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US 7,063,818 B2Granted
HC-adsorbent for internal combustion engine
AssigneeHonda Giken Kogyo Kabushiki Kaisha
InventorsTetsuo Endo, Haruhiko Shimizu, Go Motohashi
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AssigneeHonda Giken Kogyo Kabushiki Kaisha
InventorsTetsuo Endo, Haruhiko Shimizu, Go Motohashi
Estimating the term…
An internal combustion engine HC-adsorbent is located in one of a pair of exhaust passages in parallel to each other downstream of an emission control catalyst for purifying an exhaust gas and through which exhaust gas flows selectively by a switchover valve. The adsorbent is a zeolite mixture having pores at least 3.5 Å and smaller than 6 Å and not equal or larger than 6 Å and smaller than 7 Å, and zeolite having pores at least 7 Å and smaller than 10 Å and not equal or larger than 6 Å and smaller than 7 Å. HCs are desorbed quickly and easily lowering the desorption temperature, while ensuring excellent adsorbing performance for HCs of different molecular diameters. Even when a vehicle travels only a short duration after engine starting, desorption advances quickly and reliably, the adsorbent exhibiting intended adsorbing performance at the next engine starting.
An HC adsorbent for an internal combustion engine, which is mounted in one of a pair of exhaust passages which are provided in parallel to each other in an exhaust pipe downstream of an exhaust emission control catalyst for purifying an exhaust gas of the internal combustion engine, and through which the exhaust gas is permitted to flow selectively by a switchover valve, wherein said adsorbent is formed of a mixture of a plurality of types of zeolites having pores of different small diameters, a zeolite having pores of a small diameter equal to or larger than 3.5 Å and smaller than 6 Å and no pore of a small diameter equal to or larger than 6 Å and smaller than 7 Å and a zeolite having pores of a small diameter equal to or larger than 7 Å and smaller than 10 Å and no pore of a small diameter equal to or larger than 6 Å and smaller than 7 Å being contained in a total amount equal to or higher than 80% by weight in the mixture, and a zeolite having pores of a small diameter equal to or larger than 6 Å and smaller than 7 Å being also contained in an amount not exceeding 20% by weight in the mixture, wherein a ferrierite-type zeolite and a pentasil-type zeolite are selected as the zeolite having the pores of the small diameter equal to or larger than 3.5 Å and smaller than 6 Å and no pore of the small diameter equal to or larger than 6 Å and smaller than 7 Å, and a faujasite-type zeolite is selected as the zeolite having the pores of the small diameter equal to or larger than 7 Å and smaller than 10 Å and no pore of the small diameter equal to or larger than 6 Å and smaller than 7 Å, and in a three-component composition diagram in which each of ratios is indicated by one point within an equilateral triangle having three apexes each indicating the case where the mixture includes only one of zeolite components, the weight ratio of the ferrierite-type, pentasil-type and faujasite-type zeolites is set to lie in a region surrounded by a line segment connecting a point of (0:0.2:0.8), a point of (0.08:0.12:0.8), a point of (0.4:0.08:0.52), a point of (0.67:0.1:0.23), a point of (0.67:0.23:0.1), a point of (0.4:0.51:0.09), a point of (0.09:0.81:0.1) and a point of (0:0.81:0.19) to one another.
An HC adsorbent for an internal combustion engine, which is mounted in one of a pair of exhaust passages which are provided in parallel to each other in an exhaust pipe downstream of an exhaust emission control catalyst for purifying an exhaust gas of the internal combustion engine, and through which the exhaust gas is permitted to flow selectively by a switchover valve, wherein said adsorbent is formed of a mixture of a plurality of types of zeolites having pores of different small diameters, a zeolite having pores of a small diameter equal to or larger than 3.5 Å and smaller than 6 Å and no pore of a small diameter equal to or larger than 6 Å and smaller than 7 Å and a zeolite having pores of a small diameter equal to or larger than 7 Å and smaller than 10 Å and no pore of a small diameter equal to or larger than 6 Å and smaller than 7 Å being contained in a total amount equal to or higher than 80% by weight in the mixture, and a zeolite having pores of a small diameter equal to or larger than 6 Å and smaller than 7 Å being also contained in an amount not exceeding 20% by weight in the mixture, wherein a ferrierite-type zeolite and a pentasil-type zeolite are selected as the zeolite having the pores of the small diameter equal to or larger than 3.5 Å and smaller than 6 Å and no pore of the small diameter equal to or larger than 6 Å and smaller than 7 Å, and a faujasite-type zeolite is selected as the zeolite having the pores of the small diameter equal to or larger than 7 Å and smaller than 10 Å and no pore of the small diameter equal to or larger than 6 Å and smaller than 7 Å, and in a three-component composition diagram in which each of ratios is indicated by one point within an equilateral triangle having three apexes each indicating the case where the mixture includes only one of zeolite components, the weight ratio of the ferrierite-type, pentasil-type and faujasite-type zeolites is set to lie in a region surrounded by a line segment connecting a point of (0.1:0.18:0.72), a point of (0.4:0.16:0.44), a point of (0.55:0.2:0.25), a point of (0.55:0.25:0.2), a point of (0.4:0.43:0.17), a point of (0.1:0.7:0.2), a point of (0.02:0.58:0.4) and a point of (0.03:0.4:0.57) to one another.
Dependencies are inferred from the claim text.