SAE Technical Paper Series 1998
DOI: 10.4271/980423
|View full text |Cite
|
Sign up to set email alerts
|

In-line Hydrocarbon Adsorber for Cold Start Emissions - Part II

Help me understand this report

Search citation statements

Order By: Relevance

Paper Sections

Select...
3
1
1

Citation Types

0
8
0

Year Published

1999
1999
2021
2021

Publication Types

Select...
6
2

Relationship

0
8

Authors

Journals

citations
Cited by 19 publications
(8 citation statements)
references
References 5 publications
0
8
0
Order By: Relevance
“…For simulations with passive adsorption, we assumed that a 0.67 l adsorber device was installed midway between the 1.1 l TWC stages, as illustrated in Figure 6. The simulated adsorber device was also assumed to have the properties of a wash-coated cordierite monolith with a cell density of 400 cells/in 2 and a void fraction of 0.7. Based on the literature values, the storage capacities of HC and NO sorbents were assumed to be 1.5 mmol/g for C 3 H 6 29 and 0.80 mmol/g for NO 15 under dry conditions.…”
Section: Vehicle Simulations With Passive Adsorption After-treatmentmentioning
confidence: 99%
See 2 more Smart Citations
“…For simulations with passive adsorption, we assumed that a 0.67 l adsorber device was installed midway between the 1.1 l TWC stages, as illustrated in Figure 6. The simulated adsorber device was also assumed to have the properties of a wash-coated cordierite monolith with a cell density of 400 cells/in 2 and a void fraction of 0.7. Based on the literature values, the storage capacities of HC and NO sorbents were assumed to be 1.5 mmol/g for C 3 H 6 29 and 0.80 mmol/g for NO 15 under dry conditions.…”
Section: Vehicle Simulations With Passive Adsorption After-treatmentmentioning
confidence: 99%
“…For current TWCs, this threshold is about 150–200 °C. 1,2 Recently, there has been considerable interest in developing catalysts that become active at lower temperatures. 35 Since a cold start always involves a delay in catalyst heat-up, there can be a significant release of carbon monoxide (CO), unburned hydrocarbons (HCs), and nitrogen oxides (NO x ) before the catalyst becomes functional.…”
Section: Introductionmentioning
confidence: 99%
See 1 more Smart Citation
“…HC-traps [8], [9], [10] represent ideal, highly efficient, means for temporarily storing HC-emissions. However they have the disadvantage -still unresolved -that hydrocarbon desorption already begins at temperatures before the catalytic light-off temperature of oxidation-type or three-way catalytic converters is reached.…”
Section: Bypass Catalystsmentioning
confidence: 99%
“…1). Among the more successful methods that have been developed for shortening the warming-up period are: heating with electrical power [4], heating with an external combustion chamber [5], installing an auxiliary small-capacity catalytic converter [6], employing an adsorber between two catalysts with [7,8] or without a secondary air source [9] and using an on-board fuel reformer [10]. Although these methods are quite effective, their disadvantage is that they require an external energy source, a control unit or a three-stage catalyst.…”
Section: Introductionmentioning
confidence: 99%