کد مقاله | کد نشریه | سال انتشار | مقاله انگلیسی | نسخه تمام متن |
---|---|---|---|---|
5012356 | 1462811 | 2017 | 27 صفحه PDF | دانلود رایگان |
عنوان انگلیسی مقاله ISI
Energy-environment-economic investigations on evacuated active multiple stage series flow solar distillation unit for potable water production
ترجمه فارسی عنوان
تحقیقات انرژی-محیط زیست-اقتصادی بر روی واحد خنک کن خورشیدی چند مرحله ای سری تخلیه خورشیدی برای تولید آب آشامیدنی
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کلمات کلیدی
انرژی، محیط زیست و تجزیه و تحلیل اقتصادی، انرژی خورشیدی، تقطیر خنک کننده چند مرحله فعال، تولید آب آشامیدنی، کاهش تدریجی انتشار،
موضوعات مرتبط
مهندسی و علوم پایه
مهندسی انرژی
انرژی (عمومی)
چکیده انگلیسی
Multi stage solar distillation units are well known for their higher distillate productivity and are capable of fulfilling the potable water requirements of families in remote, rural, and coastal regions. In this article, active multiple stage series flow solar distillation unit has been proposed for desalting saline water and its performance, environmental benefits and economic feasibility were assessed by carrying out 3E (Energy-Environment-Economic) analyses using the developed mathematical model. Better performance was observed for the distillation unit with five distillation stages, two solar collectors connected in parallel configuration and saline water mass flow rate of 135.0Â kg/d and 75.0Â kg/d, during summer and winter seasons. Low-pressure operation in combination with evaporative cooling of condenser of last stage has enhanced the annual average daily distillate productivity from 12.60Â kg/d to 48.80Â kg/d. Distillate production was found to drop from 48.80Â kg/d to 38.90Â kg/d with the increase in salt concentration of saline water from 0Â wt% to 10Â wt%. Energy payback time of the unit desalting saline water with 5Â wt% salt concentration was within 1.0Â yr and the unit can mitigate nearly 221.80 tons of CO2 emission, 1594.73Â kg of SO2 emission and 651.37Â kg of NO emission from Indian coal based power plants during its 20Â yrs lifespan under 250 clear day operation. Increased salt concentration in saline water reduces the emission mitigation potential and increases the energy payback time of the proposed distillation unit. Distillate production cost was increased by 16.0% for every 5Â wt% increase in salt concentration. Amount invested in the unit can be regained with in 3.56Â yr irrespective of interest rate for distilled water selling price of 0.06Â USD/L (Rs. 3.91/L).
ناشر
Database: Elsevier - ScienceDirect (ساینس دایرکت)
Journal: Energy Conversion and Management - Volume 151, 1 November 2017, Pages 259-285
Journal: Energy Conversion and Management - Volume 151, 1 November 2017, Pages 259-285
نویسندگان
K.S. Reddy, H. Sharon,