Different water removal methods for facilitating biodiesel production from low-cost waste cooking oil containing high water content in hybridized reactive distillation

被引:17
|
作者
Petchsoongsakul, Nattawat [1 ]
Ngaosuwan, Kanokwan [2 ]
Kiatkittipong, Worapon [3 ]
Wongsawaeng, Doonyapong [4 ]
Assabumrungrat, Suttichai [1 ,5 ]
机构
[1] Chulalongkorn Univ, Ctr Excellence Catalysis & Catalyt React Engn, Biorefinery Cluster, Dept Chem Engn, Bangkok 10330, Thailand
[2] Rajamangala Univ Technol Krungthep, Chem Engn Div, Dept Engn, Bangkok 10120, Thailand
[3] Silpakorn Univ, Dept Chem Engn, Fac Engn & Ind Technol, Nakhon Pathom 73000, Thailand
[4] Chulalongkorn Univ, Fac Engn, Dept Nucl Engn, Bangkok 10330, Thailand
[5] Chulalongkorn Univ, Biocircular Greenecon Technol & Engn Ctr, BCGeTEC, Dept Chem Engn,Fac Engn, Bangkok 10330, Thailand
关键词
Hybridized reactive distillation; Biodiesel; Waste cooking oil (WCO); Water removal; Extended spacing stage; Pervaporation membrane; SOYBEAN OIL; FATTY-ACID; CATALYZED TRANSESTERIFICATION; PROCESS DESIGN; FOOD NATURE; ESTERIFICATION; OPTIMIZATION; CONVERSION; METHANOL;
D O I
10.1016/j.renene.2020.09.115
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
Waste cooking oil (WCO) as feedstocks for biodiesel production contains high free fatty acid and water, causing negative impacts on the biodiesel yield and its purity. In this work, three alternative methods for handling water content in WCO feedstocks using the earlier hybridization of esterification and transesterification in a single reactive distillation column (hybridized RD) were investigated. Our simulation results revealed that using two heat exchangers combined with the hybridized RD is a simple method to remove water from WCO. However, it requires the highest energy as well as biodiesel production cost (1.63 USD/kg biodiesel). The extended spacing stage modification of the hybridized RD was proposed to remove water content. It requires a new hybridized RD construction by spacing stages addition which can handle WCO with 10 wt% of water content and require less energy, resulting in lower biodiesel production cost (1.07 USD/kg biodiesel). The integration of pervaporation unit was found to be the best option. It offers the highest performance in terms of water removal and methanol recovery, resulting in the lowest biodiesel production cost (1.04 USD/kg biodiesel). This study shows that using pervaporation or extended spacing stages with hybridized RD are promising methods for biodiesel production from WCO. (C) 2020 Elsevier Ltd. All rights reserved.
引用
收藏
页码:1906 / 1918
页数:13
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