| 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 |