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Please use this identifier to cite or link to this item: http://hdl.handle.net/11375/28487
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dc.contributor.advisorKim, Younggy-
dc.contributor.authorPanagoda, Sandali-
dc.date.accessioned2023-05-02T18:21:20Z-
dc.date.available2023-05-02T18:21:20Z-
dc.date.issued2023-06-
dc.identifier.urihttp://hdl.handle.net/11375/28487-
dc.description.abstractContamination of natural waters due to nitrogenous wastes has become a crucial environmental problem due to deterioration of water quality and eutrophication in aquatic eco-systems. Thus, the reduction of nitrogen accumulation in the natural environment is vital to maintain a healthy eco-system. Bipolar membrane electrodialysis (BMED) is a promising technology for selective ammonia separation from high-strength wastewater, such as liquid digestates of food waste or wastewater sludge. This technology was recently studied for reducing membrane scaling problems associated with conventional electrodialysis (ED) systems due to the water splitting mechanism in the BPM interface. A bench-scale BMED stack was built using 5 pairs of cation exchange membranes (CEMs) and bipolar membranes (BPMs). Using the BMED stack, a simulated food liquid digestate solution was examined to separate ammonia with different voltage applications and inter-membrane distances. The highest ammonia recovery was obtained at a cell pair voltage of 5.83 V (81% separation). Experiments on investigation of optimal inter-membrane distance of BMED operation suggested that the inter-membrane distance could be increased up to 2.46 mm without a significant decrease in nitrogen recovery. The residual Ca2+ and Mg2+ in the CIP (clean-in-place) solution which explains the degree of the scaling problem in the BMED was observed consistently below 2% of the initial mass introduced to the system, indicating that BMED design and regular CIP were effective in scaling control. The ammonia loss through CEMs to the feed cell by back diffusion was minimized due to high pH in the base cell since uncharged free ammonia was dominant over ammonium cation in the base cell. The energy required for BMED operation was comparatively low; 1.93-6.93 kWh/kg-N within 90 mins. Therefore, BMED can be considered as a sustainable candidate for selective ammonia recovery at high energy efficiency with successful scaling control.en_US
dc.language.isoenen_US
dc.subjectBipolar membrane electrodialysis, Ammonia recovery, Eutrophicationen_US
dc.titleAmmonia recovery from simulated food liquid digestate using bipolar membrane electrodialysisen_US
dc.typeThesisen_US
dc.contributor.departmentCivil Engineeringen_US
dc.description.degreetypeThesisen_US
dc.description.degreeMaster of Civil Engineering (MCE)en_US
Appears in Collections:Open Access Dissertations and Theses

Files in This Item:
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Final-Thesis-Submission-Sheet.pdf
Embargoed until: 2099-01-01
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License-to-McMaster Sandali Panagoda.pdf
Embargoed until: 2099-01-01
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Thesis - Sandali Panagoda.pdf
Access is allowed from: 2024-04-28
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