István Lázár

Dr. István Lázár

Debreceni Egyetem, Department of Inorganic and Analytical Chemistry, University of Debrecen, 4032 Debrecen, Hungary
orcid

Research Focus & Metrics

Academic Career Length

39Years (1988-Present)

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

Representative Publications

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1 August 1994 in Inorganic Chemistry
Verified
Journal Article
Closed access
ÉTÉva Tóth
Éva Tóth
EBErno Brucher
Erno Brucher
ILIstván Lázár
István Lázár
ITImre Toth
Imre Toth

1 April 2017 in Colloids and Surfaces B: Biointerfaces
Verified
Journal Article
Closed access
PVPéter Veres
Péter Veres
MKMónika Kéri
Mónika Kéri
IBIstván Bányai
István Bányai
ILIstván Lázár
István Lázár
IFIstván Fábián
István Fábián
József KalmárJózsef Kalmár
József Kalmár

1 July 1992 in Journal of Magnetic Resonance Imaging
Verified
Journal Article
Closed access
PDF file
NBNavin Bansal
Navin Bansal
MGMartha J. Germann
Martha J. Germann
ILIstván Lázár
István Lázár
CMCraig R. Malloy
Craig R. Malloy
ASA. Dean Sherry
A. Dean Sherry

1 December 2015 in International Journal of Pharmaceutics
Verified
Journal Article
Closed access
PVPeter Veres
Peter Veres
ALAna M. Lopez-Periago
Ana M. Lopez-Periago
ILIstván Lázár
István Lázár
Javier SaurinaJavier Saurina
Javier Saurina
CDConcepción Domingo
Concepción Domingo

1 April 2002 in Journal of Chromatography A
Verified
Journal Article
Closed access
TITı́mea Iványi
Tı́mea Iványi
YHYvan Vander Heyden
Yvan Vander Heyden
DVDóra Visky
Dóra Visky
PBPeggy Baten
Peggy Baten
JBJacques De Beer
Jacques De Beer
JHJos Hoogmartens
Jos Hoogmartens

1 October 2016 in Gels
Verified
Journal Article
Open access
PDF file
ILIstván Lázár
István Lázár
IFIstván Fábián
István Fábián
Production of aerogels starts with solution chemistry and may end with supercritical carbon dioxide drying, which both require a specialized system. Here we present a complete aerogel production system that was developed and used in our laboratory over the last nine years. Our aim was to develop a supercritical dryer and a protocol, whereby the CO2 pump can be left out, and the entire flow system is operated by the pressure of the CO2 cylinder. Drying pressure and temperature are controlled by the combination of the filling and heating temperatures. A continuous-mode solvent exchange system has also been developed, in which the solvent consumption during the process can be reduced to one-third of the batch method. In the new medium temperature 1.5 L volume supercritical dryer, the temperature is set to a constant 80–82 °C, and the pressure can be in the 90–200 bar range, depending on the conditions. We have performed approximately 200 dryings thus far, and prepared a wide range of monolithic aerogels, from pristine silica aerogels to polysaccharides and collagen. In this paper, we have summarized not only the technical details, but also the work experiences, as well as advantages and disadvantages of the systems.