THE KINETICS OF CaO ASSISTED PATTUKKU CHARCOAL STEAM GASIFICATION

Abstract   Coal is a solid fuel that can be converted into syngas through gasification process. To obtain optimum gasification process design and operation, in-depth understanding of the influential parameters is required. This study aims to investigate the effect of temperature on the gasification...

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Main Authors: Takdir Syarif, H Sulistyo, Wahyudi B Sediawan, B Budhijanto
Format: Article
Language:English
Published: Diponegoro University 2018-05-01
Series:Reaktor
Online Access:https://ejournal.undip.ac.id/index.php/reaktor/article/view/16216
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spelling doaj-2d213302efa14c7b9d0bff11d6dbe9172020-11-25T00:30:58ZengDiponegoro UniversityReaktor0852-07982407-59732018-05-01181162110.14710/reaktor.18.1.16-2112735THE KINETICS OF CaO ASSISTED PATTUKKU CHARCOAL STEAM GASIFICATIONTakdir Syarif0H Sulistyo1Wahyudi B Sediawan2B Budhijanto3Department of Chemical Engineering, Faculty of Industrial Technology UMI MakassarDepartment of Chemical Engineering Faculty of Engineering Gadjah Mada Unuversity YogyakartaDepartment of Chemical Engineering Faculty of Engineering Gadjah Mada University YogyakartaDepartment of Chemical Engineering Faculty of Engineering Gadjah Mada University YogyakartaAbstract   Coal is a solid fuel that can be converted into syngas through gasification process. To obtain optimum gasification process design and operation, in-depth understanding of the influential parameters is required. This study aims to investigate the effect of temperature on the gasification process and to obtain its kinetics parameters. The study was carried out in a tubular reactor equipped with a heater and a condenser. Steam was used as gasifying agent, while CaO was employed as a CO2 adsorbent. The charcoal from coal was subjected to gasification at temperatures of 600°C, 700°C, and 800°C. The ratio of charcoal and CaO was 1:1. The gasification process lasted for 60 minutes with gas sample was taken every 15 minutes for composition analysis. The results showed that a temperature increase of 100°C caused a proportional increase of conversion of about 75% higher. The value of activation energy (Ea) and exponential factor (ko) were 46.645kJ/mole and 328.3894/min, respectively. For mass transfer parameters, values of activation energy for surface diffusion (Es) and surface diffusivity factor (as) were 81.126 kJ/mole and 0.138/min, respectively.   Keywords: gasification; mathematical model; Pattukku coal char; steam; Thin Reaction Zone Modelhttps://ejournal.undip.ac.id/index.php/reaktor/article/view/16216
collection DOAJ
language English
format Article
sources DOAJ
author Takdir Syarif
H Sulistyo
Wahyudi B Sediawan
B Budhijanto
spellingShingle Takdir Syarif
H Sulistyo
Wahyudi B Sediawan
B Budhijanto
THE KINETICS OF CaO ASSISTED PATTUKKU CHARCOAL STEAM GASIFICATION
Reaktor
author_facet Takdir Syarif
H Sulistyo
Wahyudi B Sediawan
B Budhijanto
author_sort Takdir Syarif
title THE KINETICS OF CaO ASSISTED PATTUKKU CHARCOAL STEAM GASIFICATION
title_short THE KINETICS OF CaO ASSISTED PATTUKKU CHARCOAL STEAM GASIFICATION
title_full THE KINETICS OF CaO ASSISTED PATTUKKU CHARCOAL STEAM GASIFICATION
title_fullStr THE KINETICS OF CaO ASSISTED PATTUKKU CHARCOAL STEAM GASIFICATION
title_full_unstemmed THE KINETICS OF CaO ASSISTED PATTUKKU CHARCOAL STEAM GASIFICATION
title_sort kinetics of cao assisted pattukku charcoal steam gasification
publisher Diponegoro University
series Reaktor
issn 0852-0798
2407-5973
publishDate 2018-05-01
description Abstract   Coal is a solid fuel that can be converted into syngas through gasification process. To obtain optimum gasification process design and operation, in-depth understanding of the influential parameters is required. This study aims to investigate the effect of temperature on the gasification process and to obtain its kinetics parameters. The study was carried out in a tubular reactor equipped with a heater and a condenser. Steam was used as gasifying agent, while CaO was employed as a CO2 adsorbent. The charcoal from coal was subjected to gasification at temperatures of 600°C, 700°C, and 800°C. The ratio of charcoal and CaO was 1:1. The gasification process lasted for 60 minutes with gas sample was taken every 15 minutes for composition analysis. The results showed that a temperature increase of 100°C caused a proportional increase of conversion of about 75% higher. The value of activation energy (Ea) and exponential factor (ko) were 46.645kJ/mole and 328.3894/min, respectively. For mass transfer parameters, values of activation energy for surface diffusion (Es) and surface diffusivity factor (as) were 81.126 kJ/mole and 0.138/min, respectively.   Keywords: gasification; mathematical model; Pattukku coal char; steam; Thin Reaction Zone Model
url https://ejournal.undip.ac.id/index.php/reaktor/article/view/16216
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