Techno-economical evaluation of membrane based biogas upgrading system:A comparison between polymeric membrane and carbon membrane technology
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Shamim Haider
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Norwegian University of Science and Technology, NTNU, Department of Chemical EngineeringNorwegian University of Science and Technology, NTNU, Department of Chemical Engineering
Shamim Haider
[1
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Arne Lindbrthen
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Norwegian University of Science and Technology, NTNU, Department of Chemical EngineeringNorwegian University of Science and Technology, NTNU, Department of Chemical Engineering
Arne Lindbrthen
[1
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May-Britt H?gg
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Norwegian University of Science and Technology, NTNU, Department of Chemical EngineeringNorwegian University of Science and Technology, NTNU, Department of Chemical Engineering
May-Britt H?gg
[1
]
机构:
[1] Norwegian University of Science and Technology, NTNU, Department of Chemical Engineering
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 CO2permeance(0.021 m~3(STP)/m~2 h bar) and CO2/CH4selectivity 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 Nm~3/h mixture of CO2/CH4containing 30-50% CO2at feed pressures 6, 8 and 10 bar, was simulated and process designed to recover99.5% CH4with 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/Nm~3 feed) and specific membrane area from 45 to 4700(m~2/Nm~3 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 $/Nm~3 and a lifetime of 15 years, the technoeconomic analysis showed that payback time for the best cascade is 1.6 months.
机构:
Hanyang Univ, Dept Chem Engn, 222 Wangsimni Ro, Seoul 04763, South KoreaHanyang Univ, Dept Chem Engn, 222 Wangsimni Ro, Seoul 04763, South Korea
Kim, Se-Jung
Song, Yongjae
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Hanyang Univ, Dept Chem Engn, 222 Wangsimni Ro, Seoul 04763, South KoreaHanyang Univ, Dept Chem Engn, 222 Wangsimni Ro, Seoul 04763, South Korea
Song, Yongjae
Binns, Michael
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Dongguk Univ, Dept Chem & Biochem Engn, 30 Pildong Ro,1 Gil, Seoul 04620, South KoreaHanyang Univ, Dept Chem Engn, 222 Wangsimni Ro, Seoul 04763, South Korea
Binns, Michael
Yeo, Jeong-Gu
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Korea Inst Energy Res, Energy Storage Res Dept, 152 Gajeong Ro, Daejeon 34129, South KoreaHanyang Univ, Dept Chem Engn, 222 Wangsimni Ro, Seoul 04763, South Korea
Yeo, Jeong-Gu
Kim, Jin-Kuk
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Hanyang Univ, Dept Chem Engn, 222 Wangsimni Ro, Seoul 04763, South KoreaHanyang Univ, Dept Chem Engn, 222 Wangsimni Ro, Seoul 04763, South Korea