Ni, Zn and Fe hydrotalcite-like catalysts for catalytic biomass compound into green biofuel

Author:

Zdainal Abidin Shajaratun Nur1,Lee Hwei Voon1,Asikin-Mijan Nurul12,Juan Joon Ching1,Rahman Noorsaadah Abd3,Mastuli Mohd Sufri45,Taufiq-Yap Yun Hin26,Kong Pei San7

Affiliation:

1. Nanotechnology and Catalysis Research Centre (Nanocat), Institute of Advanced Studies, University of Malaya, 50603 Kuala Lumpur, Malaysia

2. Catalysis Science and Technology Research Centre (PutraCAT), Faculty of Science, Universiti Putra Malaysia, 43400 UPM Serdang, Selangor, Malaysia

3. Department of Chemistry, Faculty of Science, University of Malaya, 50603 Kuala Lumpur, Malaysia

4. Centre for Nanomaterials Research, Institute of Science, Universiti Teknologi MARA, 40450 Shah Alam, Selangor, Malaysia

5. School of Chemistry and Environment, Faculty of Applied Science, Universiti Teknologi MARA, 40450 Shah Alam, Selangor, Malaysia

6. Chancellery Office, Universiti Malaysia Sabah, 88400 Kota Kinabalu,Sabah, Malaysia

7. Sime Darby Research, R&D Centre – Carey Island, Lot 2664 Jalan Pulau Carey, 42960 Pulau Carey, Selangor, Malaysia

Abstract

AbstractIn this study, the deoxygenation pathway was proposed to eliminate oxygen species from biomass-derived oil, thereby producing a high quality of hydrocarbon chains (green fuel). The catalytic deoxygenation reaction of bio-oil model compound (oleic acid) successfully produced green gasoline (C8–C12) and diesel (C13–C20) via activated hydrotalcite-derived catalysts (i.e. CMgAl, CFeAl, CZnAl and CNiAl). The reaction was performed under inert N2 condition at 300 °C for 3 h, and the liquid products were analysed by GC–MS and GC–FID analyses to determine the hydrocarbon yield and product selectivity. The activity of the catalysts towards the deoxygenation reaction presented the following increasing order: CNiAl > CMgAl > CZnAl > CFeAl. CNiAl produced a hydrocarbon yield of up to 89 %. CNiAl demonstrated the highest selectivity with 83 % diesel production, whereas CMgAl showed the highest gasoline selectivity with 30 %. These results indicated that catalysts with a high acidic profile facilitate C–O cleavage via deoxygenation, producing hydrocarbons (mainly diesel-range hydrocarbons). Meanwhile, highly basic catalysts exhibit significant selectivity towards gasoline-range hydrocarbons via cracking and lead to the occurrence of C–C cleavage. The large surface area of CNiAl (117 m2 g−1) offered high approachability of the reactant with the catalyst’s active sites, thereby promoting high hydrocarbon yield. Consequently, the hydrocarbon yield and selectivity of the deoxygenation products were predominantly influenced by the acid–base properties and structural behaviour (porosity and surface area) of the catalyst.

Publisher

Walter de Gruyter GmbH

Subject

General Chemical Engineering,General Chemistry

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