Technoeconomic Analysis of Biofuel Production and Biorefinery Operation Utilizing Geothermal Energy

被引:8
作者
Banerjee, Sudhanya [1 ]
Tiarks, Jordan A. [1 ]
Lukawski, Maciej [2 ]
Kong, Song-Charng [1 ]
Brown, Robert C. [1 ]
机构
[1] Iowa State Univ, Dept Mech Engn, Ames, IA 50011 USA
[2] Cornell Univ, Sch Chem & Biomol Engn, Ithaca, NY 14850 USA
关键词
BIOMASS RESOURCES; WORKING FLUIDS; GASIFICATION; CONVERSION; LIQUIDS;
D O I
10.1021/ef301898n
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
A technoeconomic study is conducted to assess the feasibility of integrating geothermal energy into a biorefinery for biofuel production. The biorefinery is based on a thermochemical platform that converts low-value lignocellulosic biomass into biofuels via gasification and fuel reforming. Geothermal energy is utilized in the refinery to generate process steam for gasification and steam-methane reforming in addition to providing excess electricity via the organic Rankine cycle. A process simulation model is developed to simulate the operation of the proposed biorefinery, and corresponding economic analysis tools are utilized to predict the product value. The biorefinery uses 2000 metric tons of corn stover per day, and the products include gasoline, diesel fuel, hydrogen, and electricity. Implementation of geothermal energy into the proposed biorefinery is analyzed through two studies. In the first study, process steam at 150 degrees C with a flow rate of approximately 16 kg/s is assumed to be generated through a heat exchanger process by utilizing the heat from geothermal resources, producing a geothermal liquid at 180 degrees C and a total flow rate of 105 kg/s which is used to provide steam for gasification and steam-methane reforming within the biorefinery. In the second study, additional geothermal capacity of 204 kg/s is assumed to be available and is separated into two phases (liquid and steam) via a flash column. The steam produced is utilized in the same manner as the initial study while the geothermal liquid is used for electricity production via the organic Rankine cycle to add to the profitability of the biorefinery. This analysis considers that the technology is feasible in the near future with a high scope of technology development and the end products are compatible with the present fuel infrastructure. The total capital investment, operating costs, and total product values are calculated considering an operating duration of 20 years for the plant, and the data are reported based on the 2012 cost year. Simulation results show that the price of the fuel obtained from the present biorefinery utilizing geothermal energy ranges from $5.17 to $5.48 per gallon gasoline equivalent, which is comparable to $5.14 using the purchased steam. One important incentive for using geothermal energy in the present scenario is the reduction of greenhouse gas emissions resulting from the combustion of fossil fuels used to generate the purchased steam. Geothermal energy is an important renewable energy resource, and this study provides a unique way of integrating geothermal energy into a biorefinery to produce biofuels in an environmentally friendly manner.
引用
收藏
页码:1381 / 1390
页数:10
相关论文
共 35 条
[1]  
Anderson B., 2012, COMMUNICATION
[2]  
[Anonymous], HYDROPROCESSING HEAV
[3]  
[Anonymous], 2007, NREL/TP-510-41168
[4]  
[Anonymous], 2003, BIORENEWABLE RESOURC
[5]  
Bain R. L., 1992, NRELTP51017098
[6]   Geothermal energy technology and current status: an overview [J].
Barbier, E .
RENEWABLE & SUSTAINABLE ENERGY REVIEWS, 2002, 6 (1-2) :3-65
[7]   Comparative analysis of natural and synthetic refrigerants in application to low temperature Clausius-Rankine cycle [J].
Borsukiewicz-Gozdur, Aleksandra ;
Nowak, Wladyslaw .
ENERGY, 2007, 32 (04) :344-352
[8]   Economics of biomass energy utilization in combustion and gasification plants: effects of logistic variables [J].
Caputo, AC ;
Palumbo, M ;
Pelagagge, PM ;
Scacchia, F .
BIOMASS & BIOENERGY, 2005, 28 (01) :35-51
[9]   Modelling and optimisation of solar organic rankine cycle engines for reverse osmosis desalination [J].
Carles Bruno, Joan ;
Lopez-Villada, Jesus ;
Letelier, Eduardo ;
Romera, Silvia ;
Coronas, Alberto .
APPLIED THERMAL ENGINEERING, 2008, 28 (17-18) :2212-2226
[10]   A review of thermodynamic cycles and working fluids for the conversion of low-grade heat [J].
Chen, Huijuan ;
Goswami, D. Yogi ;
Stefanakos, Elias K. .
RENEWABLE & SUSTAINABLE ENERGY REVIEWS, 2010, 14 (09) :3059-3067