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Techno-economical evaluation of membrane based biogas upgrading system:A comparison between polymeric membrane and carbon membrane technology

机译:基于膜的沼气升级系统的技术经济评价:聚合物膜和碳膜技术的比较

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摘要

A shift to renewable energy sources will reduce emissions of greenhouse gases and secure future energy supplies. In this context, utilization of biogas will play a prominent role. Focus of this work is upgrading of biogas to fuel quality by membrane separation using a carbon hollow fibre(CHF) membrane and compare with a commercially available polymeric membrane(polyimide) through economical assessment. CHF membrane modules were prepared for pilot plant testing and performance measured using CO2, O2, N2. The CHF membrane was modified through oxidation, chemical vapour deposition(CVD) and reduction process thus tailoring pores for separation and increased performance. The post oxidized and reduced carbon hollow fibres(PORCHFs) significantly exceeded CHF performance showing higher CO2 permeance(0.021 m3(STP)/m2 h bar) and CO2/CH4 selectivity of 246(5 bar feed vs 50 mbar permeate pressure). The highest performance recorded through experiments(CHF and PORCHF) was used as simulation basis. A membrane simulation model was used and interfaced to 8.6 V Aspen HYSYS.A 300 Nm3/h mixture of CO2/CH4 containing 30-50% CO2 at feed pressures 6, 8 and 10 bar, was simulated and process designed to recover99.5% CH4 with 97.5% purity. Net present value(NPV) was calculated for base case and optimal pressure(50 bar for CHF and PORCHF). The results indicated that recycle ratio(recycle/feed) ranged from 0.2 to 10, specific energy from 0.15 to 0.8(kW/Nm3 feed) and specific membrane area from 45 to 4700(m2/Nm3 feed). The high recycle ratio can create problems during start-up, as it would take long to adjust volumetric flow ratio towards 10. The best membrane separation system employs a three-stage system with polyimide at 10 bar, and a two-stage membrane system with PORCHF membranes at 50 bar with recycle. Considering biomethane price of 0.78 $/Nm3 and a lifetime of 15 years, the technoeconomic analysis showed that payback time for the best cascade is 1.6 months.
机译:转向可再生能源将减少温室气体排放并确保未来的能源供应。在这种情况下,沼气的利用将发挥重要作用。这项工作的重点是通过使用碳中空纤维(CHF)膜进行膜分离,将沼气提高到燃料质量,并通过经济评估与市售的聚合物膜(聚酰亚胺)进行比较。 CHF膜组件已准备用于中试工厂测试,并使用CO2,O2,N2测量性能。 CHF膜通过氧化,化学气相沉积(CVD)和还原过程进行了改性,因此可定制孔以进行分离并提高性能。后氧化和还原的碳中空纤维(PORCHFs)大大超过了CHF性能,显示出更高的CO2透过率(0.021 m3(STP)/ m2 h bar)和246的CO2 / CH4选择性(5 bar进料与50 mbar透过压力)。通过实验记录的最高性能(CHF和PORCHF)被用作模拟基础。使用膜模拟模型并将其连接到8.6 V Aspen HYSYS。在进料压力为6、8和10 bar的条件下,模拟了300 Nm3 / h的CO2 / CH4混合物,其中包含30-50%的CO2,并设计回收率达到99.5% CH4,纯度为97.5%。计算基础情况和最佳压力(CHF和PORCHF为50 bar)的净现值(NPV)。结果表明,循环比(循环/进料)为0.2〜10,比能为0.15〜0.8(kW / Nm3进料),比膜面积为45〜4700(m2 / Nm3进料)。高的循环比会在启动过程中产生问题,因为将体积流量比调整到10会花费很长时间。最好的膜分离系统采用三级系统,聚酰亚胺压力为10 bar,两级膜系统为PORCHF膜在50 bar下可回收。考虑到生物甲烷的价格为0.78美元/ Nm3,使用寿命为15年,技术经济分析表明,最佳级联的投资回收期为1.6个月。

著录项

  • 来源
    《绿色能源与环境:英文版》 |2016年第003期|P.222-234|共13页
  • 作者单位

    Norwegian University of Science and Technology, NTNU, Department of Chemical Engineering;

    Norwegian University of Science and Technology, NTNU, Department of Chemical Engineering;

    Norwegian University of Science and Technology, NTNU, Department of Chemical Engineering;

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  • 原文格式 PDF
  • 正文语种 CHI
  • 中图分类 废气的处理与利用;
  • 关键词

  • 入库时间 2022-08-19 04:12:58
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