MEMBRANE INSTALLATION FOR BIOGAS ENRICHMENT - FIELD TESTS AND SYSTEM SIMULATION

被引:5
作者
Chmielewski, Andrzej Grzegorz [1 ]
Urbaniak, Agata [2 ]
Palige, Jacek [1 ]
Roubinek, Otton [1 ]
Wawryniuk, Katarzyna [1 ]
Dobrowolski, Andrzej [1 ]
机构
[1] Inst Nucl Chem & Technol, Dorodna 16, PL-03195 Warsaw, Poland
[2] Warsaw Univ Technol, Dept Chem & Proc Engn, Warynskiego 1, PL-00645 Warsaw, Poland
来源
CHEMICAL AND PROCESS ENGINEERING-INZYNIERIA CHEMICZNA I PROCESOWA | 2019年 / 40卷 / 02期
关键词
polymer membranes; biogas; methane concentration upgrading; trace biogas components; membrane mobile testing unit; multistage membrane system simulation; HOLLOW-FIBER MEMBRANE; MULTICOMPONENT GAS SEPARATION; NATURAL-GAS; CARBON-DIOXIDE; OPTIMIZATION; POLYIMIDE; RECOVERY; COUNTERCURRENT; PERFORMANCE; PERMEATORS;
D O I
10.24425/cpe.2019.126116
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The paper presents results of the field tests on membrane biogas enrichment performed with the application of mobile membrane installation (MMI) with the feed stream up to 10 Nm(3)/h. The mobile installation equipped with four hollow fibre modules with polyimide type membranes was tested at four different biogas plants. Two of them were using agricultural substrates. The third one was constructed at a municipal wastewater plant and sludge was fermented in a digester and finally in the fourth case biogas was extracted from municipal waste landfill site. Differences in the concentration of bio-methane in feed in all cases were observed and trace compounds were detected as well. High selectivity polyimide membranes, in proper module arrangements, can provide a product of high methane content in all cases. The content of other trace compounds, such as hydrogen sulphide, water vapour and oxygen on the product did not exceed the values stated by standard for a biogas as a vehicle fuel. The traces of hydrogen sulphide and water vapour penetrated faster to the waste stream enriched in carbon dioxide, which could lead to further purification of the product - methane being hold in the retentate (H2O > H2S > CO2 > O-2 > CH4 > N-2). In the investigated cases, when concentration of N-2 was low and concentration of CH4 higher than 50%, it was possible to upgrade methane to concentration above 90% in a two-stage cascade. To perform simulation of CH4 and CO2 permeation through polyimide membrane, MATLAB was used. Simulation program has included permeation gaseous mixture with methane contents as observed at field tests in the range of 50 and 60% vol. The mass transport process was estimated for a concurrent hollow fibre membrane module for given pressure and temperature conditions and different values of stage cut. The obtained results show good agreement with the experimental data. The highest degree of methane recovery was obtained with gas concentrating in a cascade with recycling of the retentate.
引用
收藏
页码:235 / 260
页数:26
相关论文
共 51 条
  • [1] Performance of natural gas membranes in the presence of heavy hydrocarbons
    Al-Juaied, M
    Koros, WJ
    [J]. JOURNAL OF MEMBRANE SCIENCE, 2006, 274 (1-2) : 227 - 243
  • [2] Morphology and permeation properties of polysulfone membranes for gas separation: Effects of non-solvent additives and co-solvent
    Aroon, M. A.
    Ismail, A. F.
    Montazer-Rahmati, M. M.
    Matsuura, T.
    [J]. SEPARATION AND PURIFICATION TECHNOLOGY, 2010, 72 (02) : 194 - 202
  • [3] Natural gas processing with membranes: An overview
    Baker, Richard W.
    Lokhandwala, Kaaeid
    [J]. INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2008, 47 (07) : 2109 - 2121
  • [4] MEMBRANE PROCESSES FOR THE REMOVAL OF ACID GASES FROM NATURAL-GAS .1. PROCESS CONFIGURATIONS AND OPTIMIZATION OF OPERATING-CONDITIONS
    BHIDE, BD
    STERN, SA
    [J]. JOURNAL OF MEMBRANE SCIENCE, 1993, 81 (03) : 209 - 237
  • [5] New concepts in anaerobic digestion processes: recent advances and biological aspects
    Castellano-Hinojosa, Antonio
    Armato, Caterina
    Pozo, Clementina
    Gonzalez-Martinez, Alejandro
    Gonzalez-Lopez, Jesus
    [J]. APPLIED MICROBIOLOGY AND BIOTECHNOLOGY, 2018, 102 (12) : 5065 - 5076
  • [6] Membrane enrichment of biogas from two-stage pilot plant using agricultural waste as a substrate
    Chmielewski, Andrzej G.
    Urbaniak, Agata
    Wawryniuk, Katarzyna
    [J]. BIOMASS & BIOENERGY, 2013, 58 : 219 - 228
  • [7] HYDRAULIC MIXING MODELLING IN REACTOR FOR BIOGAS PRODUCTION
    Chmielewski, Andrzej G.
    Berbec, Aleksandra
    Zalewski, Michal
    Dobrowolski, Andrzej
    [J]. CHEMICAL AND PROCESS ENGINEERING-INZYNIERIA CHEMICZNA I PROCESOWA, 2012, 33 (04): : 621 - 628
  • [8] Modeling multicomponent gas separation using hollow-fiber membrane contactors
    Coker, DT
    Freeman, BD
    Fleming, GK
    [J]. AICHE JOURNAL, 1998, 44 (06) : 1289 - 1302
  • [9] Optimization of membrane unit for removing carbon dioxide from natural gas
    Datta, Anjan K.
    Sen, Pradip K.
    [J]. JOURNAL OF MEMBRANE SCIENCE, 2006, 283 (1-2) : 291 - 300
  • [10] Techno-economic evaluation of biogas upgrading process using CO2 facilitated transport membrane
    Deng, Liyuan
    Hagg, May-Britt
    [J]. INTERNATIONAL JOURNAL OF GREENHOUSE GAS CONTROL, 2010, 4 (04) : 638 - 646