4.7 Article

PDMS membranes for feasible recovery of dissolved methane from AnMBR effluents

Journal

JOURNAL OF MEMBRANE SCIENCE
Volume 604, Issue -, Pages -

Publisher

ELSEVIER
DOI: 10.1016/j.memsci.2020.118070

Keywords

Anaerobic membrane bioreactor (AnMBR); Greenhouse gas (GHG); Methane recovery; PDMS degassing Membrane; Urban wastewater

Funding

  1. Generalitat Valenciana [CPI-16-155, C12747]
  2. Ministerio de Economia y Competitividad via Juan de la Cierva [FJCI-2014-21616]
  3. European financial instrument for the Environment (LIFE+) [LIFE13 ENV/ES/001353]

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This study aimed to evaluate the feasibility of degassing membrane (DM) technology for recovering dissolved methane from AnMBR effluents. For that purpose, a PDMS membrane module was operated for treating the effluent from an AnMBR prototype-plant, which treated urban wastewater (UWW) at ambient temperature. Different transmembrane pressures and liquid flow rates were applied for evaluating methane recovery efficiency. Maximum methane recoveries were achieved when increasing the vacuum pressure and reducing the liquid flow rate, reaching a maximum methane recovery efficiency of around 80% at a transmembrane pressure (TMP) of 0.8 bars and a treatment flow rate (Q(L)) of 50 L h(-1). The results revealed that the combination of PDMS DMs and AnMBR technology would allow to reduce the energy demand of UWW treatment, achieving net energy productions while reducing greenhouse gas emissions. Optimum operation was determined at a TMP of 0.8 bars and a Q(L) of 150 L h(-1) when combining energy, environmental and economic targets. Under these operating conditions, the combination AnMBR + DM resulted in energy requirements and greenhouse gases emissions of -0.040 kWh and 0.113 kg of CO2-eq per m(3) of treated water, respectively, resulting in a DM payback period of around 10.5 years.

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