KINETIC MODELING OF AMMONIA SELECTIVE CATALYTIC REDUCTION FOR CLEANING EMISSIONS FROM VEHICLES: CATALYST AGING
Ammonia Selective Catalytic Reduction (NH3-SCR) is an established technology to reduce NOx for heavy-duty vehicles. Metal exchanged zeolites, such as copper zeolites, are used for NH3-SCR. The effects of hydrothermal aging over zeolite based catalyst are recently studied. However, there are no kinet...
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Main Authors: | , |
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Format: | Theses and Dissertations NonPeerReviewed |
Published: |
[Yogyakarta] : Universitas Gadjah Mada
2013
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Subjects: | |
Online Access: | https://repository.ugm.ac.id/119377/ http://etd.ugm.ac.id/index.php?mod=penelitian_detail&sub=PenelitianDetail&act=view&typ=html&buku_id=59374 |
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Institution: | Universitas Gadjah Mada |
Summary: | Ammonia Selective Catalytic Reduction (NH3-SCR) is an established technology
to reduce NOx for heavy-duty vehicles. Metal exchanged zeolites, such as copper
zeolites, are used for NH3-SCR. The effects of hydrothermal aging over zeolite
based catalyst are recently studied. However, there are no kinetic models present
that can describe aging over copper zeolites.
This project aims to develop kinetic modeling of NH3-SCR over Cu-Beta. In a
previous master thesis work experiments for studying aging of NH3-SCR over Cu-
Beta was conducted. The main reactions that were previously examined
experimentally were ammonia storage, ammonia oxidation, NO oxidation,
standard SCR, rapid SCR, NO2 SCR and N2O formation. The results of the
experiments were then used to construct the kinetic model.
We suggest that some of the different reactions that occur in the SCR mechanism
take place on different sites. We have therefore introduced aging factors that we
multiply the pre-exponential factors with. We suggest that different sites have
different aging factors. In this way we can group the reactions after on which sites
the reactions occur. This will also result in a fast way of tuning aging models
since we only need to determine NH3 storage/desorption and the aging factors.
The results showed that the simulation approach worked well for modeling the
experimental results. For ammonia TPD the simulations are enough with only
decreasing storage capacity of ammonia and using heat of adsorption measured by
microcalorimeter. Our model can describe that the higher temperature of
hydrothermal aging gives reducing of ammonia storage at higher temperature as
well as decreased temperature for NH3 desorption. For NH3 oxidation, NO
oxidation and NH3-SCR a Cu-beta catalyst which was aged between 500oC and
800oC was described with three aging factors. Meanwhile aged catalyst at 900oC
has a particular behavior for tuning aging factors due to that the structure has
collapsed at this high temperature. In addition N2O formation occurred both at low
temperature and at high temperature and a model was developed for this. |
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