Ammonia production from black liquor gasification and co-gasification with pulp and waste sludges: A techno-economic assessment

被引:47
作者
Akbari, Maryam [1 ]
Oyedun, Adetoyese Olajire [1 ]
Kumar, Amit [1 ]
机构
[1] Univ Alberta, Dept Mech Engn, Donadeo Innovat Ctr Engn 10 263, Edmonton, AB T6G 1H9, Canada
基金
加拿大自然科学与工程研究理事会;
关键词
Black liquor; Techno-economic model; Gasification; Ammonia; Production cost; HYDROGEN-PRODUCTION; OIL USE; BIOMASS; GAS; PLANT; REDUCTIONS; CONVERSION; PYROLYSIS; DESIGN;
D O I
10.1016/j.energy.2018.03.056
中图分类号
O414.1 [热力学];
学科分类号
摘要
The economic feasibility of producing ammonia through the gasification of three different feedstocks produced in pulp and paper mills is investigated in this paper. The first case uses black liquor, the main by-product of the kraft pulping process, as the feedstock, and in the other two cases pulp sludge (PS) and waste sludge (WS) are co-gasified with black liquor. For all three cases, a process model in which mass and energy balances were calculated was developed. The model results were used to estimate the equipment size and estimate costs. Techno-economic models were developed and ammonia production costs were calculated. A case study for Alberta, a western Canadian province, was conducted. The results indicated that for a 10% discount rate (or internal rate of return [IRR]), ammonia production in all three cases is cost competitive with current ammonia prices. The cost of production (COP) of ammonia for all three cases ranges from 743 to 748 Sit. Sensitivity and uncertainty analyses were conducted on the estimated COP, and the results show that the COP is the most sensitive to the capital cost, discount rate, electricity price and plant lifetime. (C) 2018 Elsevier Ltd. All rights reserved.
引用
收藏
页码:133 / 143
页数:11
相关论文
共 64 条
[1]   Comparison of pulp-mill-integrated hydrogen production from gasified black liquor with stand-alone production from gasified biomass [J].
Andersson, E. ;
Harvey, S. .
ENERGY, 2007, 32 (04) :399-405
[2]   System analysis of hydrogen production from gasified black liquor [J].
Andersson, E. ;
Harvey, S. .
ENERGY, 2006, 31 (15) :3426-3434
[3]   Techno-economic analysis of ammonia production via integrated biomass gasification [J].
Andersson, Jim ;
Lundgren, Joakim .
APPLIED ENERGY, 2014, 130 :484-490
[4]  
[Anonymous], 2011, DIFFERENCE AMMONIA A
[5]  
[Anonymous], 2003, PLANT DESIGN EC CHEM
[6]  
[Anonymous], 2016, Efficiency of biomass energy: an exergy approach to biofuels, power, and biorefineries
[7]  
[Anonymous], HYDR PROD NAT GAS RE
[8]  
[Anonymous], 2003, NAT RENEW ENERGY LAB, DOI DOI 10.2172/15006100
[9]  
Areeprasert C., 2016, Int. J. Environ. Sci. Dev, V7, P425, DOI [DOI 10.7763/IJESD.2016.V7.813, 10.7763/IJESD.2016.V7.813]
[10]   Influence of Fuel Moisture Content and Reactor Temperature on the Calorific Value of Syngas Resulted from Gasification of Oil Palm Fronds [J].
Atnaw, Samson Mekbib ;
Sulaiman, Shaharin Anwar ;
Yusup, Suzana .
SCIENTIFIC WORLD JOURNAL, 2014,