کد مقاله کد نشریه سال انتشار مقاله انگلیسی نسخه تمام متن
5477160 1399212 2016 10 صفحه PDF دانلود رایگان
عنوان انگلیسی مقاله ISI
Methodology for the optimal design of an integrated sugarcane distillery and cogeneration process for ethanol and power production
ترجمه فارسی عنوان
روش شناسی برای طراحی بهینه یک مجتمع نوشابه گازدار و فرآیند تولید انرژی اتانول و تولید برق
کلمات کلیدی
نوشیدنی قنادی و تولید انرژی، شبیه سازی، یکپارچگی حرارت، ارزیابی حرارتی اقتصادی، بهینه سازی دو جانبه تکاملی، حداکثر سودآوری،
موضوعات مرتبط
مهندسی و علوم پایه مهندسی انرژی انرژی (عمومی)
چکیده انگلیسی

:
- Methodology for optimal design of sugarcane to ethanol and power plant.
- Process simulation, heat integration and thermo-economic evaluation model.
- Bi-objective multi-variable evolutionary optimization and analysis of results.
- NPV maximization for selecting point for different economic scenarios.
- Analysis and characterization of optimal point.

The application of systematic methodologies for the optimal design of integrated processes has seen increased interest in literature, namely for bioprocesses. The development and application of such a methodology to ethanol and power production from sugarcane and leaves, in a combined distillery and cogeneration plant is investigated in this article. The methodology breaks down as follows: process simulation, heat integration and thermo-economic evaluation, bi-objective multi-variable evolutionary optimization, and process selection. The objective functions are exergy efficiency and capital cost, whereas the selection criterion is the maximization of the Net Present Value (NPV). This choice was motivated by the variation in process related market parameters and their impact on profitability. Optimization generated 31 optimal trade-off solutions with better results than literature. Exergy efficiency ranged between 37.6% and 41.7% and capital costs between 155 M$ and 210 M$. Process selection led to a single configuration maximizing NPV for four economic scenarios. The configuration's exergy efficiency and capital costs were equal to 40.63% and 163 M$. This point presented an optimal compromise between heat integration and capital costs. This article provides a breakthrough in the application of this methodology, to the investigated process specifically.

ناشر
Database: Elsevier - ScienceDirect (ساینس دایرکت)
Journal: Energy - Volume 117, Part 2, 15 December 2016, Pages 540-549
نویسندگان
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