Natasa Novak Tusar

Prof. Natasa Novak Tusar

National Institute of Chemistry

Research Focus & Metrics

Academic Career Length

20Years (2007-Present)

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

Representative Publications

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1 May 2016 in Applied Catalysis B: Environment and Energy
Verified
Journal Article
Closed access
Andraž ŠuligojAndraž Šuligoj
Andraž Šuligoj
UŠUrška Lavrenčič Štangar
Urška Lavrenčič Štangar
ARAlenka Ristić
Alenka Ristić
MMMatjaž Mazaj
Matjaž Mazaj
DVDejan Verhovšek
Dejan Verhovšek
Natasa Novak TusarNatasa Novak Tusar
Natasa Novak Tusar

1 July 2020 in Applied Catalysis B: Environment and Energy
Verified
Journal Article
Closed access
PDPetar Djinović
Petar Djinović
ARAlenka Ristić
Alenka Ristić
TŽTadej Žumbar
Tadej Žumbar
Venkata D. B. C. DasireddyVenkata D. B. C. Dasireddy
Venkata D. B. C. Dasireddy
MRMojca Rangus
Mojca Rangus
Natasa Novak TusarNatasa Novak Tusar
Natasa Novak Tusar

9 April 2018 in Journal of Materials Chemistry A
Verified
Journal Article
Open access
PDF file
Andraž ŠuligojAndraž Šuligoj
Andraž Šuligoj
IAIztok Arcon
Iztok Arcon
MMMatjaž Mazaj
Matjaž Mazaj
Goran DrazicGoran Drazic
Goran Drazic
DADenis Arčon
Denis Arčon
Natasa Novak TusarNatasa Novak Tusar
Natasa Novak Tusar
Ni and Zn show a winning combination of redox potential and band positions of TiO 2 supported metal-oxo-nanoclusters for enhanced solar-light activity. However, Ni is the only metal which has a positive effect on solar photoactivity in both oxidation and reduction reactions.

30 August 2018 in Topics in Catalysis
Verified
Journal Article
Closed access
PDF file
MOManuel Ojeda
Manuel Ojeda
NONika Osterman
Nika Osterman
Goran DrazicGoran Drazic
Goran Drazic
LŽLjudmila Fele Žilnik
Ljudmila Fele Žilnik
AMAnton Meden
Anton Meden
Natasa Novak TusarNatasa Novak Tusar
Natasa Novak Tusar

1 December 2020 in Catalysis Today
Verified
Journal Article
Closed access
Andraž ŠuligojAndraž Šuligoj
Andraž Šuligoj
ARAlenka Ristić
Alenka Ristić
GDGoran Dražić
Goran Dražić
APAlbin Pintar
Albin Pintar
NLNataša Zabukovec Logar
Nataša Zabukovec Logar
Natasa Novak TusarNatasa Novak Tusar
Natasa Novak Tusar

17 July 2018 in Frontiers in Chemistry
Verified
Journal Article
Open access
PDF file
MPMargarita Popova
Margarita Popova
PDPetar Djinović
Petar Djinović
ARAlenka Ristić
Alenka Ristić
Hristina LazarovaHristina Lazarova
Hristina Lazarova
Goran DrazicGoran Drazic
Goran Drazic
Natasa Novak TusarNatasa Novak Tusar
Natasa Novak Tusar
The hydrogenation of levulinic acid (LA) to γ-valerolactone (GVL) in vapor-phase is economically more viable route if compared to reaction in liquid-phase. To improve the GVL yield in the vapor-phase reaction, the optimization of nickel modified zeolite as bi-functional catalyst (Ni/HZSM-5) was studied. Ni/HZSM-5 materials with fixed Al/Si molar ratio of 0.04 and different nominal Ni/Si molar ratios (from 0.01 to 0.05) were synthesized without the use of organic template and with the most affordable sources of silica and alumina. Materials were characterized by X-ray powder diffraction, SEM-EDX, TEM-EDX, pyridine TPD and DRIFTS, H2-TPR, N2 physisorption and isoelectric point. In the synthesized materials, 61–83% of nickel is present as bulk NiO and increases with nickel content. Additionally, in all catalysts, a small fraction of Ni2+ which strongly interacts with the zeolite support was detected (10–18%), as well as Ni2+ acting as charge compensating cations for Brønsted acid sites (7–21%). Increasing the nickel content in the catalysts leads to a progressive decrease of Brønsted acid sites (BAS) and concomitant increase of Lewis acid sites (LAS). When BAS/LAS is approaching to 1 and at the same time the amount of NiO reducible active sites is around 80%, the bi-functional Ni/HZSM-5-3 catalyst (Ni/Al = 0.59) leads to 99% conversion of LA and 100% selectivity to GVL at 320°C. This catalyst also shows stable levulinic acid hydrogenation to GVL in 3 reaction cycles conducted at 320°C. The concerted action of the following active sites in the catalyst is a key element for its optimized performance: (1) Ni metallic active sites with hydrogenation effect, (2) Lewis acid sites with dehydration effect, and (3) nickel aluminate sites with synergetic and stabilizing effects of all active sites in the catalyst.