Simulation and optimization Distillation Tower in Phases 2 and 3 of South Pars

سال انتشار: 1393
نوع سند: مقاله کنفرانسی
زبان: انگلیسی
مشاهده: 599

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شناسه ملی سند علمی:

CBGCONF02_285

تاریخ نمایه سازی: 9 فروردین 1395

چکیده مقاله:

Distillation process is the commonest process for separating material and on the other hand it is the most expensive unit in terms of energy consumption. This process has a significant proportion of energy in the industry. Thus, according to the uncontrolled increase in consuming energy as well as global energy prices, the attempts to find ways to save energy in the distillation process is of very importance. This study investigates energy recovery for condenser of the stabilization tower (South Pars Phases 2 and 3) by using thermal integration.The tower condenser is originally air conditioner that consumes 3 megawatts electrical power for the overhead vapor condensation to the temperature of 55 ° C Per hour. The cost of the production of this amount of energy is considerable. Based on the thermal integration, the amount of feeding energy due to its low temperature is suitable for condensing and even one can improve the condensing temperature to 25 ° C. In this paper, by replacing heat exchanger with current air conditioner and by using food as condensation factor, excellent results were obtained. In case of using the integration, 3942 GJ electric power will be saved annually, the current air conditioner will be remove from the process and a good profit will obtained for this operating Unit through reducing the cost of electricity supply of condenser.

نویسندگان

Mohsen darabi

Azad University Shahrood, Department Of Chemical Engineering, Shahrood, Iran

hamid mohammadiun

assistant professor,department of mechanical engineering,shahrood branch,Islamic azad university,shahrood,iran

mostafa montazeri

Azad University Shahrood, Department Of Chemical Engineering, Shahrood, Iran

reza naeimi

process expert oil refinery of abadan

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  • M.SL. Lababidi, I.M. Alatiqi, L.J. Nayfeh, "Energy retrofits study of ...
  • Pinch Technology: Basics for the Beginners, _ cheresources _ ...
  • M.M. El-Halwagi, V. M anousiouthak _ "Synthesis of Mass Exchanger ...
  • M.S.L. Lababidi, I.M. Alatiqi, L. Nayfeh, "Energy retrofits study of ...
  • Pinch Technology: Basics for the Beginners, _ cheresources _ ...
  • M.M. El-Halwagi, Polley, "Synthesis of Mass Exchanger Network", AIChE J., ...
  • D.R. Morris, " Exergy analysis and cumulatie exergy consumption of ...
  • J. Szargut, D.R. Morris, F.R .Steward, Exergy Analysis of Thermal, ...
  • A.C. Neto, P. Pilidis, "An Exergy Analysis of Novel Power ...
  • Towler .P. "Integrated process design for improved energy efficiency." Linh ...
  • Mathur.R.M. "Process Integration through Pinch Analysis", User Guide on Process ...
  • Shenoy, U.V., Sinha, A. and Bandy opadhyay, S. (1998) "Multiple ...
  • Lee, "Application of exergy and Pinch analysis on oleochemical fractionation ...
  • Documents of south pars field deve lopment-pha ses 2&3 , ...
  • نمایش کامل مراجع