https://ogma.newcastle.edu.au/vital/access/ /manager/Index ${session.getAttribute("locale")} 5 Insights into the dissolution kinetics of thermally activated serpentine for CO₂ sequestration https://ogma.newcastle.edu.au/vital/access/ /manager/Repository/uon:34070 Wed 06 Feb 2019 09:51:32 AEDT ]]> Experimental study on the precipitation of magnesite from thermally activated serpentine for CO₂ sequestration https://ogma.newcastle.edu.au/vital/access/ /manager/Repository/uon:25541 Wed 04 Sep 2019 10:18:36 AEST ]]> The effect of catalyst modification on the conversion of glycerol to allyl alcohol https://ogma.newcastle.edu.au/vital/access/ /manager/Repository/uon:21066 Sat 24 Mar 2018 07:59:25 AEDT ]]> A promoter effect on hydrodeoxygenation reactions of oleic acid by zeolite beta catalysts https://ogma.newcastle.edu.au/vital/access/ /manager/Repository/uon:45517 (10)zeo(90), Co(10)zeo(90), Fe(10)zeo(90), Mg(10)zeo(90), Mn(10)zeo(90) and Zn(10)zeo(90) were investigated in the hydrodeoxygenation (HDO) of oleic acid (OA) to produce renewable diesel. The La(10)zeo(90) catalyst showed a conversion of OA up to 99 % with 83 % C15 and C17 selectivity after the reaction at 350 °C for 2 h under 4 MPa H2 pressure. The superior activity of La(10)zeo(90) was attributed to the synergistic interaction between La-Si-Al, a sufficient amount of weak + medium acid sites and excellent textural properties (large pore diameter). Larger pore diameter of La(10)zeo(90) is highly desirable as it will generate greater diffusion of bulky molecules, thereby improving the accessibility of the reactant and hence excellent catalytic activity. The vacuum distillation was used to purify the crude liquid product (CLP), producing high-quality diesel fractions mainly comprising C14, C15, and C17 fractions.]]> Mon 29 Jan 2024 18:39:08 AEDT ]]> Hydrodeoxygenation of fatty acid over La-modified HZSM5 for premium quality renewable diesel production https://ogma.newcastle.edu.au/vital/access/ /manager/Repository/uon:47359 Mon 29 Jan 2024 18:35:13 AEDT ]]> Effect of various operating parameters on the oxidative coupling of methane over Na₂WO₄Mn/SiO₂ catalyst with N₂O as an oxidant https://ogma.newcastle.edu.au/vital/access/ /manager/Repository/uon:18678 Mon 20 Jul 2015 17:34:23 AEST ]]>