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شبیه‌سازی عددی و مطالعه نظری تأثیر پارامترهای عملیاتی در تقطیر غشایی در خلأ | ||
| مدل سازی در مهندسی | ||
| مقاله 4، دوره 16، شماره 55، دی 1397، صفحه 41-49 اصل مقاله (946.03 K) | ||
| نوع مقاله: مقاله شیمی | ||
| شناسه دیجیتال (DOI): 10.22075/jme.2018.4902. | ||
| نویسندگان | ||
| مرتضی اصغری* ؛ شیرین قربان لوینه؛ مجتبی راجی | ||
| آزمایشگاه پژوهشس فرآیندهای جداسازی- SPRG | ||
| تاریخ دریافت: 06 آذر 1392، تاریخ بازنگری: 14 فروردین 1397، تاریخ پذیرش: 26 فروردین 1397 | ||
| چکیده | ||
| خلیج فارس و مناطق ساحلی آن بزرگترین منبع نفت خام در جهان محسوب می‌شوند. از طرفی، گرمای هدر رفته از صنایع پالایش و پتروشیمی که در محدوده اطراف خلیج‌فارس قرار گرفته‌اند، می‌تواند براساس شرایط ساده خوراک ورودی در تقطیر غشایی، مورد استفاده قرار بگیرد. از این رو، به منظور بهبود عملکرد این سیستم در نمک‌زدایی از آب خلیج فارس و افزایش شار خروجی، مدل انتقال جرم و حرارت به طور همزمان در یک سیستم تقطیر غشایی در خلآ ارائه و با داده های تجربی اعتبارسنجی شده است. تأثیر شرایط عملیاتی مختلف نظیر دمای خوراک، فشار خلأ در سمت تراویده، غلظت خوراک و ضریب انتقال حرارت بر شار تراوش‌شده مورد بررسی قرار گرفته است. همچنین، اثر دمای خوراک بر پدیده قطبش دمایی مطالعه شده است. نتایج نشان دادند که شار تراوش‌شده با افزایش دمای خوراک و ضریب انتقال حرارت افزایش و با افزایش فشار خلأ و غلظت خوراک کاهش پیدا می‌کند. همچنین مشخص شد که افزایش دما اثر نامطلوب پدیده قطبش دمایی را افزایش خواهد داد. | ||
| کلیدواژه‌ها | ||
| تقطیر غشایی در خلا؛ شبیه سازی عددی؛ انتقال جرم؛ شار تراوه؛ پلاریزاسیون دمایی | ||
| عنوان مقاله [English] | ||
| Numerical simulation and theoretical study on effects of operating parameters in Persian Gulf desalination using vacuum membrane distillation | ||
| نویسندگان [English] | ||
| Morteza Asghari؛ Shirin Gh. Lovineh؛ Mojtaba Raji | ||
| چکیده [English] | ||
| The Persian Gulf and its coastal areas are considered to be the largest source of crude oil in the world. On the other hand, the waste heat from the refining and petrochemical industries located around the Persian Gulf region can be used based on simple feed conditions for membrane distillation. Therefore, in order to improve the performance of this system in the desalination of Persian Gulf water and increase the flux of output, the mass and heat transfer model is simultaneously introduced into a membrane distillation system and validated with experimental data. The effect of different operating conditions such as feed temperature, vacuum pressure on the permeate side, feed concentration and heat transfer coefficient on the flux permeated have been investigated. Also, the effect of feed temperature on the temperature polarization phenomenon has been studied. The results showed that permeate flux increased with increasing feed temperature and heat transfer coefficient and decreased with increasing vacuum pressure and feed concentration. It was also found that the temperature increase would have an adverse effect on the phenomenon of temperature polarization. | ||
| کلیدواژه‌ها [English] | ||
| Vacuum membrane distillation, Numerical simulation, Mass transfer, Permeate Flux, Temperature polarization | ||
| مراجع | ||
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