Enhancing Water Purification Performance through Reverse Osmosis at the Genaveh Combined Cycle Power Plant: A Study on Salt Rejection and Permeate Flow Rate Optimization

سال انتشار: 1403
نوع سند: مقاله ژورنالی
زبان: انگلیسی
مشاهده: 178

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شناسه ملی سند علمی:

JR_IJCCE-43-11_016

تاریخ نمایه سازی: 16 خرداد 1404

چکیده مقاله:

The global scarcity of fresh water and the extensive use of Reverse Osmosis (RO) systems for drinking water production necessitates optimizing operational conditions to enhance membrane lifespan and water quality. This study investigates the factors affecting the efficiency of the RO process at the Genaveh Combined Cycle Power Plant to optimize water purification (reducing electrical conductivity). The impact of pressure, temperature, recovery rate, and Total Dissolved Solids (TDS) concentration of feed water on salt rejection and permeate flow rate was examined. Regarding the rate of salt rejection, changes in the concentration of Ca۲+, Mg۲+, Na+, SO۴۲-, NO۳-, and SiO۲- ions were investigated and measured using titration methods, an online sodium meter, and a spectrophotometer. Results indicate that feed water pressure significantly influences permeate flow rate, with a linear increase from ۲۷.۱ to ۳۲ m³/hr as pressure rises from ۱۰ to ۱۸ bar, peaking at ۱۸ bar. This increase in pressure also enhances salt rejection, as evidenced by the rising ion removal rate. Improving feed water temperature from ۱۷ ͦ C to ۳۵ ͦ C increases permeate flow rate, indicating a direct relationship, while the trend of ion removal decreases with temperature. An increase in the TDS concentration from ۷۱۰ to ۸۷۵ ppm results in a decrease in the permeate flow rate. Additionally, a decreasing trend is observed in the percentage change of pure water recovery compared to the permeate flow rate and ion removal. These findings provide valuable insights for optimizing RO system performance in water treatment processes

کلیدواژه ها:

Genaveh Combined Cycle Power Plant ، Reverse osmosis ، ion ، cellulose acetate ، pure water recycling percentage ، feed water salt ، permeate flow

نویسندگان

Mehran Rezvani Ardakani

Department of Chemical Engineering, Kherad Institute of Higher Education, Bushehr, I.R. IRAN

Samer Asadi

Department of Chemical Engineering, Kherad Institute of Higher Education, Bushehr, I.R. IRAN

Mohsen Abasi

Department of Chemical Engineering, Faculty of Petroleum, Gas and Petrochemical Engineering, Persian Gulf University, ۷۵۱۶۹, Bushehr, I.R. IRAN

Somayeh Lashgari

Petrochemical Research and Technology Company - PO ۱۴۳۵۸۸۴۷۱۱, Tehran, I.R. IRAN

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