Analysis of the model application of mechanical equipment for hydrothermal treatment at biogas plant

被引:0
作者
Junga P. [1 ]
Trávníček P. [1 ]
Ružbarský J. [2 ]
机构
[1] Mendel University in Brno, Faculty of Agronomy, Department of Agriculture, Food and Environmental Engineering, Zemědělská 1, Brno
[2] Technical University of Kosice, Faculty of Manufacturing Technologies with A Seat in Presov, Bayerova 1, Prešov
关键词
Biogas plant; Economic characteristics; Mechanical equipment; Operational characteristics; Thermal hydrolysis;
D O I
10.4028/www.scientific.net/KEM.669.551
中图分类号
学科分类号
摘要
The goal of the paper was to analyse model applications of mechanical equipment for hydrothermal treatment at biogas plant and impact on the operation of this production system. Alternative 1 was an alternative with a treatment output of 14 500 Mg of processed material, the annual electricity and heat total production of 4000 MWh respectively 3800 MWh, total capital expenditure of 40 000 000 CZK, unit capital expenditure of 2759 CZK per 1 Mg of processed biodegradable material and annual operating expenses of 19 371 000 CZK. The net present value (NPV) is 1 061 000 CZK, the internal rate or return (IRR) totals 4.9%, the simple payback time (Ts) is 12.6 years and the discounted payback time (Tsd) is 19.2 years. Alternative 2 employing the mechanical equipment proved a potential increase in the treatment output to 18 125 Mg, and an increase in the electricity and heat total production to 5000 MWh respectively 4800 MWh, thanks to the shortened intensification of the anaerobic fermentation process. At the same time, the total capital expenditure rose to 43 000 000 CZK, the operating expenses rose to CZK 24 213 000. The unit capital expenditure of alternative 2 amounts to 2372 CZK per 1 Mg of the of processed biodegradable material. The NPV totals 8 329 000 CZK, IRR is at 6.7%, the simple payback time (Ts) is 10.8 years and Tsd totals 15.3 years. © 2016 Trans Tech Publications, Switzerland.
引用
收藏
页码:551 / 559
页数:8
相关论文
共 12 条
[1]  
Kumar S., Kothari U., Kong L., Lee Y.Y., Gupta R.B., Hydrothermal pretreatment of switchgrass and corn stover for production of ethanol and carbon microspheres, Biomass and Bioenergy, 35, pp. 956-968, (2011)
[2]  
Hendriks A.T.W.M., Zeeman G., Pretreatments to enhance the digestibility of lignocellulosic biomass, Bioresource Technology, 100, pp. 10-18, (2009)
[3]  
Climent M., Ferre I., Baeza M., Artola A., Vazquez F., Font X., Effects of thermal and mechanical pretreatments of secondary sludge on biogas production under thermophilic conditions, Chemical Engineering Journal, 133, pp. 335-342, (2007)
[4]  
Wilson Ch.A., Novak J.T., Hydrolysis of macromolecular components of primary and secondary wastewater sludge by thermal hydrolytic pretreatment, Water Research, 43, pp. 4489-4498, (2009)
[5]  
Carrere H., Sialve B., Bernet N., Improving pig manure conversion into biogas by thermal and thermo-chemical pretreatments, Bioresource Technology, 100, pp. 3690-3694, (2009)
[6]  
Piementel D., Patzek T.W., Ethanol production using corn, switchgrass and wood, Natural Resources Research, 14, pp. 3196-3199, (2005)
[7]  
Chen Y., Cheng J.J., Creamer K.S., Inhibition of anaerobic digestion process: A rewiew, Bioresource Technology, 99, pp. 4044-4064, (2008)
[8]  
Ganesh R., Torrijos M., Sousbie P., Steyer J.P., Lugardon A., Delgenes J.P., Anaerobic co-digestion of solid waste: Effect of increasing organic loading rates and characterization of the solubilized organic matter, Bioresource Technology, 130, pp. 559-569, (2013)
[9]  
Li Y., Park S.Y., Zhu J., Solid-state anaerobic digestion for methane production from organic waste, Renewable and Sustainable Energy Rewiews, 15, pp. 821-826, (2011)
[10]  
Synek M., Managerial Economy, pp. 308-309, (2007)