Study on co-catalyst of Layer Double Hydroxide (LDH) and metal catalyst for deoxygenation of Used Cooking Oil (UCO) to produce green fuel

• UCO utilization as a source of green fuel, an alternative a renewable fuel. • Simpler approach to examined catalytic process at lower temperature in reactor that equipped with distillation to give direct analysis for the product. • Providing detailed assessment and deeper insights upon these enablers by establishing contextual interconnection and specific impacts of co-catalyst. • Research must continue to mindfully integrate eco-friendly options into traditional life styles that UCO to green fuel is a valuable contribution toward the future of environmentally sustainable and cost-effective fuel. Green fuel that produced from Used Cooking Oil (UCO) has emerged as a cleaner technology, a product with better properties than biodiesel attracted research community.This work was further observation from profiling co-catalyst consisted Layer Double Hydroxide (LDH) and Fe and Cu as metal catalysts for DeOxygenation (DO). Co-catalytic reactor was operated at low temperature, 250 °C, adjusted to C 12 H 26 boiling point. Moreover, The reactor was equipped with condensor and operated for 36 h to obtain the distillate. Effect of co-catalyst was assessed with Response Surface Method (RSM) using Stat Ease 360 Design Expert. The experimental design for co-catalyst was set at 2 % LDH, 1–3 % Cu and 2–4 % Fe. LDH role was to cut fatty acid chain, while Fe-Cu was to shift in producing more Hydrocarbon (HC) in distillate. As a result, LDH was able to break down fatty acid chain which indicated by average molecular weight fatty acid in UCO 264 and 150 in distillate. Meanwhile, Fe+Cu was able to convert 66.53 % fatty acid and suppress alcohol, ester and ketone/aldehyde formation and shifted to HC. HC level and selectivity reached 59 % and 86 %, respectively. Therefore, LDH and Fe+Cu as co-catalyst were synergized as expected. Simulation of distillate yield was carried out with RSM optimal at 2 % LDH, 4 % Fe and 3 % predicted the yield 10.37 %. Experiment approval showed the yield was 10.7 %.

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Publication Details

Journal
Results in Engineering
Published
2025-04-12
DOI
https://doi.org/10.1016/j.rineng.2025.104865
Citations
2
Primary Topic
Catalysis and Hydrodesulfurization Studies
Type
article
Field-Weighted Citation Impact
1.43

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article

Study on co-catalyst of Layer Double Hydroxide (LDH) and metal catalyst for deoxygenation of Used Cooking Oil (UCO) to produce green fuel

Adid Adep Dwiatmoko, Robert Ronal Widjaya, Tri Widjaja, Edi Supriadi et al.
2 citations
Results in Engineering
Catalysis and Hydrodesulfurization Studies
1.43
article

Study on co-catalyst of Layer Double Hydroxide (LDH) and metal catalyst for deoxygenation of Used Cooking Oil (UCO) to produce green fuel

Adid Adep Dwiatmoko, Robert Ronal Widjaya, Tri Widjaja, Edi Supriadi, Joni Prasetyo, Ahmad Wibisana, Deliana Dahnum, Ali Altway, Hendro Yuwono, Muh. Nur Khoiru Wihadi, Firman Tri Ajie, Sasmito Wulyoadi
article en
2 citations

Abstract

• UCO utilization as a source of green fuel, an alternative a renewable fuel. • Simpler approach to examined catalytic process at lower temperature in reactor that equipped with distillation to give direct analysis for the product. • Providing detailed assessment and deeper insights upon these enablers by establishing contextual interconnection and specific impacts of co-catalyst. • Research must continue to mindfully integrate eco-friendly options into traditional life styles that UCO to green fuel is a valuable contribution toward the future of environmentally sustainable and cost-effective fuel. Green fuel that produced from Used Cooking Oil (UCO) has emerged as a cleaner technology, a product with better properties than biodiesel attracted research community.This work was further observation from profiling co-catalyst consisted Layer Double Hydroxide (LDH) and Fe and Cu as metal catalysts for DeOxygenation (DO). Co-catalytic reactor was operated at low temperature, 250 °C, adjusted to C 12 H 26 boiling point. Moreover, The reactor was equipped with condensor and operated for 36 h to obtain the distillate. Effect of co-catalyst was assessed with Response Surface Method (RSM) using Stat Ease 360 Design Expert. The experimental design for co-catalyst was set at 2 % LDH, 1–3 % Cu and 2–4 % Fe. LDH role was to cut fatty acid chain, while Fe-Cu was to shift in producing more Hydrocarbon (HC) in distillate. As a result, LDH was able to break down fatty acid chain which indicated by average molecular weight fatty acid in UCO 264 and 150 in distillate. Meanwhile, Fe+Cu was able to convert 66.53 % fatty acid and suppress alcohol, ester and ketone/aldehyde formation and shifted to HC. HC level and selectivity reached 59 % and 86 %, respectively. Therefore, LDH and Fe+Cu as co-catalyst were synergized as expected. Simulation of distillate yield was carried out with RSM optimal at 2 % LDH, 4 % Fe and 3 % predicted the yield 10.37 %. Experiment approval showed the yield was 10.7 %.

Results in EngineeringVol. 26
Sepuluh Nopember Institute of Technology (ID), Universitas Pamulang (ID), National Nuclear Energy Agency of Indonesia (ID), National Research and Innovation Agency (ID)
Kementerian Pendidikan dan Kebudayaan
Zero hunger
Openalex Percentile: Top 21%
Catalysis and Hydrodesulfurization Studies
1.43
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