کد مقاله کد نشریه سال انتشار مقاله انگلیسی نسخه تمام متن
623063 1455324 2015 16 صفحه PDF دانلود رایگان
عنوان انگلیسی مقاله ISI
Application of advanced thermodynamics, thermoeconomics and exergy costing to a Multiple Effect Distillation plant: In-depth analysis of cost formation process
ترجمه فارسی عنوان
استفاده از ترمودینامیک پیشرفته، اقتصاد گرماسنجی و هزینه های اضافی برای کارخانه تقطیر چندگانه: تجزیه و تحلیل عمق فرایند شکل گیری هزینه
کلمات کلیدی
ارزیابی اگزرژی، اقتصادسنجی تبخیر اثر چندگانه، روند شکل گیری هزینه، اگزرژی شیمیایی، اگزرژی حرارتی
موضوعات مرتبط
مهندسی و علوم پایه مهندسی شیمی تصفیه و جداسازی
چکیده انگلیسی


• A forward feed Multiple Effect Distillation plant is examined.
• An exergy analysis is performed at single effect and at subprocess levels.
• A thermoeconomic model is developed, that includes “residue” exergy flows.
• Specific costs are calculated for each chemical and thermal exergy flow.
• Asymmetries are found in the unit cost of distillate produced in different effects.

The high thermal energy consumption per m3 fresh water is one of the main barriers to the spread of thermally driven desalination processes and has limited their use to applications in countries with high reserves of fossil fuels or to specific technological solutions like dual purpose cogeneration plants and solar desalination systems. Being energy conversion efficiency a major issue to improve the performance of thermally driven desalination plants, thermoeconomic analysis has been attracting the efforts of researchers for the identification of margins for process improvement. In this paper a rigorous exergy and thermoeconomic analysis is presented for an 8 effect forward feed Multiple Effect Distillation plant, based on models developed in Engineering Equation Solver. The innovative contribution lies in the detailed methodological formulation with explicative notes on the main assumptions and in the high level of disaggregation used, which allows us to follow each specific subprocess and thus to acquire an in-depth understanding of the whole cost formation process. The results indicate that the monetary value associated with the physical and chemical exergy flows highly vary throughout the plant and that the contribution to the final cost of fresh water is higher for the distillate produced in the last effects.

ناشر
Database: Elsevier - ScienceDirect (ساینس دایرکت)
Journal: Desalination - Volume 371, 1 September 2015, Pages 88–103
نویسندگان
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