Download | - View accepted manuscript: Design and economics of a hybrid membrane–temperature swing adsorption process for upgrading biogas (PDF, 915 KiB)
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DOI | Resolve DOI: https://doi.org/10.1016/j.memsci.2012.02.040 |
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Author | Search for: Shao, Pinghai1; Search for: Dal-cin, Mauro1; Search for: Kumar, Ashwani1; Search for: Li, Haibin; Search for: Singh, Davinder Paul |
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Affiliation | - National Research Council of Canada. NRC Institute for Chemical Process and Environmental Technology
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Format | Text, Article |
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Subject | Process design and optimization; hollow fiber membrane; pressure ratio; recycling; biogas emission; capital and operating cost; economic analysis |
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Abstract | Processing biogas from wastewater digesters allows recovery of valuable methane and reduction in green house gas emissions. A two-stage membrane process, coupled with a temperature-swing-adsorption (TSA) as pre-treatment, was designed to generate pipeline quality methane. To improve methane recovery and process energy efficiency, the non-product streams of the membrane process were recycled and the permeate of the first membrane stage was maintained at a given pressure as the driving force for second membrane stage. The membrane process design was optimized by minimizing the objective function; the overall processing cost. It was found the membrane approach excels the PSA for producing pipeline quality methane (97% purity) in terms of methane recovery, processing cost and lower emissions. A techno-economic analysis showed that the payback time for an operation processing 200 Nm(3)/h of biogas was 6.8 months. |
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Publication date | 2012-03-01 |
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In | |
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Language | English |
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Peer reviewed | Yes |
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Identifier | S0376738812001561 |
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NRC number | NRCC 53059 |
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NPARC number | 21268481 |
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Export citation | Export as RIS |
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Report a correction | Report a correction (opens in a new tab) |
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Record identifier | 95c322c7-6a0a-4d89-a4d8-99b1e01d45a3 |
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Record created | 2013-07-26 |
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Record modified | 2020-06-04 |
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