Mika Suvanto

Prof. Mika Suvanto

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Research Focus & Metrics

Academic Career Length

19Years (2008-Present)

(Calculated once Scilit publication data is synced: current year − year of first publication + 1)

Representative Publications

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1 August 2009 in Applied Surface Science
Verified
Journal Article
Closed access
ISInka Saarikoski
Inka Saarikoski
MSMika Suvanto
Mika Suvanto
TPTapani A. Pakkanen
Tapani A. Pakkanen

27 February 2018 in ChemCatChem
Verified
Journal Article
Open access
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NKNiko Kinnunen
Niko Kinnunen
MKMatthew Keenan
Matthew Keenan
KKKauko Kallinen
Kauko Kallinen
TMTeuvo Maunula
Teuvo Maunula
MSMika Suvanto
Mika Suvanto
Catalytic combustion of methane, the main component of natural gas, is a challenge under lean‐burn conditions and at low temperatures owing to sulfur poisoning of the Pd‐rich catalyst. This paper introduces a more sulfur‐resistant catalyst system that can be regenerated during operation. The developed catalyst system lowers the barrier that has restrained the use of liquefied natural gas as a fuel in energy production.

1 July 2008 in Thin Solid Films
Verified
Journal Article
Closed access
VMVille Miikkulainen
Ville Miikkulainen
MSMika Suvanto
Mika Suvanto
TPTapani A. Pakkanen
Tapani A. Pakkanen

8 May 2019 in Catalysts
Verified
Journal Article
Open access
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NKNiko Kinnunen
Niko Kinnunen
VNVille H. Nissinen
Ville H. Nissinen
JHJanne Hirvi
Janne Hirvi
KKKauko Kallinen
Kauko Kallinen
TMTeuvo Maunula
Teuvo Maunula
MSMika Suvanto
Mika Suvanto
Exhaust gas aftertreatment systems play a key role in controlling transportation greenhouse gas emissions. Modern aftertreatment systems, often based on Pd metal supported on aluminum oxide, provide high catalytic activity but are vulnerable to sulfur poisoning due to formation of inactive sulfate species. This paper focuses on regeneration of Pd-based catalyst via the decomposition of alumina-supported aluminum and palladium sulfates existing both individually and in combination. Decomposition experiments were carried out under hydrogen (10% H2/Ar), helium (He), low oxygen (0.1% O2/He), and excess oxygen (10% O2/He). The structure and composition of the model catalysts were examined before and after the decomposition reactions via powder X-ray diffraction and elemental sulfur analysis. The study revealed that individual alumina-supported aluminum sulfate decomposed at a higher temperature compared to individual alumina-supported palladium sulfate. The simultaneous presence of aluminum and palladium sulfates on the alumina support decreased their decomposition temperatures and led to a higher amount of metallic palladium than in the corresponding case of individual supported palladium sulfate. From a fundamental point of view, the lowest decomposition temperature was achieved in the presence of hydrogen gas, which is the optimal decomposition atmosphere among the studied conditions. In summary, aluminum sulfate has a two-fold role in the regeneration of a catalyst—it decreases the Pd sulfate decomposition temperature and hinders re-oxidation of less-active metallic palladium to active palladium oxide.

9 August 2021 in Coatings
Verified
Journal Article
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MKMatti Kultamaa
Matti Kultamaa
KMKari Mönkkönen
Kari Mönkkönen
JSJarkko J. Saarinen
Jarkko J. Saarinen
MSMika Suvanto
Mika Suvanto
Zinc electroplating was used to enhance corrosion resistance of porous metal injection molded 440C stainless steel. Controlled porosity was achieved by the powder space holder technique and by using sodium chloride as a space holder material. The internal pore structure of porous 440C was deposited by zinc using electroplating with three different electrolytes of zinc acetate, zinc sulfate, and zinc chloride. Our results show that all zinc depositions on porous 440C samples significantly improved corrosion resistance. The lowest corrosion was observed with zinc acetate at 30 wt.% porosity. The developed zinc coated porous 440C samples have potential in applications in corrosive environments.

1 April 2012 in Surface and Coatings Technology
Verified
Journal Article
Closed access
Alina A. ManshinaAlina A. Manshina
Alina A. Manshina
APAlexey V. Povolotskiy
Alexey V. Povolotskiy
APAnastasia Povolotckaia
Anastasia Povolotckaia
TITatiana Yu. Ivanova
Tatiana Yu. Ivanova
IKIgor O. Koshevoy
Igor O. Koshevoy
TPTapani A. Pakkanen
Tapani A. Pakkanen