dc.contributor.author |
Naik, S.P. |
|
dc.contributor.author |
Fernandes, J.B. |
|
dc.date.accessioned |
2015-06-03T07:29:22Z |
|
dc.date.available |
2015-06-03T07:29:22Z |
|
dc.date.issued |
2001 |
|
dc.identifier.citation |
Applied Catalysis A-General. 205(1and2); 2001; 195-199. |
en_US |
dc.identifier.uri |
http://dx.doi.org/10.1016/S0926-860X(00)00555-X |
|
dc.identifier.uri |
http://irgu.unigoa.ac.in/drs/handle/unigoa/1245 |
|
dc.description.abstract |
Reaction between ethanol and ammonia have been studied on various zinc oxide modified HZSM-5 (Si/Al=225) catalysts under various conditions of temperature, C/N ratio of the reactants and their WHSV. Two pure zinc oxides were taken for the study.One was a highly active acidic form ZI and the other was a stoichiometric non acidic zinc oxide Z(2). The activity of the catalysts for ammonolysis reaction followed the order Z(2)much less thanZ(1)much less than HZSM-5. However, for composite catalysts containing 10-40 percent Z(1) on HZSM-5, the activity increased synergistically and became maximum (similar to 81 percent conversion of alcohol) for the catalyst 40 percent Z(1)/HZSM-5 and about 50 percent conversion for the catalyst 40 percent Z(2)/HZSM-5. The products formed were mainly N-heterocycles.Some novel high molar mass N-heterocycles were also detected. The catalytic activity and product selectivity was crucially affected by the reaction conditions, particularly the effect of temperature; the optimum yield of the products was obtained at the catalyst temperature of 723 K. C/N ratio 0.3892 and WHSV of 2.5 h(-1). |
en_US |
dc.publisher |
Elsevier |
en_US |
dc.subject |
Chemistry |
en_US |
dc.title |
Ammonolysis of ethanol on pure and zinc oxide modified HZSM-5 zeolites |
en_US |
dc.type |
Journal article |
en_US |
dc.identifier.impf |
y |
|