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All Journal Agrokreatif Jurnal Ilmiah Pengabdian kepada Masyarakat Jurnal Sains dan Teknologi Reaksi Jurnal Pengabdian kepada Masyarakat Nusantara Jurnal Teknologi WISDOM : Jurnal Pengabdian Kepada Masyarakat Wisdom
Eka Kurniasih
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Agriculture, Biological Sciences & Forestry Chemical Engineering, Chemistry & Bioengineering Chemistry Civil Engineering, Building, Construction & Architecture Computer Science & IT Decision Sciences, Operations Research & Management Economics, Econometrics & Finance Education Electrical & Electronics Engineering Engineering Materials Science & Nanotechnology Mechanical Engineering Social Sciences Other

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Journal : Jurnal Teknologi

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Aplikasi Katalis Heterogen (H-Zeolit) pada Prototype Fluidized Bed Reactor Secara Batch untuk Produksi Biodiesel dari Fatty Acid Methyl Ester Furia Andani; Pardi -; Eka Kurniasih
Jurnal Teknologi Vol 16, No 1 (2016): April 2016
Publisher : Politeknik Negeri Lhokseumawe

Show Abstract | Download Original | Original Source | Check in Google Scholar | Full PDF (263.877 KB) | DOI: 10.30811/teknologi.v16i1.324

Abstract

Biodiesel is an alternative energy diesel / solar is usually produced through esterification and transesterification. Usually biodiesel produced using a homogeneous catalyst (alkaline/acid). There are weaknesses in homogeneous alkaline catalysts (KOH and NaOH), the soap will appear at the end of the biodiesel production process and very difficult when the separation (separation). Heterogeneous catalyst is a homogeneous catalyst solution to replace due to different phase reactants, a heterogeneous catalyst is zeolite, zeolite catalyst are very easily separated and do not form soap at the end of the biodiesel production process. In previous research, biodiesel is produced using a laboratory scale reactor neck flask 3. Therefore, in this research developed the biodiesel production process of fatty acid methyl ester (FAME) using zeolite catalyst H+ in the fluidized bed reactor prototype. Zeolite catalyst performance can be enlarged with the filling material into the zeolite KI. Prototype fluidized bed reactor is operated at the speed of the flow rate of 5 liter / min and the fluidization in the reactor with the minimum fluidization velocity 1.24 cm/s, the weight ratio of zeolite catalyst 2.5% (w/w), mole ratio of methanol : FAME conversion of methyl ester obtained in the 80 minute, is 69.58%
Co-Authors . Raudah Alfizar Amir D Cut Meutia Rahmi Furia Andani Inayatillah Inayatillah Juhan, Nawawi Khairun Nisa Liston Siringo Ringo Mauliana Mauliana Muhammad Reza Aulia Pardi - Pardi Pardi Rahmawati Rahmawati, Gunawan Reza Fauzan Shafira Riskina Syafruddin Syafruddin Syarif, Jenne Yunianda Eka Pertiwi Zahra Fona