Advanced Exergoeconomic Analysis of C۳MR, MFC and DMR ‎Refrigeration Cycles in an Integrated Cryogenic Process

Publish Year: 1397
نوع سند: مقاله ژورنالی
زبان: English
View: 205

This Paper With 31 Page And PDF Format Ready To Download

  • Certificate
  • من نویسنده این مقاله هستم

استخراج به نرم افزارهای پژوهشی:

لینک ثابت به این Paper:

شناسه ملی سند علمی:

JR_GPJU-6-1_004

تاریخ نمایه سازی: 23 مرداد 1400

Abstract:

C۳MR, MFC, and DMR processes in an integrated LNG-NGL-NRU structure are investigated using the conventional and advanced exergy and exergoeconomic analyses. The results of advanced exergy analysis reveal that in most of the equipment, the highest amount of irreversibility is occurred because of endogenous exergy destruction. In C۳MR process, compressor C۵ with ۹۷۳۰ kW; in MFC process, compressor C۱ with ۶۳۴۲ kW; and in DMR process, compressor C۳ with ۱۰۰۰۸ kW; have the most amount of avoidable endogenous exergy destruction in comparison with the other equipment. According to the advanced exergoeconomic analysis, the amount of endogenous part of exergy destruction cost and investment cost is higher than the exogenous part for most of the equipment, representing that interactions among the equipment is not considerable. Compressors have the highest amount of avoidable endogenous investment cost in all of the processes. Furthermore, in C۳MR process, HX۲ heat exchanger with ۱۱۲۱ /h; in MFC process, compressor C۱ with ۴۵۰ /h; and in DMR process, HX۳ heat exchanger with ۳۹۵۵ /h; have the most amount of avoidable endogenous exergy destruction cost. Based on total costs defined for the equipment, in C۳MR process, HX۲ heat exchanger with ۱۱۲۶ /h should be modified. In MFC process, compressor C۱ with ۵۰۴.۷ /h should be considered. In DMR process, HX۳ heat exchanger with ۳۹۶۳ /h should be improved its performance. Finally, sensitivity analysis as well as validation have been conducted, and three different strategies are used to reduce the cost of avoidable exergy destruction of system equipment.

Authors

Vahid Ghazizadeh

Mechanical Engineering, K. N. Toosi University of Technology, Tehran, Iran

Bahram Ghorbani

Amol University of Special Modern Technologies

Reza Shirmohammadi

Department of Renewable Energies and Environment, Faculty of New Sciences & Technologies, University of Tehran, Tehran, Iran

Mehdi Mehrpooya

Department of Renewable Energies and Environment, Faculty of New Sciences & Technologies, University of Tehran, Tehran, Iran

Mohammad Hosein Hamedi

Mechanical Engineering, K. N. Toosi University of Technology, Tehran, Iran

مراجع و منابع این Paper:

لیست زیر مراجع و منابع استفاده شده در این Paper را نمایش می دهد. این مراجع به صورت کاملا ماشینی و بر اساس هوش مصنوعی استخراج شده اند و لذا ممکن است دارای اشکالاتی باشند که به مرور زمان دقت استخراج این محتوا افزایش می یابد. مراجعی که مقالات مربوط به آنها در سیویلیکا نمایه شده و پیدا شده اند، به خود Paper لینک شده اند :
  • Abbassi, A., & Aliehyaei, M. (۲۰۰۴). Exergy method of optimisation ...
  • Açıkkalp, E., Aras, H., & Hepbasli, A. (۲۰۱۴). Advanced exergoeconomic ...
  • Aghniaey, S., & Mahmoudi, S. M. S. (۲۰۱۴). Exergy analysis ...
  • Ansarinasab, H., & Mehrpooya, M. (۲۰۱۷a). Advanced exergoeconomic analysis of ...
  • Ansarinasab, H., & Mehrpooya, M. (۲۰۱۷b). Evaluation of novel process ...
  • Ashouri, M., Ahmadi, M. H., Pourkiaei, S. M., Astaraei, F. ...
  • Aslani, A., Akbari, S., & Tabasi, S. (۲۰۱۸). The Robustness ...
  • Bejan, A., & Tsatsaronis, G. (۱۹۹۶). Thermal design and optimization: ...
  • Bellos, E., Tzivanidis, C., & Antonopoulos, K. A. (۲۰۱۶). Exergetic ...
  • Cuellar, K. T., Wilkinson, J. D., Hudson, P. H. M., ...
  • Davarpanah, A., Mirshekari, B., Behbahani, T. J., & Hemati, M. ...
  • Ding, H., Sun, H., Sun, S., & Chen, C. (۲۰۱۷). ...
  • Ghorbani, B., Hamedi, M.-H., & Amidpour, M. (۲۰۱۶). Exergoeconomic Evaluation ...
  • Ghorbani, B., Hamedi, M.-H., Amidpour, M., & Mehrpooya, M. (۲۰۱۶). ...
  • Ghorbani, B., Mafi, M., Amidpour, M., Nayenian, M., & Salehi, ...
  • Ghorbani, B., Mehrpooya, M., Hamedi, M.-H., & Amidpour, M. (۲۰۱۷). ...
  • Ghorbani, B., Shirmohammadi, R., Mehrpooya, M., & Mafi, M. (۲۰۱۸). ...
  • Kelly, S., Tsatsaronis, G., & Morosuk, T. (۲۰۰۹). Advanced exergetic ...
  • Khademi, M., Jafarkazemi, F., Ahmadifard, E., & Younesnejad, S. (۲۰۱۳). ...
  • Khan, M. S., Chaniago, Y. D., Getu, M., & Lee, ...
  • Mazarei, M., Davarpanah, A., Ebadati, A., & Mirshekari, B. (۲۰۱۸). ...
  • Mehdizadeh-Fard, M., Pourfayaz, F., Mehrpooya, M., & Kasaeian, A. (۲۰۱۸). ...
  • Mehrpooya, M., & Ansarinasab, H. (۲۰۱۵b). Advanced exergoeconomic evaluation of ...
  • Mehrpooya, M., Ansarinasab, H., Sharifzadeh, M. M. M., & Rosen, ...
  • Mehrpooya, M., Hossieni, M., & Vatani, A. (۲۰۱۴). Novel LNG-based ...
  • Mehrpooya, M., Jarrahian, A., & Pishvaie, M. R. (۲۰۰۶). Simulation ...
  • Mehrpooya, M., & Shafaei, A. (۲۰۱۶). Advanced exergy analysis of ...
  • Moharamian, A., Soltani, S., Rosen, M. A., & Mahmoudi, S. ...
  • Peters, M. S., Timmerhaus, K. D., West, R. E., Timmerhaus, ...
  • Petrakopoulou, F., Tsatsaronis, G., & Morosuk, T. (۲۰۱۳). Evaluation of ...
  • Petrakopoulou, F., Tsatsaronis, G., Morosuk, T., & Carassai, A. (۲۰۱۲). ...
  • Qualls, W., Ransbarger, W., Huang, S., Yao, J., Elliot, D., ...
  • Raj, R., Suman, R., Ghandehariun, S., Kumar, A., & Tiwari, ...
  • Ransbarger, W. L. (۲۰۰۶). Intermediate pressure LNG refluxed NGL recovery ...
  • Roberts, M. J., & Rowles, H. C. (۲۰۰۳). Integrated high ...
  • Romeo, L. M., Usón, S., Valero, A., & Escosa, J. ...
  • Shariati Niasar, M., Amidpour, M., Ghorbani, B., Rahimi, M.-J., Mehrpooya, ...
  • Shirmohammadi, R., Soltanieh, M., & Romeo, L. M. (۲۰۱۸). Thermoeconomic ...
  • Vatani, A., Mehrpooya, M., & Tirandazi, B. (۲۰۱۳). A novel ...
  • نمایش کامل مراجع