Carboxylase applied on carbon materials as an oxygen electrode of fuel elements
Închide
Articolul precedent
Articolul urmator
612 2
Ultima descărcare din IBN:
2019-09-04 15:07
Căutarea după subiecte
similare conform CZU
544+577.1+66 (1)
Chimie fizică (500)
Bazele materiale ale vieții. Biochimie. Biologie moleculară. Biofizică (671)
Tehnologie chimică. Industrii chimice și înrudite (1520)
SM ISO690:2012
SOFRONKOV, Aleksandr, ZHUK, O., VASILIEVA, M.. Carboxylase applied on carbon materials as an oxygen electrode of fuel elements. In: Materials Science and Condensed Matter Physics, Ed. 9, 25-28 septembrie 2018, Chișinău. Chișinău, Republica Moldova: Institutul de Fizică Aplicată, 2018, Ediția 9, p. 239.
EXPORT metadate:
Google Scholar
Crossref
CERIF

DataCite
Dublin Core
Materials Science and Condensed Matter Physics
Ediția 9, 2018
Conferința "International Conference on Materials Science and Condensed Matter Physics"
9, Chișinău, Moldova, 25-28 septembrie 2018

Carboxylase applied on carbon materials as an oxygen electrode of fuel elements

CZU: 544+577.1+66

Pag. 239-239

Sofronkov Aleksandr1, Zhuk O.2, Vasilieva M.1
 
1 Odessa State Environmental University,
2 University of Opole
 
 
Disponibil în IBN: 10 februarie 2019


Rezumat

Recently, much attention has been paid to the study of biocatalysts. It is connected with the possibility of their use under mild conditions: рН~7; Т=(293 +\- 5) К. In addition, they have a unique specificity.  We investigated carboxylase applied on carbon carriers: coals - AG-2, CAD, BAU, nanotubes. The study was carried out in a conventional electrochemical cell at the Sistem-5000 potentiostat which simultaneously measured the kinetics of decomposition of H2O2 and monitored the potential. The catalyst charge was constant 50 mg in all the experiments.  As it is known, the decomposition of Н2О2 can occur by an ionic or radical mechanism [1]. The results obtained showed that decomposition of Н2О2 can not occur on the researched catalysts (carboxylase-carbon carrier) by ionic mechanism, since in this case the initial stage would be one of the following reactions:  К [H2O] адс. + Н2О2 → К [ Н3О+]адс.+ [НО2- ] ;  НО2- + Н2О2 → H2O + О2+ ОН- ;  К [ Н3О+]адс+ ОН- → К [H2O] адс + H2O ;  Н2О2+ ОН- → H2O + НО2- ;  Since the heats of formation of Н2О and Н3О+ are the same [2], an activation energy of ~ 28.6 kJ/mol is needed for the course of this reaction. It differs significantly from the value of the activation energy of Н2О2 catalytic decomposition on the researched catalysts. Therefore, radical mechanism of Н2О2 decomposition should be applied.