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2014
DOI: 10.1063/1.4887756
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Optimization of the pyrolysis process of empty fruit bunch (EFB) in a fixed-bed reactor through a central composite design (CCD)

Abstract: Abstract. The production of crude palm oil from the processing of palm fresh fruit bunches in the palm oil mills in Malaysia hs resulted in a huge quantity of empty fruit bunch (EFB) accumulated. The EFB was used as a feedstock in the pyrolysis process using a fixed-bed reactor in the present study. The optimization of process parameters such as pyrolysis temperature (factor A), biomass particle size (factor B) and holding time (factor C) were investigated through Central Composite Design (CCD) using Stat-Ease… Show more

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Cited by 13 publications
(5 citation statements)
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“…A standard RSM analysis in conjunction with one factor design was used to develop experimental runs. In single factor experiments, ANOVA models are used to compare the mean response values at different levels of the factor [16]. Each level of the factor is investigated to see if the response is significantly different from the response at other levels of the factor.…”
Section: Response Surface Methodologymentioning
confidence: 99%
“…A standard RSM analysis in conjunction with one factor design was used to develop experimental runs. In single factor experiments, ANOVA models are used to compare the mean response values at different levels of the factor [16]. Each level of the factor is investigated to see if the response is significantly different from the response at other levels of the factor.…”
Section: Response Surface Methodologymentioning
confidence: 99%
“…Oil palm empty fruit bunches were gathered in Surat Thani, Southern Thailand, for usage as a raw material in this study. The activated carbon was made in the following processes: the raw materials were crushed and sieved into tiny sizes ranging from 1.0 to 2.0 mm and then pyrolyzed in a fixed bed reactor with flowing N 2 at 450 °C for 1.5 hours, yielding biochar (hereafter named EFB) [12,13]. The biochar was soaked in a phosphoric acid solution with a biochar/H 3 PO 4 impregnation ratio of 1 : 1.75 (wt%) and periodic stirring [14].…”
Section: Adsorbent Preparationmentioning
confidence: 99%
“…The second category is bio-oil characterization and compound analysis [42][43][44][45]. The third category covers the conversion process, experimental design and optimization, including optimal design of reactors to achieve a high production yield, design of experiments, Taguchi Method and other methodologies involved in optimizing the reactors [46][47][48][49][50][51][52][53][54][55]. The fourth category covers bio-oil upgrading for fuel applications [56,57].…”
Section: Type Of Biomass Bymentioning
confidence: 99%
“…Major References Method of bio-oil conversion [32][33][34][35][36][37][38][39][40][41] Chemical compound analysis [42][43][44][45] Optimization of process design and parameters [46][47][48][49][50][51][52][53][54][55][56] Upgrading of bio-oil [57,58] Energy and environment [30,[59][60][61][62][63][64][65][66][67][68] 2. Conversion of Oil Palm EFB to Bio-Oil: Principles and Processes…”
Section: Categorymentioning
confidence: 99%
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