Comparative Technoeconomic Analysis of Using Waste and Virgin Cooking Oils for Biodiesel Production

被引:17
作者
Al-Sakkari, Eslam G. [1 ]
Mohammed, Mohammed G. [1 ,2 ]
Elozeiri, Alaaeldin A. [1 ]
Abdeldayem, Omar M. [1 ,3 ]
Habashy, Mahmoud M. [1 ,3 ]
Ong, Ee Shen [3 ]
Rene, Eldon R. [3 ]
Ismail, Ibrahim [1 ,5 ]
Ashour, Ibrahim [1 ,4 ]
机构
[1] Zewail City Sci & Technol, Environm Engn Program, Giza, Egypt
[2] Cairo Univ, Fac Engn, Chem Engn Dept, Giza, Egypt
[3] UNESCO IHE Inst Water Educ, Dept Environm Engn & Water Technol, Delft, Netherlands
[4] Menia Univ, Fac Engn, Chem Engn Dept, El Minia, Egypt
[5] King Salman Int Univ, Fac Engn, Energy Engn Program, El Toor, Egypt
关键词
biodiesel; waste cooking oil; cement kiln dust; technoeconomic study; sensitivity analysis; CEMENT KILN DUST; HETEROGENEOUS CATALYST; PRODUCTION ECONOMICS; SULFURIC-ACID; BLACK CARBON; TRANSESTERIFICATION; PERFORMANCE; OPTIMIZATION; FEASIBILITY; FEEDSTOCK;
D O I
10.3389/fenrg.2020.583357
中图分类号
TE [石油、天然气工业]; TK [能源与动力工程];
学科分类号
0807 ; 0820 ;
摘要
This study aims to provide the technoeconomic aspects of two clean processes for biodiesel production. The first process utilizes waste cooking oil as a feedstock and potassium hydroxide as a homogeneous catalyst. The second process uses cement kiln dust heterogeneous catalyst and virgin soybean oil. A comparison was performed between the results of the technical and economic assessments to determine the more feasible process. Theoretical purities of biodiesel and glycerol obtained upon conducting the simulation of both processes are high, i.e., 99.99%. However, the homogeneous process is economically superior as its payback period is slightly more than 1 year while the return on investment is higher than 74%, and the unit production cost is USD 1.067/kg biodiesel. Sensitivity analysis revealed that the profitability of biodiesel production is very sensitive to the feedstock price and recommends shifting toward waste vegetable oils as a cheap feedstock to have a feasible and economic process.
引用
收藏
页数:13
相关论文
共 58 条
[1]  
Abed K. A., 2019, Egyptian Journal of Petroleum, V28, P183, DOI 10.1016/j.ejpe.2019.03.001
[2]   Investigation of cement kiln dust utilization for catalyzing biodiesel production via response surface methodology [J].
Al-Sakkari, E. G. ;
El-Sheltawy, S. T. ;
Abadir, M. F. ;
Attia, N. K. ;
El-Diwani, G. .
INTERNATIONAL JOURNAL OF ENERGY RESEARCH, 2017, 41 (04) :593-603
[3]   Kinetic study of soybean oil methanolysis using cement kiln dust as a heterogeneous catalyst for biodiesel production [J].
Al-Sakkari, E. G. ;
El-Sheltawy, S. T. ;
Attia, N. K. ;
Mostafa, S. R. .
APPLIED CATALYSIS B-ENVIRONMENTAL, 2017, 206 :146-157
[4]  
Al-Sakkari E.G., 2018, J ADV CHEM SCI, V4, P586, DOI [DOI 10.30799/JACS.195.18040305, 10.30799/jacs.195.18040305]
[5]   Esterification of high FFA content waste cooking oil through different techniques including the utilization of cement kiln dust as a heterogeneous catalyst: A comparative study [J].
Al-Sakkari, Eslam G. ;
Abdeldayem, Omar M. ;
El-Sheltawy, S. T. ;
Abadir, Magdi F. ;
Soliman, Ahmed ;
Rene, Eldon R. ;
Ismail, Ibrahim .
FUEL, 2020, 279
[6]  
AlSakkari EG, 2018, J ADV CHEM SCI, P593
[7]  
[Anonymous], 2019, WASTE MANAGEMENT RES
[8]   Biodiesel production from Calophyllum inophyllum oil a potential non-edible feedstock: An overview [J].
Arumugam, A. ;
Ponnusami, V. .
RENEWABLE ENERGY, 2019, 131 :459-471
[9]   Biodiesel Production from Melia azedarach and Ricinus communis Oil by Transesterification Process [J].
Awais, Muhammad ;
Musmar, Sa'ed A. ;
Kabir, Faryal ;
Batool, Iram ;
Rasheed, Muhammad Asif ;
Jamil, Farrukh ;
Khan, Sami Ullah ;
Tlili, Iskander .
CATALYSTS, 2020, 10 (04)
[10]   Is the production of biofuels and bio-chemicals always profitable? Co-production of biomethane and urea from biogas as case study [J].
Baena-Moreno, Francisco M. ;
Sebastia-Saez, D. ;
Wang, Qiang ;
Reina, T. R. .
ENERGY CONVERSION AND MANAGEMENT, 2020, 220