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dc.contributor.author | Nazarov M. | |
dc.contributor.author | Laskin A. | |
dc.contributor.author | Ilyasov I. | |
dc.contributor.author | Lamberov A. | |
dc.contributor.author | Bikmurzin A. | |
dc.contributor.author | Shatilov V. | |
dc.date.accessioned | 2018-09-18T20:48:02Z | |
dc.date.available | 2018-09-18T20:48:02Z | |
dc.date.issued | 2013 | |
dc.identifier.issn | 2070-0504 | |
dc.identifier.uri | https://dspace.kpfu.ru/xmlui/handle/net/142293 | |
dc.description.abstract | Pilot tests of SGA-2M promoted Pd/Al2O3 catalyst in the selective hydrogenation of acetylene are performed on an industrial ethane-ethylene fraction in a system of two serially arranged adiabatic flow reactors. The optimum process conditions under which the conversion of acetylene reaches 100% at a selectivity of 68.2% with respect to ethylene are determined: system pressure, 21 atm; hydrocarbon feedstock hourly space velocity (HSV), 1500 h-1, carbon monoxide concentration, 7 ppm; H2: C 2H2 molar ratio at the first and second hydrogenation stages, 1.0: 1.0 and 1.4: 1.0; inlet temperature of the first and second reactors, 40 and 55 C, respectively. The interregeneration service life of the SGA-2M catalyst under optimum conditions is estimated at 12 months. SGA-2M catalysts can be recommended for purifying ethane-ethylene fractions containing up to 2 vol % of acetylene. © 2013 Pleiades Publishing, Ltd. | |
dc.relation.ispartofseries | Catalysis in Industry | |
dc.subject | alumopalladium catalyst | |
dc.subject | selective hydrogenation of acetylene | |
dc.title | Pilot tests of a catalyst for the selective hydrogenation of acetylene | |
dc.type | Article | |
dc.relation.ispartofseries-issue | 2 | |
dc.relation.ispartofseries-volume | 5 | |
dc.collection | Публикации сотрудников КФУ | |
dc.relation.startpage | 143 | |
dc.source.id | SCOPUS20700504-2013-5-2-SID84881340525 |