2022
DOI: 10.3390/molecules27196527
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Catalytic Deoxygenation of Hydrolyzed Oil of Chlorella Vulgaris Microalgae over Lanthanum-Embedded HZSM-5 Zeolite Catalyst to Produce Bio-Fuels

Abstract: Microalgae is one of the most important sources of green hydrocarbons because it contains a high percentage of lipids and is likely to reduce reliance on fossil fuels. Several zeolite-based catalysts have a short lifetime due to coke-formation deactivation. In this study, a lanthanum-modified HZSM-5 zeolite catalyst for the conversion of crude oil into non-oxygenated compounds (hydrocarbons) and oxygenated compounds has been investigated. The crude oil of Chlorella Vulgaris microalgae was extracted using Soxhl… Show more

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Cited by 4 publications
(3 citation statements)
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“…Increasing the metal doping ratio of lanthanum and samarium deformed the crystallinity of H-ZSM5, resulting in a decrease in the peak intensity. 22 The shape of the graph is similar to that of H-ZSM5, indicating that the ratio of metal doping is small.…”
Section: Catalyst Characteristicsmentioning
confidence: 69%
See 1 more Smart Citation
“…Increasing the metal doping ratio of lanthanum and samarium deformed the crystallinity of H-ZSM5, resulting in a decrease in the peak intensity. 22 The shape of the graph is similar to that of H-ZSM5, indicating that the ratio of metal doping is small.…”
Section: Catalyst Characteristicsmentioning
confidence: 69%
“…In the cerium regenerative zeolite, new peaks can be found at 28, 38, 48, and 55°, which are in accordance with peaks indicating the coupling of CeO 2 . , On the other hand, in the case of the zeolite modified with lanthanum and samarium, there is no new peak. Increasing the metal doping ratio of lanthanum and samarium deformed the crystallinity of H-ZSM5, resulting in a decrease in the peak intensity . The shape of the graph is similar to that of H-ZSM5, indicating that the ratio of metal doping is small.…”
Section: Resultsmentioning
confidence: 85%
“…Before the current investigation, we published two different studies that explored in detail the catalytic deoxygenation process for the algal HO under identical operating conditions (batch reactor, 300 • C, 1000 rpm, 7 bar of N 2 inert gas (initial pressure), catalystto-algal HO ratio = 15% (wt.%), and 6 h). The first study focused on loading Lanthanum on the parent HZSM-5 zeolite at various loading weight percentages (5%La/HZSM-5, 10%La/HZSM-5, and 15%La/HZSM-5) [49], while the second focused on loading Cerium at various loading weight percentages (5%Ce/HZSM-5, 10%Ce/HZSM-5, and 15%Ce/HZSM-5) [50].…”
Section: Introductionmentioning
confidence: 99%