从动物残渣中生产燃料气体。第二部分。经济评估

E. Ashare, R.L. Wentworth, D.L. Wise
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引用次数: 13

摘要

建立了一个描述动物粪便厌氧消化的数学模型,考虑了该过程的物质和能量平衡、动力学和经济学。该模型具有灵活性,适用于任何规模或类型的畜牧业经营的残留物。为该模型编写了一个计算机程序,该程序包含了基于最小单位气体成本的过程优化程序,优化变量为消化器温度、保留时间和进水挥发性固体浓度。计算机程序用于确定最佳基线工艺条件和经济性,通过厌氧消化燃料气生产来自1万头环境牛肉饲养场的残留物。在最低单位天然气成本条件下,该试验场计算出每天生产8500立方米(300 MCF)甲烷,成本为4.90美元/GJ或0.183美元/m'(5.17美元/MCF [CH4]),总资本需求为1,165,000美元,总资本投资为69.4万美元,年平均净运营成本为37万美元。不包括沼气池排出物可能的再进料费用,但计入了原粪肥每毫克2.78美元(每吨2.50美元)的费用。单位气体成本的主要贡献是劳动力(37%),原料粪便(11%),气体压缩功率(10%)和沼气池成本(13%)。进行了单位气体成本对单位气体成本主要贡献变化的敏感性分析,该分析的结果指出了厌氧消化系统设计中可能需要合理改进的领域,以便以更经济可行的成本生产气体。敏感性分析包括饲养场规模和类型、沼气池类型、沼气池运行条件和经济投入数据对单位气体成本的影响。例如,计算出一个40,000头的环境饲养场生产甲烷的成本为1.42美元/GJ或0.050美元/m3(1.50美元/MCF),使用连续搅拌罐式反应器消化池,并将消化池出水作为再进料计入。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
Fuel gas production from animal residue part II. an economic assessment

A mathematical model description of anaerobic digestion of animal residues was developed, taking into account material and energy balances, kinetics, and economics of the process. The model had the flexibility to be applicable to residues from any size or type of animal husbandry operation. A computer program was written for this model incorporating a procedure for process optimization, based on minimum unit gas cost, with the optimization variables being digester temperature, retention time, and influent volatile solids concentration. The computer program was used to determine the optimum baseline process conditions and economics for the fuel gas production via anaerobic digestion of residues from a 10,000 head environmental beef feedlot. This feedlot - at the conditions for minimum unit gas cost - was calculated to produce 8500 m3 (300 MCF)/day of methane at a cost of $4.90/GJ or $0.183/m' ($5.17/MCF [CH4]), with a total capital requirement of $1,165,000, a total capital investment of $694,000, and an annual average net operating cost of $370,000. No credit for possible refeed of digester effluent was included but a cost of $2.78/Mg ($2.50/ton) for the raw manure was incorporated. The major contributions to this unit gas cost were due to labor (37%), raw manure (11%), power for gas compression (10%), and digester cost (13%). A sensitivity analysis of the unit gas cost to changes in the major contributions to unit gas cost was performed, and the results of this analysis indicated areas in the anaerobic digestion system design where reasonable improvements may be expected so as to produce gas at a more economically feasible cost. This sensitivity analysis included the effects on unit gas cost of feedlot size and type, digester type, digester operating conditions, and economic input data. For example, a 40,000 head environmental feedlot was computed to produce methane for $1.42/GJ or $0.050/m3 ($1.50/MCF), using a continuously stirred tank reactor digester and taking a credit for the digester effluent as refeed.

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