WO2010133309A1 - HIGH Pd CONTENT DIESEL OXIDATION CATALYSTS WITH IMPROVED HYDROTHERMAL DURABILITY - Google Patents

HIGH Pd CONTENT DIESEL OXIDATION CATALYSTS WITH IMPROVED HYDROTHERMAL DURABILITY Download PDF

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Publication number
WO2010133309A1
WO2010133309A1 PCT/EP2010/002904 EP2010002904W WO2010133309A1 WO 2010133309 A1 WO2010133309 A1 WO 2010133309A1 EP 2010002904 W EP2010002904 W EP 2010002904W WO 2010133309 A1 WO2010133309 A1 WO 2010133309A1
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Prior art keywords
catalyst
zeolite
optionally
substrate
overcoat
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PCT/EP2010/002904
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English (en)
French (fr)
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Barry W. L. Southward
John G. Nunan
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Umicore AG and Co KG
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Umicore AG and Co KG
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Priority to RU2011151282/05A priority Critical patent/RU2011151282A/ru
Priority to EP19199595.0A priority patent/EP3616777A1/en
Priority to JP2012511173A priority patent/JP2012527338A/ja
Priority to BRPI1013026A priority patent/BRPI1013026A2/pt
Priority to EP10721975A priority patent/EP2432577A1/en
Priority to CN201080017819.9A priority patent/CN102413904B/zh
Publication of WO2010133309A1 publication Critical patent/WO2010133309A1/en
Anticipated expiration legal-status Critical
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    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
    • F01N—GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR MACHINES OR ENGINES IN GENERAL; GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR INTERNAL-COMBUSTION ENGINES
    • F01N3/00—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust
    • F01N3/08—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for rendering innocuous
    • F01N3/10—Exhaust 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
    • F01N3/105—General auxiliary catalysts, e.g. upstream or downstream of the main catalyst
    • F01N3/106—Auxiliary oxidation catalysts
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
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    • B01D53/34—Chemical or biological purification of waste gases
    • B01D53/92—Chemical or biological purification of waste gases of engine exhaust gases
    • B01D53/94—Chemical or biological purification of waste gases of engine exhaust gases by catalytic processes
    • B01D53/944—Simultaneously removing carbon monoxide, hydrocarbons or carbon making use of oxidation catalysts
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    • B01D53/94—Chemical or biological purification of waste gases of engine exhaust gases by catalytic processes
    • B01D53/9459—Removing one or more of nitrogen oxides, carbon monoxide, or hydrocarbons by multiple successive catalytic functions; systems with more than one different function, e.g. zone coated catalysts
    • B01D53/9463—Removing one or more of nitrogen oxides, carbon monoxide, or hydrocarbons by multiple successive catalytic functions; systems with more than one different function, e.g. zone coated catalysts with catalysts positioned on one brick
    • B01D53/9468—Removing one or more of nitrogen oxides, carbon monoxide, or hydrocarbons by multiple successive catalytic functions; systems with more than one different function, e.g. zone coated catalysts with catalysts positioned on one brick in different layers
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    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
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    • B01J37/02—Impregnation, coating or precipitation
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    • B01J37/0246—Coatings comprising a zeolite
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
    • F01N—GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR MACHINES OR ENGINES IN GENERAL; GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR INTERNAL-COMBUSTION ENGINES
    • F01N3/00—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust
    • F01N3/08—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for rendering innocuous
    • F01N3/10—Exhaust 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
    • F01N3/103—Oxidation catalysts for HC and CO only
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
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    • B01D2255/00—Catalysts
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    • B01D2255/00—Catalysts
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    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
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    • B01J29/04—Catalysts comprising molecular sieves having base-exchange properties, e.g. crystalline zeolites
    • B01J29/06—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof
    • B01J29/70—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof of types characterised by their specific structure not provided for in groups B01J29/08 - B01J29/65
    • B01J29/7007—Zeolite Beta
    • B—PERFORMING OPERATIONS; TRANSPORTING
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    • B01J37/0009—Use of binding agents; Moulding; Pressing; Powdering; Granulating; Addition of materials ameliorating the mechanical properties of the product catalyst
    • B01J37/0027—Powdering
    • B01J37/0036—Grinding
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
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    • F01N2370/00—Selection of materials for exhaust purification
    • F01N2370/02—Selection of materials for exhaust purification used in catalytic reactors
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    • F01N2570/00—Exhaust treating apparatus eliminating, absorbing or adsorbing specific elements or compounds
    • F01N2570/12—Hydrocarbons
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    • F01N—GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR MACHINES OR ENGINES IN GENERAL; GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR INTERNAL-COMBUSTION ENGINES
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Definitions

  • HC storage/release component conventionally a microporous crystalline aluminosilicate also known as a Zeolite or molecular sieve, is employed to prevent low temperature HC poisoning of the PGM centres (see Applied Catalysis B, vol. 70, (2007), p2, Applied Catalysis A vol. 221, (2001), p443).
  • the introduction of the Zeolite in the DOC provides a mechanism for the low temperature condensative adsorption of a significant portion of the higher molecular weight unburat HC species emitted during 'cold start' of the engine. This limits the potential for HC adsorption on active precious metal centres and their resultant poisoning by 'site-blocking'.
  • the retained HC species are 'released' by evaporation and diffusion out of the porous structure of the Zeolite but only at temperatures where the PGM is fully active and capable of combusting the plume of released species (see US 2,125,231).
  • the choice of metal(s) in the DOC is based upon their ability to offer the highest turnover frequency (number of reactions per second) with respect to the oxidation of CO and Hydrocarbon to CO 2 and H 2 O at low temperatures and low concentrations of active component within the DOC formulation.
  • Pt e.g. US 5,627,124
  • Pd has been employed as the primary catalytic species (e.g. US2008/0045405 Al, U. Neuhausen, K.V. Klementiev, F.-W. Schutze, G. Miehe, H. Fuess and E.S. Lox in Applied Catalysis B: Environmental, vol. 60, 3-4, (2005), pl91-199 and references therein).
  • the invention disclosed herein describes a new class of layered and zoned DOC systems capable of addressing the challenges and requirements outlined previously.
  • This new class of Pd-rich DOCs provides both high activity but also enhanced hydrothermal durability, especially with regards to the cycle post-injection DPF regeneration cycles typical of modern vehicular applications, as compared to conventional DOC technologies.
  • These benefits are realised by the combination of functionalised layers to introduce the capability of the DOC to resist 'quenching' i.e. transient active site blocking arising from (especially) HC or CO under lower temperatures i.e. 'cold start' conditions.
  • the use of 'quench' tolerant overcoat with a second dedicated oxidation layer, which itself may also be Pd rich provides a synergy which enables high conversion of pollutants at lower temperatures and with increased hydrothermal durability.
  • the present invention describes a method for removal of gaseous pollutants from the exhaust stream of a diesel/compression ignition engine. This is achieved by contacting the exhaust stream with the novel catalyst described herein, where the catalyst comprises a novel washcoat design comprising two functionalised layers which enable high catalytic performance over a range of PGM contents and ratios of Pt:Pd, including technologies enriched in Pd content.
  • the present invention provides an oxidation catalyst, for the remediation of pollutants from the exhaust of a compression ignition comprising a carrier or substrate upon which is disposed at least two layers of washcoat wherein:
  • the first layer or undercoat layer comprises a refractory oxide support, optionally a zeolite, optionally an oxygen storage material and a primary catalyic metal selected from the group consisting of platinum, palladium, iridium, rhodium, ruthenium, alloys thereof, and mixtures thereof
  • a second layer or overcoat layer comprises a refractory oxide support, optionally a zeolite, optionally an oxygen storage material and a primary catalytic metal selected from the group consisting of platinum, palladium, iridium, rhodium, ruthenium, alloys, thereof, and mixtures thereof,
  • the Pt:Pd ratio of the undercoat is from about 20:1 to about 1:2
  • the Pt:Pd ratio of the overcoat is from about 2:3 to about 0:1 e.g. a Pt-free, Pd-only layer.
  • the Pt:Pd ratio of the undercoat is about 1:1 and the Pt:Pd ratio of the overcoat is about 1:2.
  • the overcoat may optionally contain salts or oxides of barium or lantherium.
  • the refractory oxide support in the undercoat and/or the overcoat is alumina, a modified or heteroatom doped alumina, zirconia or titania or combinations thereof.
  • the heteroatom dopant can be Si, Fe, Zr, Ba or La or combinations thereof.
  • the optional zeolite in the undercoat and/or overcoat is selected from the group Beta ( ⁇ ), Chabazite, Clinoptilolite, Faujastie, Ferrierite, Mordenite, Offretite, Silicalite, zeolite X, zeolite Y, ultrastable zeolite Y, ZSM5, ZSMl 1, ZSM22 or other ZSM series material or structural isomorphs thereof, e.g. SAPO34 or mixtures thereof.
  • the catalyst device of the invention has an inlet and an outlet and, and the overcoat is optionally applied to cover a length of about 5% to about 75% from the inlet, and the undercoat is applied to cover a length of about 95% to about 25% from the inlet.
  • Another aspect of the invention relates to a diesel oxidation catalyst wherein the catalyst has an inlet and an outlet, wherein a washcoat zone is applied to cover a length of about 25% to about 95% from the inlet and the washcoat contains Pt:Pd at a ratio of about 2:3 to about 0:1 and a second washcoat zone is optionally applied to cover a length of about 5% to about 75% from the outlet and the washcoat contains Pt:Pd at a ratio of about 2: 1 to about 1 :2.
  • a still further aspect of the invention relates to a method of treating exhaust gas comprising passing an exhaust gas over a catalytic device, comprising: a housing disposed around a substrate; an oxidation catalyst, for the remediation of pollutants from the exhaust of a compression ignition comprising a carrier or substrate upon which is disposed at least two layers of washcoat wherein:
  • the first layer or undercoat layer comprises a refractory oxide support, optionally a zeolite, optionally an oxygen storage material and primary catalytic metal(s) selected form the group of Precious Group Metals consisting of platinum, pallandium, iridium, rhodium, ruthenium, alloys thereof, and combinations thereof;
  • a second layer or overcoat layer comprises a refractory oxide support, optionally a zeolite, optionally an oxygen storage material and primary catalytic metal(s) selected from the group of Precious Group Metals consisting of platinum, palladium, iridium, rhodium, ruthenium, alloys thereof, and combinations thereof;
  • the catalytic device of the invention further includes a retention material disposed between the housing and the substrate.
  • Figure 1 shows the effect of a Propene/Propane mix (120 ppm Cl) on the CO light-off (T5 0 ) for conventional PtPd DOC, 120 gcf PGM @ 3:1, in SGB testing.
  • Figure 2 compares the light-off and quench/light-down performance for conventional PtPd DOC 120 gcf @ 3:1 in SGB testing.
  • Figure 5 compares the light-off and light-down for the conventional PtPd DOC 120 gcf @ 3:1, and three next generation 'quench' resistant DOC technologies A, B, and C.
  • Figure 6 illustrates the impact of CO or HC pulses on the isothermal activity at 170, 160 and 150 0 C for next generation 'quench' resistant DOC Catalyst B.
  • Figure 9 illustrates engine dynamometer aging and testing of conventional DOC, 120 gcf PGM at 3:1 versus 'quench' resistant DOC technologies at 160 gcf Pt: Pd 1: 1.13.
  • Figure 10 compares the engine dynamometer aging and testing of conventional DOC, 120 gcf PGM at 3:1 vs 'quench' resistant DOC technologies at differing PGM content and Pt:Pd ratios (G is 160 @ 1:1.13, H is 143 @ 1.3:1 and J is 183 @ 1:1.77).
  • Figure 11 shows the vehicle performance of the DOC technologies ex Figure 10.
  • Figure 12 compares the dyno aging/testing of a conventional DOC - 120 @ 3:1 vs 'quench' resistant DOCs (160 @ 1 :1.13) with differing Pt:Pd distributions in Pass 1 and 2.
  • Figure 13 contrasts the dyno testing of a conventional DOC, 120 gcf PGM at 3:1 vs 50% zoned coated 'quench' resistant DOCs at 154 gcf @ 4:3 (1.3:1).
  • Figure 14 summarizes the vehicle performance of an OEM DOC versus one commercial DOC 70 gcf @ 3/2 versus a zone-coated quench resistant DOC 70 gcf @ 3/2.
  • Figure 15A and B show the SGB testing/oven aging data for a conventional DOC, 150 gcf PGM @ 4:1 vs 'quench' resistant DOC, 210 gcf PGM @ 1:1.1 using complex HC mix.
  • Figure 16A and B show the SGB testing /oven aging data for a conventional DOC, 150 @ 4:1 vs 'quench' resistant DOC, 210 gcf PGM @ 1:1.1 using C3 only HC mix.
  • Figure 17 illustrates the impact of Pt:Pd ratio on performance of conventional DOC, 120 gcf PGM at 3:1 versus 120 gcf @ 2:1 Pt:Pd.
  • the present invention relates to the development and use of novel high Pd content diesel oxidation catalyst (DOC) for emission aftertreatment catalysis.
  • DOC diesel oxidation catalyst
  • This is made possible by the development of a specific layered or zoned strategy, wherein the distinct layers afford specific functionalities to the catalyst and work in concert to provide an effective synergy for overall improvements in performance and durability.
  • the design herein employs a more conventional undercoat (pass 1) to facilitate the required CO, HC and NO oxidation reactions and a second layer or zone (pass 2), which is enriched in Pd or indeed Pd-only, which has been developed to provide the catalyst with a characteristic dubbed 'quench' tolerance.
  • Both layers comprise typical base metal components e.g. alumina (or other suitable refractory oxide e.g. Z1O 2 , TiO 2 ), zeolite for bulk HC storage/release and optionally an oxygen storage material based upon CeZrOx.
  • alumina or other suitable refractory oxide e.g. Z1O 2 , TiO 2
  • zeolite for bulk HC storage/release and optionally an oxygen storage material based upon CeZrOx.
  • zeolites have well defined channel and/or cage structures arising from the combination of primary building units (repeating structures derived from the assemblages of TO4 tetrahedra, where T is Si or Al ) e.g. for MFI zeolites the primary building unit is the 5-1 ring structure (see http://www.iza-structure.org/databases for further details).
  • the combination of these primary building units gives rise to the secondary order within the zeolite and thus enforces limits upon the maximum size of species which may enter the structure, i.e. provides the 'molecular sieve' function.
  • zeolite ⁇ the structure contains two 12 ring structures, one a regular ring of 5.6 by 5.6 A and a second more irregular ring of ca. 7.7 by 6.6 A (at maximum and minimum), and hence molecules with diameters (so- called critical diameters) larger than this are excluded and thus the zeolite cannot prevent adsorption of such large HCs e.g. poly-substituted aromatics or poly-aromatic species on active PGM sites.
  • the first layer/pass/zone applied to the substrate hereafter the undercoat, comprises a refractory oxide support e.g. (modified/doped) alumina, zirconia etc. and optionally a zeolite and also optionally an OS material.
  • the undercoat is characterised by possessing Pt and optionally Pd at a ratio of about Pt:Pd 20:1 to about 1:2.
  • overcoat again comprises a refractory oxide support e.g. (modified/doped) alumina, zirconia, titania etc. and optionally a zeolite and also optionally an OS material.
  • a refractory oxide support e.g. (modified/doped) alumina, zirconia, titania etc. and optionally a zeolite and also optionally an OS material.
  • the base metal oxide components of the undercoat and overcoat may be identical. This enables production of a 'white' washcoat which is split into two batches prior to coating and the appropriate PGM loads and ratios added individually.
  • the overcoat also contains precious metal, but in this instance the washcoat is enriched in Pd such that the ratio of PtPd is about 0:1 (i.e. Pd-only) to about 2:3.
  • Pd-only i.e. Pd-only
  • This strategy is contra to the teachings in US 2005/0045405 Al wherein a layered design is also employed but this design is based upon a Pt-enriched overcoat and Pd-enriched undercoat.
  • US 2005/0045405 Al stresses the importance of avoiding Pd migration to the overcoat and that it is necessary to omit zeolite (HC storage component) from the undercoat, neither of these teachings are consistent with the current invention.
  • this design is intended to maximise NO 2 production rather than provide optimised CO, HC and NO oxidation function. Further differentiation will be drawn in the following examples.
  • the novel oxidation catalyst described herein is intended for the remediation of pollutants from the exhaust of a compression ignition engine. It comprises a carrier or substrate upon which is disposed at least two layers of washcoat wherein at least both layers comprise a refractory oxide support (alumina, heteroatom doped alumina e.g. Si, Fe, Zr, Ba or La, or zirconia as ZrO 2 , titania etc.), optionally a zeolite e.g.
  • a refractory oxide support alumina, heteroatom doped alumina e.g. Si, Fe, Zr, Ba or La, or zirconia as ZrO 2 , titania etc.
  • a zeolite e.g.
  • the layers of the catalyst may contain different base metal components or indeed identical components but the two layers are especially differentiated in that the second layer (overcoat) is substantially enriched in Pd content and particularly wherein the Pd to Pt ratio of the overcoat is greater than that of the undercoat.
  • the Pt:Pd ratio of the undercoat is from about 20:1 to about 1:2 while the Pt:Pd ratio of the overcoat is from about 2:3 to about 0:1 i.e. a Pt- free, Pd-only layer.
  • the catalyst may contain two layers wherein the Pt:Pd ratio of the undercoat is about 1:1 and the Pt:Pd ratio of the overcoat is about 1:2.
  • the overcoat may additionally contain Rhodium.
  • the overcoat may additionally be modified by the inclusion of salts or oxides of Barium and Lanthanum.
  • the layers of the catalyst may also be expressed as zones e.g. wherein the catalyst has an inlet and an outlet, and the overcoat is applied to cover a length of about 5% to about 75% from the inlet. Similarly, wherein the catalyst has an inlet and an outlet, and the undercoat is applied to cover a length of about 95% to about 25% from the inlet.
  • SGB Synthetic Gas Bench
  • Figure 3 further examines the ability of CO and propene to 'quench' the catalytic oxidation function of the commercial DOC.
  • This Figure contrasts the performance of the 120 gcf 3:1 DOC under isothermal conditions with transient pulses of either CO or HC viz.
  • the DOC is exposed to 12% O2, CsHg/C ⁇ Hg (3:1) @ 150 ppm Cl, 150 ppm NO, 5% CO2, 5% H2O and N2 (30 1/min) plus 400 ppm CO, which is increased to 1200 ppm for 5 min to attempt to quench catalytic function.
  • the catalyst maintains 100% CO conversion at 170 0 C under both low and high CO conditions but upon decreasing the temperature to 160 0 C the catalyst is thermally deactivated and ⁇ 20% conversion is seen for both low and high CO at 160 and 150 0 C, consistent with catalyst deactivation due to domination of the surface by HC and CO species.
  • the bed temperature of the catalyst reflects the various processes. Thus small increases in the bed exotherm are associated with the high CO pulses and as the catalyst deactivates the exotherm in the catalyst is seen to traverse from the front of the core to the rear (where the thermocouple was located) and hence immediately prior to complete deactivation an exotherm is recorded. In the case of the HC pulses a different response is noted.
  • each HC pulse is associated with a much larger bed exotherm than seen for the CO pulses, consistent both with the higher increase in fuel content but also with the exotherm being close to the outlet of the core.
  • a decrease in CO conversion is noted.
  • This loss in CO function is further evident during the third pulse consistent with the proposed mechanism of HC site blocking resulting in catalyst deactivation, a process we have dubbed 'quenching'. Then as the temperature of the catalyst is decreased to 160 0 C, immediate and complete deactivation occurs, suggesting the catalyst was already in a more unstable condition with regards to oxidation function, this sensitivity being ascribed to a significantly higher residual HC coverage arising from the HC pulsing.
  • Table 1 summarizes the impact of HC content and species, and the role of zeolite or 'quench' resistant pre-bed on the activity of a 3%Pd-Zr ⁇ 2 model DOC.
  • Table 1 The impact of HC content, HC speciation, and the presence or absence of zeolite on the activity of a 3%Pd-Zr ⁇ 2 model DOC in SGB powder studies.
  • 1:1 Mix denotes 1:1 mixture of Propene and n-Octane (350 ppm Cl of each HC).
  • the performance of the commercial DOC of Figure 2 is now contrasted with that for Catalyst A (aged as per reference), a next generation DOC ( Figure 4).
  • the DOC herein contains Rh, which is included in the overcoat, and is employed specifically for its ability to oxidise CO with far less inhibition or competition from HC i.e. Rh is oxo-phillic and hence the surface is found to contain significantly higher O coverage under all conditions. Due to this characteristic the CO light-off and quench occur at far lower temperatures than for the commercial DOC. Moreover, the CO and HC light-off features are no longer interconnected further reflecting the change in surface competition vis-a-vis O, HC and CO for this technology. However it should also be noted that the concept technology described herein achieves high performance at a significant price premium due to the use of Rh. Hence what is required is to achieve comparable activity benefits at competitive price.
  • Catalyst B maintains full CO conversion at 160 0 C at both high and low CO concentration but in contrast exhibits stepwise deactivation with subsequent pulses of high HC, akin to titration of the active sites by retention of 'toxic', site-blocking propene- derived species. Moreover as the temperature is cooled to 150 0 C the test ex HC pulse sample again exhibits a near instantaneous decrease to 0% CO conversion, while for the ex CO pulse test again shows the propagation of exotherm /deactivation front through the core before the catalyst is quenched, consistent with Figure 3 and the mechanism proposed therein. The performance of Catalyst C is even better.
  • Figure 9 compares the dyno aging and testing performance of the commercial DOC 120 gcf @ 3:1 versus two further layered DOC technologies E and F. In this instance the samples were aged by standard DPF regeneration or by aggressive DPF regeneration (with 400 0 C catalyst inlet and 850 0 C catalyst bed temperature during post injection).
  • the enhanced performance obtained with this new DOC design is possible with a range of Pt: Pd ratios.
  • the Pt: Pd ratio of the undercoat is from about 20:1 to about 1 :2 and the Pt: Pd ratio of the overcoat is from about 2:3 to about 0:1.
  • catalysts G, H and J all offer competitive performance versus the commercial DOC reference, as shown in the dyno performance summary in Figure 10. It should be stressed that in all cases the performance is equal, or typically better, whilst offering PGM savings of 2.84, 2 and 4.88% respectively.
  • Figure 11 compares vehicle performance data for the DOC parts of Figure 10. This testing on a typical Euro 4 engine confirms the benefits seen on the dyno. All test parts offer equal, or better, activity with up >10% decrease in CO emissions seen for Catalysts G and H. In all cases the benefits are ascribed to superior EUDC performance i.e. better light-off and increased tolerance to quenching from HC poisons.
  • Figure 13 examines the potential for applying the second layer of the quench resistant DOC as a partial or zone pass. Additionally it reports the performance for a series of parts wherein Pd is again 'thrifted' from the second pass and moved into the first. The data suggest that by zone coating, again in combination with the type of higher zeolite contents as employed in Figure 13, it becomes possible to increase the Pt:Pd ratio in the second layer (zone) without the adverse effects noted previously. Thus parts N, O and P display equivalent performance. Note no comparison is drawn here versus the reference since the PGM cost of the test parts is too high for meaningful comparison.
  • FIG. 14 reports vehicle performance data for three DOCs tested after 7Oh of post injection aging performed at a major OEM.
  • the three DOCs comprise an internal OEM reference versus a conventional DOC 70gcf @ 3:2 (catalyst Q) and zone coated quench resistant DOC also 70 gcf @ 3:2 (Catalyst R).
  • the data show again a clear performance benefit for the new generation DOC which provides 79% CO and 86% HC conversion respectively over the NEDC cycle for a vehicle with comparatively cool engine out temperatures (average 150 0 C for first 800 s) consistent with the enhanced light-off and decreased 'quenching' of the new generation design.
  • Figures 15A/B and 16A/B show the SGB performance data after increasingly severe hydrothermal oven aging cycles for two commercial DOCs 150 gcf @ 4:1 versus the new generation DOC 210 @ 1 : 1.10. Samples were tested as cores 2.22 cm*2.54 cm after aging at 700 0 C, 25 hours, 10% steam, air and 800 0 C, 25 hours, 10% steam, air. Two SGB test protocols were employed to further differentiate the impact of HC concentration and speciation on performance.
  • the first test conditions were selected to mimic a Euro V exhaust and comprised lOOOppm CO, 600 ppm Cl n-Octane, 180 ppm Cl Methyl-Benzene, 75 ppm Cl Propene, 75 ppm Cl Methane, 80 ppm NO, 3 ppm SO2, 3.5% CO2, 13% O2, 3.5% H2O, balance N2 and total flow 5 1 /min with ramp from 50 to 300 0 C at 10 °C/min (hereafter complex HC mix test).
  • the second set of test conditions were more typical 'SGB' conditions, employing only light HC species and comprised 350 ppm CO, 120 ppm Kt ⁇ , 90 ppm Cl propene, 180 ppm Cl propane, 2 ppm SO 2 , 270 ppm NO, 6% O2, 10.7% CO2, 3.5% H 2 O and balance N2 and total flow 5 1 /min with ramp from 100 to 400 0 C at 15 °C/min (hereafter C3 only HC mix test).
  • the performance of the cores in the complex HC mix test both suggest the robustness of all DOCs to low levels of SOx poisoning but also re-confirm the CO light-off benefit for the new generation DOC, the benefit again being seen to increase with increasing severity of the aging cycle.
  • FIG. 17 A further differentiation between conventional DOCs and the new generation technology may be found by comparing Figure 17 and Figure 18 wherein the effect Pt:Pd ratio on performance is examined.
  • Figure 17 the activity of commercial DOCs at equal PGM content but differing Pt:Pd ratio (120 @ 3:1 versus 120 @ 2:1) are shown.
  • decreased Pt and increased Pd content correlates with increasing light-off temperatures and HC weaker oxidation performance.
  • the 2:1 DOC also exhibits a more severe deactivation profile with the performance gap being increasingly large with harsher aging.
  • the recovery of the technology after SOx aging is particularly weak.
  • the DOC exhibits exactly the kind of weaknesses associated with increased Pd content in a conventional DOC design, as outlined in US2005/0045405 Al.
  • the performance data in Figure 18 are in even more marked contrast.
  • the fresh and 800 air/steam oven aged performance of three next generation quench resistant DOCs are compared. Testing was performed on a drilled core (1"*3") in the SGB using a matrix of 400 ppm CO (std CO) or 1200 ppm CO (hi CO), 150 ppm Cl propene/propane (3:1) or 450 ppm Cl (hi HC), 12% O2, 150 ppm NO, 5% CO2, 5%
  • a catalytic device can comprise a housing disposed around a substrate with a compression ignition oxidation catalyst disposed at the substrate.
  • the method for treating a compression ignition exhaust stream can comprise: introducing a diesel exhaust stream to a compression ignition oxidation catalyst; and oxidising an exhaust stream component.
  • the catalyst materials are included in the formulation by combining alumina, or other appropriate support, with other catalyst materials to form a mixture, drying (actively or passively), and optionally calcining. More specifically, a slurry can be formed by combining alumina and water, and optionally pH control agents (such as inorganic or organic acids and bases) and/or other components.
  • the catalytic materials e.g. catalytic metals, such as Pt
  • This slurry can then be washcoated onto a suitable substrate.
  • the washcoated product can be dried and heat treated to fix the washcoat onto the substrate.
  • the catalyst can further comprise a zeolite.
  • Possible zeolites include Y-type zeolite, beta ( ⁇ ) zeolite, ZSM-5, silica alumina phosphate (SAPO e.g. SAPO34) and the like, as well as combinations comprising at least one of the foregoing zeolites.
  • SAPO silica alumina phosphate
  • the zeolite can, for example, have a silica to alumina ratio (Si: Al) of about 25 to about 80, or, more specifically, about 35 to about 60. If the zeolite is employed, it can be added to the slurry along with the catalytic material (e.g., before the catalytic material has been calcined).
  • This slurry can be dried and heat treated, e.g., at temperatures of about 500 0 C to about 1,000 0 C, or more specifically about 500 0 C to about 700 0 C, to form the finished catalyst formulation.
  • the slurry can be washcoated onto the substrate and then heat treated as described above, to adjust the surface area and crystalline nature of the support.
  • catalyst metals may optionally be disposed on the support. The catalyst metals, therefore, can be added after the washcoat is fixed onto the substrate by additional washcoat steps and/or by exposing the washcoated substrate to a liquid containing the catalytic metal.
  • the supported catalyst comprises a PGM (Pt, Pd, Rh etc.) or more preferred a combination of PGMs, (modified) alumina, and zeolite, and optionally oxygen storage (OS) material.
  • the amounts of these components in the catalyst can be: about 0.1 wt % to about 10 wt % PGM, about 50 wt % to about 80 wt % (modified) alumina, about 5 wt % to about 50 wt % OS, and about 10 wt % to about 50 wt % zeolite; or, more 'specifically, about 1 wt % to about 5 wt % PGM, about 40 wt % to about 60 wt % modified alumina, about 5 wt % to about 20 wt % of OS, and about 20 wt % to about 40 wt % zeolite.
  • the supported catalyst can be disposed on a substrate.
  • the substrate can comprise any material designed for use in the desired environment, e.g., a compression ignition engine (e.g., a diesel engine) environment.
  • a compression ignition engine e.g., a diesel engine
  • Some possible materials include cordierite, silicon carbide, metal, metal oxides (e.g., alumina, and the like), glasses, and the like, and mixtures comprising at least one of the foregoing materials.
  • These materials can be in the form of packing material, extrudates, foils, perform, mat, fibrous material, monoliths (e.g., a honeycomb structure, and the like), other porous structures (e.g., porous glasses, sponges), foams, molecular sieves, and the like (depending upon the particular device), and combinations comprising at least one of the foregoing materials and forms, e.g., metallic foils, open pore alumina sponges, and porous ultra-low expansion glasses.
  • these substrates can be coated with oxides and/or hexaaluminates, such as stainless steel foil coated with a hexaaluminate scale.
  • the substrate can have any size or geometry, the size and geometry are preferably chosen to optimise geometric area in the given exhaust emission control device design parameters.
  • the substrate has a honeycomb geometry, with the combs through-channel having any multi-sided or rounded shape, with substantially square, triangular, pentagonal, hexagonal, heptagonal, or octagonal or similar geometries preferred due to ease of manufacturing and increased surface area.
  • the substrate can be disposed in a housing to form the converter.
  • the housing can have any design and comprise any material suitable for the application. Suitable materials for the housing can comprise metals, alloys, and the like, such as ferritic stainless steels (including stainless steels such as, e.g., the 400-Series such as SS-409, SS-439, and SS-441), and other alloys (e.g. those containing nickel, chromium, aluminium, yttrium and the like, e.g., to permit increased stability and/or corrosion resistance at operating temperatures or under oxidising or reducing atmospheres).
  • ferritic stainless steels including stainless steels such as, e.g., the 400-Series such as SS-409, SS-439, and SS-441
  • other alloys e.g. those containing nickel, chromium, aluminium, yttrium and the like, e.g., to permit increased stability and/or corrosion resistance at operating temperatures or under oxidising or
  • end cone(s), end plate(s), exhaust manifold cover(s), and the like can be concentrically fitted about the one or both ends and secured to the housing to provide a gas tight seal.
  • These components can be formed separately (e.g., moulded or the like), or can be formed integrally with the housing using methods such as, e.g., a spin forming, or the like.
  • the retention material Disposed between the housing and the substrate can be a retention material.
  • the retention material which may be in the form of a mat, particulates, or the like, may be an intumescent material e.g., a material that comprises vermiculite component, i.e., a component that expands upon the application of heat, a non-intumescent material, or a combination thereof.
  • intumescent material e.g., a material that comprises vermiculite component, i.e., a component that expands upon the application of heat, a non-intumescent material, or a combination thereof.
  • These materials may comprise ceramic materials e.g., ceramic fibres and other materials such as organic and inorganic binders and the like, or combinations comprising at least one of the foregoing materials.
  • the coated monolith containing the high Pd-content layered DOC is incorporated into the exhaust flow of the compression ignition engine.
  • This provides a means for treating said compression ignition exhaust stream to reduce the concentrations of environmental toxins by passing said diesel exhaust stream over the aforementioned compression ignition oxidation catalyst under net oxidising conditions (oxygen rich) to facilitate catalytic conversion/oxidation into more environmentally benign products.
  • PGM mass Adjust slurry pH to 5-6 prior to PGM addition. Add Palladium Nitrate solution to slurry vortex over 30 minutes, prevent slurry from reaching pH values of less than 3 by judicious use of base. Stir for 2 hours to allow foil chemisorption of Pd. Next add Rh nitrate dropwise to slurry vortex, again prevent pH from going below 3 with base. Stir 1 hour. Check specific gravity and pH and adjust to facilitate coating in one pass. Then coat monolith in 1 pass and calcine at temperatures > 540 0 C for > 1 hour.
  • Pass 1 take the required concentration of Pt nitrate solution and slowly dilute with appropriate rheology modifiers as required prior to adding solution dropwise to milled Alumina slurry.
  • Slurry must be at a pH lower than 6.0 prior to metal addition and during Pt addition, monitor pH and prevent slurry from going to pH values below 3.0 with the judicious use of base. After metal addition, adjust to a pH of 3.5 with base and stir slurry for two hours. Examine d5 ⁇ , do,o and djoo to confirm no agglomeration of PGM has occurred.
  • Slurry must be at a pH lower than 6.0 prior to metal addition and during Pt addition, monitor pH and prevent slurry from going to pH values below 3.0 with the judicious use of base. After metal addition, adjust to a pH of 3.5 with base and stir slurry for two hours. Examine dso, do.o and dioo to confirm no agglomeration of
  • Zone Pass 2 49.4 HP 14/150 Zr5 1.2Ba 20gcf Pd 1 Ogcf Pt 17.47 ⁇ -40 50% [0115]
  • X Pass 1 - 82.5 HP14/150 Zr5 50gcf Pd 55gcf Pt 29.1 ⁇ -40

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EP19199595.0A EP3616777A1 (en) 2009-05-18 2010-05-11 High pd content diesel oxidation catalyst with improved hydrothermal durability
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BRPI1013026A BRPI1013026A2 (pt) 2009-05-18 2010-05-11 "catalisadores de oxidação de diesel com alto teor de pd com durabilidade hidrotérmica aprimorada".
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CN102413904A (zh) 2012-04-11
JP2012527338A (ja) 2012-11-08
RU2011151282A (ru) 2013-06-27
EP2432577A1 (en) 2012-03-28
EP3616777A1 (en) 2020-03-04
KR20120026096A (ko) 2012-03-16
BRPI1013026A2 (pt) 2016-04-05
US20100290964A1 (en) 2010-11-18
US8246923B2 (en) 2012-08-21

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