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Composite, zoned oxidation catalyst for compression ignition internal combustion engine

A composite oxidation, compression ignition technology, applied in physical/chemical process catalysts, metal/metal oxide/metal hydroxide catalysts, internal combustion piston engines, etc., can solve performance loss, hinder active sites or pores, loss, etc. problems, to achieve the effect of improving durability, reducing costs, and improving management

Pending Publication Date: 2021-12-10
JOHNSON MATTHEY PLC
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0043] It is believed that two basic mechanisms by which catalysts used to treat exhaust gases from internal combustion engines may be poisoned are: (i) selective poisoning, in which pollutants react directly with active sites or catalyst supports, resulting in reduced or catastrophic loss of activity; and (ii) non-selective poisoning, which sterically hinders access to the active sites or pores in the catalyst support by contaminating (or masking) the surface of the support or active sites, resulting in loss of performance

Method used

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  • Composite, zoned oxidation catalyst for compression ignition internal combustion engine
  • Composite, zoned oxidation catalyst for compression ignition internal combustion engine
  • Composite, zoned oxidation catalyst for compression ignition internal combustion engine

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0373] Embodiment 1 (comparison)

[0374] A bare cordierite honeycomb structure flow-through substrate monolith with 400 cells per square inch, a wall thickness of six thousandths of an inch (6 mils) and a total length of 4 inches was coated with the catalyst washcoat in the following zoned arrangement. A first catalyst washcoat slurry comprising an aqueous salt of platinum and palladium (as nitrate) and an alumina support doped with 5% by weight silica was applied to the substrate monolith from one end marked as the inlet end Axial length up to 75% of the total base monolith length. The concentrations of the platinum and palladium salts were chosen to achieve a 2:1 platinum to palladium weight ratio in the first catalyst washcoat of 6.67Pt:3.33Pd gft in the coating -3 load. The inlet coating was then dried in a conventional oven at 100°C for 1 hour to remove excess water and other volatiles.

[0375] A second catalyst washcoat slurry comprising an aqueous solution of pla...

Embodiment 2

[0381] The same product as disclosed in Comparative Example 1 was prepared except that, in addition to the aqueous salts of platinum and palladium, the first catalyst washcoat slurry contained an aqueous barium acetate salt according to the invention. The concentration of barium acetate is chosen such that the barium loading in the first catalyst washcoat is 80 gft for 75% of the axial length of the first catalyst washcoat -3 . That is, the first catalyst washcoat zone and the second catalyst washcoat zone comprise 80 gft -3 loading of barium. The total PGM loading and Pt:Pd weight ratio on the substrate monolith as a whole is the same as in Example 1, i.e. 20 gft -3 .

[0382] Using EPMA-WDX image analysis, it was found that the first catalyst washcoat region prepared in this way had a reduced amount of Pd in ​​the perpendicular direction towards the substrate surface, and to a lesser extent the same as Pt, but also had an amount of Pd in ​​the Relatively strong inhomogen...

Embodiment 3

[0383] Example 3 - Test method and results for comparison of the presence and absence of barium in the inlet zone

[0384] Each of the composite oxidation catalysts prepared according to Examples 1 and 2 was thermally analyzed using a laboratory bench-mounted diesel engine. The engine runs on EUVI B7 fuel (7% biofuel) for engine operation and exhaust hydrocarbon enrichment (exothermic generation), runs at 2200rpm and is equipped with an exhaust system consisting of exhaust pipes and removable , into which each composite oxidation catalyst can be inserted for testing, with the inlet end / first catalyst, highly loaded washcoat zone oriented to the upstream side. The engine is a 7-litre capacity EUV 6-cylinder producing 235kW at 2500rpm, and the exhaust system includes a "7th injector" which is set up to inject hydrocarbon fuel directly into the exhaust pipe, which is in the Downstream of the engine manifold and upstream of the composite oxidation catalyst to be tested. This i...

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Abstract

A composite oxidation catalyst (18, 20) for use in an exhaust system for treating an exhaust gas produced by a vehicular compression ignition internal combustion engine (30) and upstream of a particulate matter filter (44, 50) in the exhaust system comprises a substrate (5) having a total length L and a longitudinal axis and having a substrate surface extending axially between a first substrate end (I) and a second substrate end (O); and three or more catalyst washcoat zones (1, 2, 3; or 1, 2, 3, 4) arranged axially in series on and along the substrate surface, wherein a first catalyst washcoat zone (1) having a length L1, wherein L1 < L, is defined at one end by the first substrate end (I) and at a second end by a first end (19, 21) of a second catalyst washcoat zone (2) having a length L2, wherein L2 < L, wherein the first catalyst washcoat zone (1) comprises a first refractory metal oxide support material and two or more platinum group metal components supported thereon comprising both platinum and palladium at a weight ratio of platinum to palladium of >=1; the second catalyst washcoat zone (2) comprises a second refractory metal oxide support material and one or more platinum group metal components supported thereon; and a third catalyst washcoat zone (3) comprising a third refractory metal oxide support material and one or more platinum group metal components supported thereon is defined at a second end thereof by the second substrate end (O), wherein a total platinum group metal loading in the first catalyst washcoat zone (1) defined in grams of platinum group metal per cubic foot of substrate volume (g / l) (g / ft3) is greater than a total platinum group metal loading in the second catalyst washcoat zone (2), wherein a total platinum group metal loading in the third catalyst washcoat zone (3) defined in grams of platinum group metal per cubic foot of substrate volume (g / l) (g / ft3) is less than the total platinum group metal loading in the second catalyst washcoat zone (2) and wherein the first catalyst washcoat zone (1) comprises one or more first alkaline earth metal components supported on the first refractory metal oxide support material.

Description

technical field [0001] The present invention relates to a composite zoned oxidation catalyst for use in an exhaust system for treating exhaust gas produced by a compression ignition internal combustion engine of a vehicle, preferably for heavy duty diesel vehicles and located upstream of a particulate filter in the exhaust system . The invention also relates to an exhaust system or a vehicle comprising a composite zoned oxidation catalyst. The present invention also relates to the use of a composite zoned oxidation catalyst for generating an exotherm to regenerate a downstream particulate filter; and a method for preparing the composite zoned oxidation catalyst. Background technique [0002] Internal combustion engines produce pollutants such as carbon monoxide (CO), unburned hydrocarbons (HC), nitrogen oxides (NO x ) and particulate matter (PM) exhaust. Emission standards for pollutants in the exhaust gases produced by internal combustion engines, especially for vehicle ...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J23/40B01J23/44B01J23/58B01J23/656B01J35/04F01N3/10F01N3/28B01D53/94B01D53/62B01D53/72B01D53/56
CPCB01J23/44B01J23/58B01J23/40B01J23/6562B01D53/945F01N3/101F01N3/2803B01D2258/012B01D53/944B01D2255/1021B01D2255/1023B01D2255/2042B01D2255/9032B01D2255/9035B01D2255/9037B01J23/894B01J37/0215B01J37/0242B01J37/0244B01J37/0246B01J37/038F01N3/021F01N3/035F01N3/103F01N3/2066F01N3/28F01N2510/0682F01N2510/0684F01N2590/08Y02A50/20Y02T10/12B01D53/9477B01J37/0248F01N2370/00B01J35/19B01J35/30B01J35/396B01J35/56B01J21/08B01J23/42F01N3/0231F01N3/10F01N2570/10F01N2570/12F01N2570/14
Inventor A·奇菲K·科尔O·库珀C·戴利L·吉尔伯特R·汉利大卫·米卡莱夫F·莫罗P·菲利普斯G·普拉特
Owner JOHNSON MATTHEY PLC
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