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dc.contributor.author서영웅-
dc.date.accessioned2019-11-26T20:50:34Z-
dc.date.available2019-11-26T20:50:34Z-
dc.date.issued2017-07-
dc.identifier.citationRSC ADVANCES, v. 7, no. 56, page. 35346-35356en_US
dc.identifier.issn2046-2069-
dc.identifier.urihttps://pubs.rsc.org/en/content/articlelanding/2017/RA/C7RA05558G#!divAbstract-
dc.identifier.urihttps://repository.hanyang.ac.kr/handle/20.500.11754/114847-
dc.description.abstractThe effect of the support in the simultaneous hydrogenation of acetophenone and dehydrogenation of 1,4-butanediol was studied using supported (MgO, gamma-Al2O3, MgO-Al2O3 and SiO2) copper (10 wt%) catalysts, prepared via impregnation. In this process, acetophenone was transformed to 1-phenylethanol/ethylbenzene and 1,4-butanediol converted to gamma-butyrolactone/tetrahydrofuran under a hydrogen-free environment, indicating the major role of the supports. The Cu/MgO catalyst was active and highly selective towards the production of 1-phenylethanol and gamma-butyrolactone. However, an adverse behaviour was observed over Cu/MgO-Al2O3. An extraordinary catalytic performance was obtained over Cu/SiO2 with high selectivity for ethylbenzene (99%) and gamma-butyrolactone (99%). Contrarily, no hydrogenation of acetophenone was observed over Cu/g-Al2O3 due to the dehydration of 1,4-butanediol, yielding tetrahydrofuran. The main advantage of this process is that no external hydrogen is required for the hydrogenation of acetophenone. Copper dispersion, the reduction behaviour of copper, copper particle size and the acidity and basicity of the catalysts play important roles in the activity. All four catalysts were characterized using BET surface area, N2O pulse chemisorption, XRD, XRF, H-2-TPR, XPS, and TPD of NH3/CO2 to understand our results.en_US
dc.description.sponsorshipAuthors are gratefully thanks to CSIR-UGC (INDIA) for the financial support. This research was also financially supported by Basic Science Research Program through the National Research Foundation of Korea (NRF) funded by the Ministry of Education (NRF-2016R1A6A1A03013422) and New & Renewable Energy Core Technology Program of the Korea Institute of Energy Technology Evaluation and Planning (KETEP), granted financial resource from the Ministry of Trade, Industry & Energy, Republic of Korea (No. 20143030091040).en_US
dc.language.isoen_USen_US
dc.publisherROYAL SOC CHEMISTRYen_US
dc.subjectLIQUID-PHASE HYDROGENATIONen_US
dc.subjectRANEY-NICKEL CATALYSTSen_US
dc.subjectSELECTIVE HYDROGENATIONen_US
dc.subjectCU/MGO CATALYSTSen_US
dc.subjectMALEIC-ANHYDRIDEen_US
dc.subjectOXIDE CATALYSTSen_US
dc.subjectZRO2 CATALYSTen_US
dc.subjectCYCLOHEXANONEen_US
dc.subjectETHYLBENZENEen_US
dc.subjectNITROBENZENEen_US
dc.titleOne-pot synthesis of ethylbenzene/1-phenylethanol and gamma-butyrolactone from simultaneous acetophenone hydrogenation and 1,4-butanediol dehydrogenation over copper based catalysts: effects of the supporten_US
dc.typeArticleen_US
dc.relation.no56-
dc.relation.volume7-
dc.identifier.doi10.1039/c7ra05558g-
dc.relation.page35346-35356-
dc.relation.journalRSC ADVANCES-
dc.contributor.googleauthorKannapu, Hari Prasad Reddy-
dc.contributor.googleauthorSuh, Young-Woong-
dc.contributor.googleauthorNarani, Anand-
dc.contributor.googleauthorVaddeboina, Veeralakshmi-
dc.contributor.googleauthorBurri, David Raju-
dc.contributor.googleauthorSeetha, Rama Rao Kamaraju-
dc.relation.code2017009490-
dc.sector.campusS-
dc.sector.daehakCOLLEGE OF ENGINEERING[S]-
dc.sector.departmentDEPARTMENT OF CHEMICAL ENGINEERING-
dc.identifier.pidywsuh-
dc.identifier.orcidhttp://orcid.org/0000-0002-2094-0724-


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