Hilde J. Venvik

Prof. Hilde J. Venvik


Research Focus & Metrics

Academic Career Length

14Years (2013-Present)

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

Representative Publications

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1 July 2014 in Applied Catalysis A: General
Verified
Journal Article
Closed access
AMAndrea Montebelli
Andrea Montebelli
CVCarlo Giorgio Visconti
Carlo Giorgio Visconti
GGGianpiero Groppi
Gianpiero Groppi
ETEnrico Tronconi
Enrico Tronconi
SKStefanie Kohler
Stefanie Kohler
RMRune Myrstad
Rune Myrstad

1 February 2020 in Catalysis Today
Verified
Journal Article
Closed access
CWC.J. Weststrate
C.J. Weststrate
Mehdi MahmoodiniaMehdi Mahmoodinia
Mehdi Mahmoodinia
MFMari Helene Farstad
Mari Helene Farstad
ISIngeborg-Helene Svenum
Ingeborg-Helene Svenum
MSMarie D. Strømsheim
Marie D. Strømsheim
HVHilde J. Venvik
Hilde J. Venvik

20 February 2017 in Catalysis Letters
Verified
Journal Article
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FDFarbod Dadgar
Farbod Dadgar
RMRune Myrstad
Rune Myrstad
PPPeter Pfeifer
Peter Pfeifer
AHAnders Holmen
Anders Holmen
HVHilde J. Venvik
Hilde J. Venvik

10 October 2018 in Membranes
Verified
Journal Article
Open access
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NVNicla Vicinanza
Nicla Vicinanza
ISIngeborg-Helene Svenum
Ingeborg-Helene Svenum
Thijs PetersThijs Peters
Thijs Peters
RBRune Bredesen
Rune Bredesen
HVHilde J. Venvik
Hilde J. Venvik
Sputtered Pd77%Ag23% membranes of thickness 2.2–8.5 µm were subjected to a three-step heat treatment in air (HTA) to investigate the relation between thickness and the reported beneficial effects of HTA on hydrogen transport. The permeability experiments were complimented by volumetric hydrogen sorption measurements and atomic force microscopy (AFM) imaging in order to relate the observed effects to changes in hydrogen solubility and/or structure. The results show that the HTA—essentially an oxidation-reduction cycle—mainly affects the thinner membranes, with the hydrogen flux increasing stepwise upon HTA of each membrane side. The hydrogen solubility is found to remain constant upon HTA, and the change must therefore be attributed to improved transport kinetics. The HTA procedure appears to shift the transition from the surface to bulk-limited transport to lower thickness, roughly from ~5 to ≤2.2 µm under the conditions applied here. Although the surface topography results indicate that HTA influences the surface roughness and increases the effective membrane surface area, this cannot be the sole explanation for the observed hydrogen flux increase. This is because considerable surface roughening occurs during hydrogen permeation (no HTA) as well, but not accompanied by the same hydrogen flux enhancement. The latter effect is particularly pronounced for thinner membranes, implying that the structural changes may be dependent on the magnitude of the hydrogen flux.

1 March 2020 in Catalysis Today
Verified
Journal Article
Closed access
HBHamidreza Bakhtiary-Davijany
Hamidreza Bakhtiary-Davijany
FHFatemeh Hayer
Fatemeh Hayer
XPXuyen Kim Phan
Xuyen Kim Phan
RMRune Myrstad
Rune Myrstad
HVHilde J. Venvik
Hilde J. Venvik
AHAnders Holmen
Anders Holmen

2 March 2020 in Topics in Catalysis
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Journal Article
Open access
PDF file
ISIngeborg-Helene Svenum
Ingeborg-Helene Svenum
JHJeffrey A. Herron
Jeffrey A. Herron
MMManos Mavrikakis
Manos Mavrikakis
HVHilde J. Venvik
Hilde J. Venvik
The co-adsorption of hydrogen and carbon monoxide on Pd3Ag(111) alloy surfaces has been studied as a model system for Pd-Ag alloys in membrane and catalysis applications using periodic density functional theory calculations (PW91-GGA). We explored the effects of Pd–Ag surface composition, since segregation of silver towards and away from the surface has been suggested to explain the experimentally observed changes in H2activation, CO inhibition and reactivity. We found that CO pre-adsorbed on the surface weakens the adsorption of H on Pd3Ag(111) alloy surfaces irrespective of whether the surface termination corresponds to the bulk Pd3Ag composition, or is purely Pd-terminated. A higher coverage of H with CO present is obtained for the Pd-terminated surface; this surface also exhibits a larger range of chemical potentials for co-adsorbed hydrogen and CO. The barrier for H2activation increases with increasing CO coverage, but the surface composition has the largest impact on H2activation at intermediate CO coverage. The results imply that Pd-based membranes with typically ~ 23 wt% Ag are less prone to CO poisoning if the surface becomes Pd-terminated.