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dc.contributor.authorIlhan, Sedat
dc.date.accessioned2021-03-04T14:24:38Z
dc.date.available2021-03-04T14:24:38Z
dc.identifier.citationIlhan S., "Leaching of Spent Ni-Mo Hydrodesulphurization (HDS) Catalyst in Oxalic Acid Solutions", 3rd Pan American Materials Congress (PAMC), California, Amerika Birleşik Devletleri, 26 Şubat - 02 Mart 2017, ss.557-564
dc.identifier.otherav_81601822-6400-46c4-a21e-d88337239014
dc.identifier.othervv_1032021
dc.identifier.urihttp://hdl.handle.net/20.500.12627/88187
dc.identifier.urihttps://doi.org/10.1007/978-3-319-52132-9_56
dc.description.abstractIn this work, the effect of crushing, temperature, oxalic acid concentration and stirring speed on the leaching of spent Ni-Mo HDS catalyst was investigated. Spent Ni-Mo HDS catalyst was roasted at 500 degrees C under dynamic air atmosphere for 4 h prior to leaching experiments. It was found that roasted spent Ni-Mo HDS catalyst included mainly Al2O3, MoO3, NiMoO4 and AlPO4. Leaching experiments were performed using 5 g of uncrushed roasted Ni-Mo HDS catalyst, 1 L of 0.25, 0.50, 0.75 and 1 M H2C2O4 solutions, 25, 40, 55 and 70 degrees C temperatures and 200, 250 and 300 rpm stirring speeds. Leaching behavior of Mo, Al, P and Ni was determined. It is seen that H2C2O4 can be used successfully for the leaching of roasted HDS catalyst. More than 90% of the molybdenum and 80% of Nickel is extracted from the experiments carried out using 300 rpm stirring speed, 1 M H2C2O4 and 40 degrees C.
dc.language.isoeng
dc.subjectMalzeme Bilimi
dc.subjectMühendislik, Bilişim ve Teknoloji (ENG)
dc.subjectMALZEME BİLİMİ, BİYOMATERYAL
dc.subjectMühendislik ve Teknoloji
dc.subjectMALZEME BİLİMİ, MULTIDISCIPLINARY
dc.titleLeaching of Spent Ni-Mo Hydrodesulphurization (HDS) Catalyst in Oxalic Acid Solutions
dc.typeBildiri
dc.contributor.departmentİstanbul Üniversitesi , Mühendislik Fakültesi , Metalurji Ve Malzeme Mühendisliği
dc.contributor.firstauthorID150540


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