Enzymatic pretreatment of recycled grease trap waste in batch and continuous-flow reactors for biodiesel production

被引:12
|
作者
Tran, Nam Nghiep [1 ,2 ]
Gelonch, Marc Escriba [3 ]
Liang, Shu [1 ]
Xiao, Zihao [1 ]
Sarafraz, Mohammad Mohsen [4 ]
Tisma, Marina [5 ]
Federsel, Hans-Jurgen [6 ]
V. Ley, Steven [7 ]
Hessel, Volker [1 ]
机构
[1] Univ Adelaide, Sch Chem Engn & Adv Mat, North Terrace Campus, Adelaide, SA 5005, Australia
[2] Can Tho Univ, Sch Chem Engn, Campus 2,3-2 St, Can Tho 900000, Vietnam
[3] Univ Lleida, Dept Chem, Av Pla La Massa 8, Barcelona 08700, Spain
[4] Deakin Univ, Sch Engn, Geelong, Vic, Australia
[5] Josip Juraj Strossmayer Univ Osijek, Fac Food Technol Osijek, F Kuhaca 18, HR-31000 Osijek, Croatia
[6] RISE Res Inst Sweden, Dept Chem Proc & Pharmaceut Dev, Res & Business Dev, Box 5607, S-11486 Stockholm, Sweden
[7] Univ Cambridge, Yusuf Hamied Dept Chem, Lensfield Rd, Cambridge CB2 1EW, England
关键词
Grease trap waste; Free fatty acids; Biodiesel; Lipase; Continuous flow reactor; SLUDGE PALM OIL; COOKING OIL; PROCESS OPTIMIZATION; CATALYZED BIODIESEL; SEWAGE-SLUDGE; FATTY-ACIDS; ANIMAL FATS; LIPASE; TRANSESTERIFICATION; ESTERIFICATION;
D O I
10.1016/j.cej.2021.131703
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
In this study, we investigated enzymatic pre-treatment of grease trap waste (GTW) as an environmentally beneficial procedure for biodiesel production. Different enzymes, both commercial and newly designed industrial enzymes, were used to reduce the free fatty acids (FFA) level of GTW through an esterification reaction. The process conditions were optimized using response surface methodology with central composite design parameters. A set of 30 experiments, for both batch and continuous flow reactors, were designed to identify the optimal process conditions in which the highest conversion of FFA is achieved. Within the range of the selected operating conditions, the optimized values of reaction temperature, catalyst quantities, ethanol to oil molar ratio, and reaction time for the batch reactor, in which FFA level was reduced to 31.5 %, were found to be 70 degrees C, 4.5 wt%, 3:1, and 25 min respectively. A significant improvement in the reduction of FFA, of which FFA amount is only 9.9 %, was obtained in the flow reactor when using the commercial enzyme (T = 57 degrees C, catalyst loading 4.85 %, ethanol to oil ratio 2:1, t = 25 min). In addition to achieving higher conversion, the continuous-flow experiments saved time since the entire series of experiments were completed in<1.5 days, compared to the 6 days required for the equivalent batch processes. These results confirm the superiority of the continuous-flow reactors over their batch counterparts and open the door for future automation of the methods.
引用
收藏
页数:12
相关论文
共 50 条
  • [21] LIQUEFACTION OF HYDROLYTIC EUCALYPTUS LIGNIN WITH FORMATE IN WATER, USING BATCH AND CONTINUOUS-FLOW REACTORS
    SCHUCHARDT, U
    RODRIGUES, JAR
    COTRIM, AR
    COSTA, JLM
    BIORESOURCE TECHNOLOGY, 1993, 44 (02) : 123 - 129
  • [22] APPLICATION OF BATCH KINETIC DATA TO THE SIZING OF CONTINUOUS-FLOW ACTIVATED-SLUDGE REACTORS
    VANNIEKERK, A
    JENKINS, D
    RICHARD, MG
    WATER SCIENCE AND TECHNOLOGY, 1987, 19 (3-4) : 505 - 516
  • [23] Assessment of continuous catalyst-free production of ethyl esters from grease trap waste
    Trentini, Caroline Portilho
    Fonseca, Jhessica Marchini
    Cardozo-Filho, Lucio
    Reis, Ralpho R.
    Sampaio, Silvio Cesar
    da Silva, Camila
    JOURNAL OF SUPERCRITICAL FLUIDS, 2018, 136 : 157 - 163
  • [24] Biosorption of Pb(II) and Cu(II) by activated sludge in batch and continuous-flow stirred reactors
    Sag, Y
    Tatar, B
    Kutsal, T
    BIORESOURCE TECHNOLOGY, 2003, 87 (01) : 27 - 33
  • [25] Biohydrogen production from enzymatic hydrolysis of food waste in batch and continuous systems
    Wei Han
    Yingting Yan
    Yiwen Shi
    Jingjing Gu
    Junhong Tang
    Hongting Zhao
    Scientific Reports, 6
  • [26] Biohydrogen production from enzymatic hydrolysis of food waste in batch and continuous systems
    Han, Wei
    Yan, Yingting
    Shi, Yiwen
    Gu, Jingjing
    Tang, Junhong
    Zhao, Hongting
    SCIENTIFIC REPORTS, 2016, 6
  • [27] Resource utilization of waste deNOx catalyst for continuous-flow catalysis by supported metal reactors
    Jin, Qijie
    Shen, Yuesong
    Li, Xiujun
    Zeng, Yanwei
    MOLECULAR CATALYSIS, 2020, 480
  • [28] Dark fermentative biohydrogen production from confectionery wastewater in continuous-flow reactors
    Mikheeva, E. R.
    Katraeva, I., V
    Vorozhtsov, D. L.
    Kovalev, D. A.
    Kovalev, A. A.
    Grigoriev, V. S.
    Litti, Yu, V
    INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2022, 47 (53) : 22348 - 22358
  • [29] Deacidification of high-acid rice bran oil by the tandem continuous-flow enzymatic reactors
    Xu, Liujia
    Zhang, Yi
    Zivkovic, Vladimir
    Zheng, Mingming
    FOOD CHEMISTRY, 2022, 393
  • [30] A continuous-flow bubble column reactor for biodiesel production by non-catalytic transesterification
    Joelianingsih
    Nabetani, H.
    Sagara, Y.
    Tambunan, A. H.
    Abdullah, K.
    FUEL, 2012, 96 (01) : 595 - 599