The catalytic deoxygenation reaction temperature and N2 gas flow rate influence the conversion of soybean fatty acids into Green Diesel
Background: Green diesel is a promising alternative as a petroleum replacement given the worldwide demand for petroleum fuel. Environmental issues have drawn public attention and concerns towards advancing renewable energy development. A catalytic deoxygenation (deCOx) was carried out to produce gre...
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| Format: | Article |
| Language: | English |
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Taiwan Institute of Chemical Engineers
2024
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| Online Access: | http://psasir.upm.edu.my/id/eprint/113728/1/113728.pdf |
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| author | Hafriz, R.S.R.M. Habib, S.H. Raof, N.A. Razali, S.Z. Yunus, R. Razali, N.M. Salmiaton, A. |
| author_facet | Hafriz, R.S.R.M. Habib, S.H. Raof, N.A. Razali, S.Z. Yunus, R. Razali, N.M. Salmiaton, A. |
| author_sort | Hafriz, R.S.R.M. |
| collection | UPM |
| description | Background: Green diesel is a promising alternative as a petroleum replacement given the worldwide demand for petroleum fuel. Environmental issues have drawn public attention and concerns towards advancing renewable energy development. A catalytic deoxygenation (deCOx) was carried out to produce green diesel from soybean oil (SO) using a low-cost NiO-doped calcined dolomite (NiO[sbnd]CD) catalyst. Method: The structure, chemical composition and morphology of NiO[sbnd]CD were comprehensively characterized by XRF, BET, TPD-CO2, SEM and TEM. In this study, the effect of two operating parameters, reaction temperature and flow rate of nitrogen, was discovered using a one-factor-at-a-time (OFAT) optimisation study. In addition, the life cycle cost analysis (LCCA) of stepwise catalyst preparation and green diesel production has been performed. Significant findings: An optimal reaction temperature of 420 °C was found to provide the highest yield of green diesel (47.13 wt.%) with an 83.51% hydrocarbon composition. The ideal nitrogen flow rate, however, was found to be 50 cm3/min, which produced 41.80 wt.% of green diesel with an 88.63% hydrocarbon composition. The deoxygenation reaction was significantly impacted by both reaction temperature and nitrogen flow rate. According to LCCA, NiO[sbnd]CD catalyst has potential to lower the overall cost of producing green diesel compared to commercial zeolite catalysts. © 2024 |
| first_indexed | 2025-02-19T02:48:51Z |
| format | Article |
| id | upm.eprints-113728 |
| institution | Universiti Putra Malaysia |
| language | English |
| last_indexed | 2025-02-19T02:48:51Z |
| publishDate | 2024 |
| publisher | Taiwan Institute of Chemical Engineers |
| record_format | dspace |
| spelling | upm.eprints-1137282025-01-15T08:11:30Z http://psasir.upm.edu.my/id/eprint/113728/ The catalytic deoxygenation reaction temperature and N2 gas flow rate influence the conversion of soybean fatty acids into Green Diesel Hafriz, R.S.R.M. Habib, S.H. Raof, N.A. Razali, S.Z. Yunus, R. Razali, N.M. Salmiaton, A. Background: Green diesel is a promising alternative as a petroleum replacement given the worldwide demand for petroleum fuel. Environmental issues have drawn public attention and concerns towards advancing renewable energy development. A catalytic deoxygenation (deCOx) was carried out to produce green diesel from soybean oil (SO) using a low-cost NiO-doped calcined dolomite (NiO[sbnd]CD) catalyst. Method: The structure, chemical composition and morphology of NiO[sbnd]CD were comprehensively characterized by XRF, BET, TPD-CO2, SEM and TEM. In this study, the effect of two operating parameters, reaction temperature and flow rate of nitrogen, was discovered using a one-factor-at-a-time (OFAT) optimisation study. In addition, the life cycle cost analysis (LCCA) of stepwise catalyst preparation and green diesel production has been performed. Significant findings: An optimal reaction temperature of 420 °C was found to provide the highest yield of green diesel (47.13 wt.%) with an 83.51% hydrocarbon composition. The ideal nitrogen flow rate, however, was found to be 50 cm3/min, which produced 41.80 wt.% of green diesel with an 88.63% hydrocarbon composition. The deoxygenation reaction was significantly impacted by both reaction temperature and nitrogen flow rate. According to LCCA, NiO[sbnd]CD catalyst has potential to lower the overall cost of producing green diesel compared to commercial zeolite catalysts. © 2024 Taiwan Institute of Chemical Engineers 2024 Article PeerReviewed text en cc_by_nc_nd_4 http://psasir.upm.edu.my/id/eprint/113728/1/113728.pdf Hafriz, R.S.R.M. and Habib, S.H. and Raof, N.A. and Razali, S.Z. and Yunus, R. and Razali, N.M. and Salmiaton, A. (2024) The catalytic deoxygenation reaction temperature and N2 gas flow rate influence the conversion of soybean fatty acids into Green Diesel. Journal of the Taiwan Institute of Chemical Engineers, 165. art. no. 105700. ISSN 1876-1070; eISSN: 1876-1070 https://linkinghub.elsevier.com/retrieve/pii/S1876107024003584 10.1016/j.jtice.2024.105700 |
| spellingShingle | Hafriz, R.S.R.M. Habib, S.H. Raof, N.A. Razali, S.Z. Yunus, R. Razali, N.M. Salmiaton, A. The catalytic deoxygenation reaction temperature and N2 gas flow rate influence the conversion of soybean fatty acids into Green Diesel |
| title | The catalytic deoxygenation reaction temperature and N2 gas flow rate influence the conversion of soybean fatty acids into Green Diesel |
| title_full | The catalytic deoxygenation reaction temperature and N2 gas flow rate influence the conversion of soybean fatty acids into Green Diesel |
| title_fullStr | The catalytic deoxygenation reaction temperature and N2 gas flow rate influence the conversion of soybean fatty acids into Green Diesel |
| title_full_unstemmed | The catalytic deoxygenation reaction temperature and N2 gas flow rate influence the conversion of soybean fatty acids into Green Diesel |
| title_short | The catalytic deoxygenation reaction temperature and N2 gas flow rate influence the conversion of soybean fatty acids into Green Diesel |
| title_sort | catalytic deoxygenation reaction temperature and n2 gas flow rate influence the conversion of soybean fatty acids into green diesel |
| url | http://psasir.upm.edu.my/id/eprint/113728/1/113728.pdf |
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