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المؤلفJoel, Minier-Matar
المؤلفAl-Maas, Mashael
المؤلفDardor, Dareen
المؤلفJanson, Arnold
المؤلفNasser, Mustafa S.
المؤلفAdham, Samer
تاريخ الإتاحة2022-09-12T06:01:46Z
تاريخ النشر2021-04-30
اسم المنشورJournal of Water Process Engineering
المعرّفhttp://dx.doi.org/10.1016/j.jwpe.2020.101760
الاقتباسMinier-Matar, J., Al-Maas, M., Dardor, D., Janson, A., Nasser, M. S., & Adham, S. (2021). Industrial wastewater volume reduction through osmotic concentration: Membrane module selection and process modeling. Journal of Water Process Engineering, 40, 101760.‏
الرقم المعياري الدولي للكتاب22147144
معرّف المصادر الموحدhttps://www.sciencedirect.com/science/article/pii/S2214714420306371
معرّف المصادر الموحدhttp://hdl.handle.net/10576/33851
الملخصOsmotic concentration (OC), a form of forward osmosis (FO) but without draw solution recovery, can be applied for reducing wastewater disposal volumes in the oil & gas industry. Within this industry, wastewater is often disposed of by injection through disposal wells into deep underground reservoirs. By reducing wastewater disposal volumes, the sustainability of the disposal reservoir is improved. In this application of OC, seawater or brine from a desalination plant serves as the draw solution and the diluted seawater is discharged to the sea. This study compared 3 commercial hollow-fiber FO membranes (CTA, TFC, aquaporin proteins) for reducing the volume of low salinity wastewater generated during liquified natural gas (LNG) production. Additionally, a model was developed to predict the performance of commercial full-scale membranes by identifying optimum operating conditions, taking into consideration the trade-off between feed concentration factor and water flux. Bench-scale tests were conducted using synthetic and actual wastewater from an LNG facility to evaluate OC technology performance and validate model predictions.Based on model results with a feed mimicking the salinity of actual wastewater, a 4x concentration factor produced a reasonable compromise between feed recovery and draw solution dilution and was considered the optimum for future tests. At higher concentration factors, the increased dilution of the draw solution negatively impacted flux. In bench tests with real wastewater, the TFC chemistry had a ≈5x higher water flux (9.7 vs. 1.9 L/m2-h) and a ≈3x lower specific reverse solute flux (192 vs. 551 mg/L) compared to the CTA chemistry. However, both membranes showed less than 5% fouling and a specific forward organic solute flux of less than 0.5 mg/L of total organic carbon (TOC). Pilot testing for >50 h showed stable performance, comparable to bench scale data and model predictions.
اللغةen
الناشرElsevier Ltd
الموضوعOsmotic concentration
Forward osmosis
Wastewater treatment
Oil and gas
Seawater
Bench scale
Pilot plant
العنوانIndustrial wastewater volume reduction through osmotic concentration: Membrane module selection and process modeling
النوعArticle
رقم المجلد40
Open Access user License http://creativecommons.org/licenses/by/4.0/
dc.accessType Open Access


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