Biotechnology, Lund University, P,O, Box 124, Lund, SE-221 00, Sweden.
Biotechnol Biofuels. 2013 Apr 22;6(1):56. doi: 10.1186/1754-6834-6-56.
The study presented here has used the commercial flow sheeting program Aspen Plus™ to evaluate techno-economic aspects of large-scale hemp-based processes for producing transportation fuels. The co-production of biogas, district heat and power from chopped and steam-pretreated hemp, and the co-production of ethanol, biogas, heat and power from steam-pretreated hemp were analysed. The analyses include assessments of heat demand, energy efficiency and process economics in terms of annual cash flows and minimum biogas and ethanol selling prices (MBSP and MESP).
Producing biogas, heat and power from chopped hemp has the highest overall energy efficiency, 84% of the theoretical maximum (based on lower heating values), providing that the maximum capacity of district heat is delivered. The combined production of ethanol, biogas, heat and power has the highest energy efficiency (49%) if district heat is not produced. Neither the inclusion of steam pretreatment nor co-production with ethanol has a large impact on the MBSP. Ethanol is more expensive to produce than biogas is, but this is compensated for by its higher market price. None of the scenarios examined are economically viable, since the MBSP (EUR 103-128 per MWh) is higher than the market price of biogas (EUR 67 per MWh). The largest contribution to the cost is the cost of feedstock. Decreasing the retention time in the biogas process for low solids streams by partly replacing continuous stirred tank reactors by high-rate bioreactors decreases the MBSP. Also, recycling part of the liquid from the effluent from anaerobic digestion decreases the MBSP. The production and prices of methane and ethanol influence the process economics more than the production and prices of electricity and district heat.
To reduce the production cost of ethanol and biogas from biomass, the use of feedstocks that are cheaper than hemp, give higher output of ethanol and biogas, or combined production with higher value products are primarily suggested. Further, practical investigations on increased substrate concentration in biogas and ethanol production, recycling of the liquid in anaerobic digestion and separation of low solids flows into solid and a liquid fraction for improved reactor applications deserves further attention.
本研究使用商业流程模拟程序 Aspen Plus™ 评估了大规模基于大麻的工艺生产运输燃料的技术经济方面。分析了切碎和蒸汽预处理大麻的沼气、区域供热和电力联产,以及蒸汽预处理大麻的乙醇、沼气、热和电联产。分析包括根据年度现金流量和最低沼气和乙醇销售价格 (MBSP 和 MESP) 评估热需求、能源效率和工艺经济性。
从切碎的大麻中生产沼气、热和电具有最高的整体能源效率,为理论最大值的 84%(基于低位热值),前提是区域供热的最大容量得以输送。如果不生产区域供热,乙醇、沼气、热和电联产的综合生产具有最高的能源效率(49%)。蒸汽预处理的包含或与乙醇的联产对 MBSP 没有重大影响。生产乙醇比生产沼气贵,但这被其更高的市场价格所弥补。所检查的方案都没有经济可行性,因为 MBSP(每兆瓦时 103-128 欧元)高于沼气的市场价格(每兆瓦时 67 欧元)。成本的最大贡献是原料成本。通过部分用高速生物反应器代替连续搅拌罐反应器来减少低固体流的沼气工艺中的保留时间,降低了 MBSP。此外,从厌氧消化的流出物中回收部分液体也降低了 MBSP。甲烷和乙醇的生产和价格对工艺经济性的影响大于电力和区域供热的生产和价格。
为了降低生物质乙醇和沼气的生产成本,建议主要使用比大麻更便宜的原料、提高乙醇和沼气产量,或与附加值更高的产品联产。此外,进一步关注沼气和乙醇生产中底物浓度的提高、厌氧消化中液体的回收以及低固体流的固液分离以改善反应器应用值得进一步关注。