Effects of Ion Exchange Process on Catalyst Activity and Plasma-Assisted Reactor Toward Cracking of Palm Oil into Biofuels

*Istadi Istadi orcid scopus  -  Department of Chemical Engineering, Diponegoro University, Indonesia
Luqman Buchori  -  Department of Chemical Engineering, Diponegoro University, Indonesia
Didi Dwi Anggoro  -  Department of Chemical Engineering, Diponegoro University, Indonesia
Teguh Riyanto  -  Department of Chemical Engineering, Diponegoro University, Indonesia
Anindita Indriana  -  Department of Chemical Engineering, Diponegoro University, Indonesia
Chusnul Khotimah  -  Department of Chemical Engineering, Diponegoro University, Indonesia
Fachmy Adji Pangestu Setiawan  -  Department of Chemical Engineering, Diponegoro University, Indonesia
Received: 29 Jan 2019; Revised: 9 Apr 2019; Accepted: 10 Apr 2019; Published: 1 Aug 2019; Available online: 30 Apr 2019.
Open Access Copyright (c) 2019 Bulletin of Chemical Reaction Engineering & Catalysis
License URL: http://creativecommons.org/licenses/by-sa/4.0

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Section: The 3rd International Conference on Chemical and Material Engineering 2018 (ICCME 2018)
Language: EN
Statistics: 572 506

Biofuels can be produced through a conventional catalytic cracking system and/or a hybrid catalytic-plasma cracking system. This paper was focused on studying effect of Na+ ion exchange to HY-Zeolite catalyst on catalyst performance to convert palm oil into biofuels over a conventional continuous fixed bed catalytic cracking reactor and comparing the catalytic cracking performance when carried out in a continuous hybrid catalytic-plasma reactor. The catalysts were characterized by X-ray Diffraction (XRD) and Bruneuer-Emmet-Teller (BET) surface area methods. The biofuels product were analyzed using Gas Chromatography-Mass Spectrometry (GC-MS) to determine the hydrocarbons composition of biofuels product. From the results, ion exchange process of Na+ into HY-Zeolite catalyst decreases the catalyst activity due to decreasing the number of active sites caused by blocking of Na+ ion. The selectivity to gasoline ranges achieved 34.25% with 99.11% total conversion when using HY catalyst over conventional continuous fixed bed reactor system. Unfortunately, the selectivity to gasoline ranges decreased to 13.96% and the total conversion decrease slightly to 98.06% when using NaY-Zeolite catalyst. As comparison when the cracking reaction was carried out in a hybrid catalytic-plasma reactor using a spent residual catalytic cracking (RCC) catalyst, the high energetics electron from plasma can improve the reactor performance, where the conversion and yield were increased and the selectivity to lower ranges of hydrocarbons was increased. However, the last results were potential to be intensively studied with respect to relation between reactor temperature and plasma-assisted catalytic reactor parameters. Copyright © 2019 BCREC Group. All rights reserved


Keywords: catalytic-cracking; palm oil; hybrid catalytic-plasma reactor; biofuels

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