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Continuous production of biodiesel from cottonseed oil and methanol using a column reactor packed with calcined sodium silicate base catalyst☆
引用本文:Xia Gui,Sichen Chen,Zhi Yun. Continuous production of biodiesel from cottonseed oil and methanol using a column reactor packed with calcined sodium silicate base catalyst☆[J]. 中国化学工程学报, 2016, 24(4): 499-505. DOI: 10.1016/j.cjche.2015.11.006
作者姓名:Xia Gui  Sichen Chen  Zhi Yun
作者单位:College of Chemistry and Chemical Engineering, Nanjing Tech University, Nanjing 210009, China
基金项目:Supported by the National Natural Science Foundation of China(21306088);National Key Technologies R&D Program of China(2015BAD15B07);State Key Laboratory of Chemical Engineering(SKL-Ch E-13A01,Tsinghua University,China);Priority Academic Program Development of Jiangsu Higher Education Institutions(PAPD,China)
摘    要:Sodium silicate and that calcined at 400 °C for 2 h were used to catalyze the transesterification of cottonseed oil with methanol. Calcined sodium silicate(CSS) catalyst exhibited much higher catalytic activity and stability. A maximum biodiesel yield of 98.9% was achieved at methanol/oil mole ratio of 12:1, reaction temperature65 °C, reaction time 3.0 h, and CSS/oil mass ratio of 2 wt%. After 7 consecutive reactions without any treatment,biodiesel yield reduced to 82.5%. Considering technological and economic feasibility, CSS base catalyst supported on θ rings was prepared for continuous transesterification. The maximum yield was 99.1% under optimum conditions(reaction temperature 55 °C, methanol velocity 1 ml·min-1, oil velocity 3 ml·min-1, and 5 tower sections). These results indicate that this new continuous biodiesel production process and apparatus present a great potential for industrial application in biodiesel.

关 键 词:Transesterification  Cottonseed oil  Calcined sodium silicate  Biodiesel  Sodium silicate  Continuous production  
收稿时间:2015-06-01

Continuous production of biodiesel from cottonseed oil and methanol using a column reactor packed with calcined sodium silicate base catalyst
Xia Gui,Sichen Chen,Zhi Yun. Continuous production of biodiesel from cottonseed oil and methanol using a column reactor packed with calcined sodium silicate base catalyst[J]. Chinese Journal of Chemical Engineering, 2016, 24(4): 499-505. DOI: 10.1016/j.cjche.2015.11.006
Authors:Xia Gui  Sichen Chen  Zhi Yun
Affiliation:College of Chemistry and Chemical Engineering, Nanjing Tech University, Nanjing 210009, China
Abstract:Sodium silicate and that calcined at 400℃ for 2 h were used to catalyze the transesterification of cottonseed oil with methanol. Calcined sodium silicate (CSS) catalyst exhibited much higher catalytic activity and stability. A maximum biodiesel yield of 98.9% was achieved at methanol/oil mole ratio of 12:1, reaction temperature 65℃, reaction time 3.0 h, and CSS/oil mass ratio of 2 wt%. After 7 consecutive reactions without any treatment, biodiesel yield reduced to 82.5%. Considering technological and economic feasibility, CSS base catalyst supported on θ rings was prepared for continuous transesterification. The maximum yield was 99.1% under optimum conditions (reaction temperature 55℃,methanol velocity 1 ml·min-1, oil velocity 3ml·min-1, and 5 tower sections). These results indicate that this newcontinuous biodiesel production process and apparatus present a great potential for industrial application in biodiesel.
Keywords:Transesterification  Cottonseed oil  Calcined sodium silicate  Biodiesel  Sodium silicate  Continuous production
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