dc.contributor.author |
Tsapekis, OG |
en |
dc.contributor.author |
Salmas, CE |
en |
dc.contributor.author |
Androutsopoulos, GP |
en |
dc.date.accessioned |
2014-03-01T01:57:19Z |
|
dc.date.available |
2014-03-01T01:57:19Z |
|
dc.date.issued |
2008 |
en |
dc.identifier.issn |
1790-7632 |
en |
dc.identifier.uri |
https://dspace.lib.ntua.gr/xmlui/handle/123456789/28401 |
|
dc.subject |
hydrogen sulfide |
en |
dc.subject |
selective oxidation |
en |
dc.subject |
iron chelate |
en |
dc.subject |
absorption with chemical reaction |
en |
dc.subject |
NTA |
en |
dc.subject |
nitrilo triacetic acid |
en |
dc.subject.classification |
Environmental Sciences |
en |
dc.subject.other |
CHEMISTRY |
en |
dc.title |
CHEMICAL KINETICS OF HYDROGEN SULFIDE SELECTIVE OXIDATION IN IRON CHELATE SOLUTIONS |
en |
heal.type |
journalArticle |
en |
heal.language |
English |
en |
heal.publicationDate |
2008 |
en |
heal.abstract |
The present work concerns the investigation of the chemical kinetics of H2S selective oxidation into elemental sulfur, by gas absorption and chemical reaction in Fe3+ center dot(NTA) aqueous solutions. By using initial reactivity data, priority is given to the study of intrinsic kinetics i.e. to avoid interactions with ligand degradation and the presence of sulfur. A wetted wall gas-liquid reactor was employed under a batch-recycle regime. The conversion of Fe3+ to Fe2+ chelate was determined over the pH range ca. 3-6, temperature range ca. 30-60 degrees C and a short overall per run contact time of phases. The penetration theory was used for the evaluation of intrinsic reaction rate constant and enhancement factor. Activation energy values determined from the pertinent Arrhenius plots fall in the range, Ea=17.2- 22.8 kcal mol(-1). These values compare satisfactorily with the value Ea=24 kcal mol-1 obtained from a similar kinetic study performed in a bubble column reactor and indicates a chemical reaction control of the overall gas absorption phenomenon. Enhancement factors varied in the respective ranges E =2.7-7.5 (pH=3), E=3.2-14.1 (pH=4), E=5.9-17.0 (pH=5), Kai E=6.7-20.1 (pH=6) indicating a substantial increase of the mass transfer coefficient due to chemical reaction. For the experimental conditions applied in this study the following kinetic correlation was validated: R-H2S = {[-10.62 + 4.15 (pH)].10(14) exp (-19083/RgT)} C-H2S |
en |
heal.publisher |
GLOBAL NETWORK ENVIRONMENTAL SCIENCE & TECHNOLOGY |
en |
heal.journalName |
GLOBAL NEST JOURNAL |
en |
dc.identifier.isi |
ISI:000260710100012 |
en |
dc.identifier.volume |
10 |
en |
dc.identifier.issue |
3 |
en |
dc.identifier.spage |
386 |
en |
dc.identifier.epage |
394 |
en |