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

被引:0
|
作者
Shamim Haider [1 ]
Arne Lindbrthen [1 ]
May-Britt H?gg [1 ]
机构
[1] Norwegian University of Science and Technology, NTNU, Department of Chemical Engineering
关键词
Carbon membrane; Biogas upgrading; Techno-economical analysis; NPV calculations;
D O I
暂无
中图分类号
X701 [废气的处理与利用];
学科分类号
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 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.
引用
收藏
页码:222 / 234
页数:13
相关论文
共 50 条
  • [31] Membrane technology for treating decanted oily wastewater from marine oil spill operations: Comparison between membrane filtration and membrane bioreactor
    Bhattacharyya, Anisha
    Liu, Lei
    Walsh, Margaret
    Lee, Kenneth
    MARINE POLLUTION BULLETIN, 2023, 194
  • [32] Development of High Methane Recovery Biogas Upgrading System using DDR-type Zeolite Membrane
    Himeno, Shuji
    Suganoh, Shintaro
    Takemi, Tomohiro
    KAGAKU KOGAKU RONBUNSHU, 2014, 40 (06) : 492 - 498
  • [33] Comparison between a moving bed membrane bioreactor and a conventional membrane bioreactor on organic carbon and nitrogen removal
    Yang, Shuai
    Yang, Fenglin
    Fu, Zhimin
    Lei, Ruibo
    BIORESOURCE TECHNOLOGY, 2009, 100 (08) : 2369 - 2374
  • [34] Demonstration of a Biogas Methanation Combined with Membrane Based Gas Upgrading in a Promising Power-to-Gas Concept
    Kirchbacher, Florian
    Miltner, Martin
    Lehner, Markus
    Steinmueller, Horst
    Harasek, Michael
    PRES2016: 19TH INTERNATIONAL CONFERENCE ON PROCESS INTEGRATION, MODELING AND OPTIMIZATION FOR ENERGY SAVINGS AND POLLUTION REDUCTION, 2016, 52 : 1231 - 1236
  • [35] Modification of covalent organic frameworks with dual functions ionic liquids for membrane-based biogas upgrading
    Zhao, Rui
    Wu, Hong
    Yang, Leixin
    Ren, Yanxiong
    Liu, Yutao
    Qu, Zihan
    Wu, Yingzhen
    Cao, Li
    Chen, Zan
    Jiang, Zhongyi
    JOURNAL OF MEMBRANE SCIENCE, 2020, 600
  • [36] A techno-economic evaluation of the energy generation by proton exchange membrane fuel cell using biogas reforming
    Cozendey da Silva, Hector Napolea
    Prata, Diego Martinez
    Alves Lima, Gilson Brito
    Zotes, Luis Perez
    Mattos, Lisiane Veiga
    JOURNAL OF CLEANER PRODUCTION, 2018, 200 : 598 - 608
  • [37] Synthesis of ZIF-8 based composite hollow fiber membrane with a dense skin layer for facilitated biogas upgrading in gas-liquid membrane contactor
    Xu, Yilin
    Li, Xin
    Lin, Yuqing
    Malde, Chandresh
    Wang, Rong
    JOURNAL OF MEMBRANE SCIENCE, 2019, 585 : 238 - 252
  • [38] Preparation of bio-polymeric ferric sulfate based on membrane separation technology
    School of Chemical Engineering, Northeast Dianli University, Jilin 132012, China
    Huagong Xuebao, 2008, 10 (2622-2626):
  • [39] A Novel System for Carbon Dioxide Capture Utilizing Electrochemical Membrane Technology
    Ghezel-Ayagh, Hossein
    Jolly, Stephen
    Patel, Dilip
    Hunt, Jennifer
    Steen, William A.
    Richardson, Carl F.
    Marina, Olga A.
    FUEL CELL SEMINAR 2012, 2013, 51 (01): : 265 - 272
  • [40] Hollow fiber membrane based H2 diffusion for efficient in situ biogas upgrading in an anaerobic reactor
    Luo, Gang
    Angelidaki, Irini
    APPLIED MICROBIOLOGY AND BIOTECHNOLOGY, 2013, 97 (08) : 3739 - 3744