE |
| 10 2016 222 743 | May 2017 | DE |
| 10 2016 115 030 | Feb 2018 | DE |
| 10 2018 127 387 | May 2019 | DE |
| 10 2007 051 510 | Feb 2021 | DE |
| 0 716 918 | Jun 1996 | EP |
| 1 716 917 | Nov 2006 | EP |
| 2 769 762 | Aug 2014 | EP |
| 2 551 482 | Jan 2015 | EP |
| 2 546 488 | Apr 2015 | EP |
| 2 551 481 | Aug 2015 | EP |
| 3 085 913 | Oct 2016 | EP |
| 3 085 915 | Oct 2016 | EP |
| 3 085 916 | Oct 2016 | EP |
| 2 570 178 | Apr 2017 | EP |
| 2 522 822 | Jun 2017 | EP |
| 2 796 684 | Jan 2018 | EP |
| 3 425 180 | Jan 2019 | EP |
| 2965011 | Mar 2012 | FR |
| 3010134 | Mar 2015 | FR |
| 2984953 | Apr 2015 | FR |
| 2977913 | Jun 2015 | FR |
| 3020835 | Nov 2015 | FR |
| 3020834 | Jun 2016 | FR |
| 3020835 | Jun 2016 | FR |
| 3098854 | Jul 2021 | FR |
| 3097775 | May 2022 | FR |
| 3102683 | Jun 2022 | FR |
| 3111664 | Jul 2022 | FR |
| 3110634 | Sep 2022 | FR |
| 2 385 545 | Aug 2003 | GB |
| 201921025624 | Jan 2021 | IN |
| 2003-056274 | Feb 2003 | JP |
| 2009-156077 | Jul 2009 | JP |
| 2010-180863 | Aug 2010 | JP |
| 2013-133774 | Jul 2013 | JP |
| WO-2009024815 | Feb 2009 | WO |
| WO-2009024815 | Feb 2009 | WO |
| WO-2010146285 | Dec 2010 | WO |
| WO-2011110885 | Sep 2011 | WO |
| WO-2012110720 | Aug 2012 | WO |
| WO-2012123660 | Sep 2012 | WO |
| WO-2018017164 | Jan 2018 | WO |
| WO-2018075061 | Apr 2018 | WO |
| WO-2018226626 | Dec 2018 | WO |
| WO-2019029880 | Feb 2019 | WO |
| WO-2019143373 | Jul 2019 | WO |
| WO-2020009713 | Jan 2020 | WO |
| WO-2021050819 | Mar 2021 | WO |
| WO-2021112826 | Jun 2021 | WO |
| WO-2021113246 | Jun 2021 | WO |
| WO-2021173357 | Sep 2021 | WO |
| WO-2021225824 | Nov 2021 | WO |
| Entry |
|---|
| Final Office Action issued in U.S. Appl. No. 13/837,446 dated Jan. 5, 2015. |
| First Examination Report in IN 202247030005, dated Jul. 13, 2022. |
| First Examination Report in IN 202247032735, dated Jul. 22, 2022. |
| Office Action issued in German Patent Application No. DE 102014002750.3, dated Jan. 24, 2022, 5 pages. |
| International Search Report and Written Opinion in International Patent Application No. PCT/US2020/062718 dated Feb. 19, 2021. |
| International Search Report and Written Opinion issued in PCT Application No. PCT/US2021/056073, dated Jan. 26, 2022. |
| International Search Report and Written Opinion issued in PCT Application No. PCT/US2021/029282 dated Jul. 27, 2021. |
| Search Report and Written Opinion issued in PCT Application No. PCT/US2019/064232 dated Feb. 12, 2020. |
| U.S. Office Action issue in U.S. Appl. No. 13/837,446 dated Aug. 29, 2014. |
| International Search Report and Written Opinion dated Jul. 27, 2021 in PCT Application No. PCT/US2021/029282. |
| Coanda effect, https://en.wikipedia.org/w/index.php?title=Coand%C4%83_effect&oldid=1000333406 (last visited Mar. 12, 2021). |
| Combined Search and Examination Report in UK Patent Application No. GB2205057.9, dated May 5, 2022. |
| Examination Report in U.K. Patent Application No. 1413056.1 dated Sep. 21, 2017. |
| Examination Report in UK Patent Application No. GB 1917608.0 dated Sep. 6, 2021. |
| Final Office Action in U.S. Appl. No. 17/695,580 dated Feb. 6, 2023. |
| First Examination Report in Indian Patent Application No. 201947050068, dated Jan. 13, 2021. |
| First Examination Report in Indian Patent Application No. 202147057999. |
| First Office Action in Chinese Patent Application No. 201880001223.6, dated Dec. 17, 2020. |
| G. Comes, “Theoretical Modeling, Design and Simulation of an Innovative Diverting Valve Based on Coanda Effect”, Fluids 2018, 3, 103, (2018). |
| International Search Report & Written Opinion in PCT Application No. PCT/US2012/022582 dated Oct. 25, 2012. |
| International Search Report and Written Opinion in PCT Appplication No. PCT/IB2019/054988 dated Jan. 29, 2020, 12. |
| International Search Report and Written Opinion in PCT Application No. PCT/US2021/017551 dated Apr. 28, 2021. |
| International Search Report and Written Opinion in PCT Application No. PCT/US2022/014781 dated Apr. 25, 2022. |
| International Search Report and Written Opinion in PCT Application No. PCT/US2018/035959, dated Oct. 19, 2018. |
| Office Action on U.S. Appl. No. 15/657,941 dated Aug. 6, 2019. |
| Office Action in U.S. Appl. No. 16/618,716 dated Feb. 23, 2021. |
| Office Action in U.S. Appl. No. 17/400,567 dated May 23, 2022. |
| Office Action in U.S. Appl. No. 17/695,580 dated Jul. 27, 2022. |
| Office Action in German Patent Application No. DE 11 2012 005 741.4 dated Dec. 7, 2022. |
| Preliminary Office Action in BR1120190253246, dated Apr. 26, 2022. |
| Search and Examination Report issued in GB2116026.2 dated Dec. 20, 2021. |
| Search Report issued in UK Patent Application No. GB 2101393.3, dated Feb. 22, 2021. |
| Search Report Letter issued in UK Patent Application No. GB 2101393.3, dated Feb. 22, 2021. |
| Office Action in U.S. Appl. No. 14/372,810 dated Mar. 8, 2017. |
| Office Action in U.S. Appl. No. 14/372,810 dated May 25, 2016. |
| Number | Date | Country | |
|---|---|---|---|
| 20230123437 A1 | Apr 2023 | US |
| Number | Date | Country | |
|---|---|---|---|
| 63022057 | May 2020 | US |
