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Preliminary techno‐economic analysis of a multi‐bed series reactor as a simultaneous CF 4 abatement and utilization process

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  • Boreum Lee
  • Seonju Jeong
  • Sunggeun Lee
  • Ho‐Young Jung
  • Shin‐Kun Ryi
  • Hankwon Lim

Abstract

A preliminary techno‐economic analysis combining process simulation and economic analysis has been carried out to assess the feasibility of employing a new CF 4 abatement and utilization process without HF effluent, where CaO was employed to convert produced HF into CaF 2 , a useful chemical. Moreover, the effect of employing multi‐bed series reactors compared with a single‐bed reactor on CaF 2 production was analyzed using Aspen HYSYS-super-® based on material and energy balances from process flow diagrams for three systems, a single‐bed reactor (S‐1), a two‐bed series reactor (S‐2), and a three‐bed series reactor (S‐3). From economic analysis to estimate annual operating cost savings for three systems, it was found that multi‐bed series reactors (S‐2 and S‐3) performed better than a single‐bed reactor (S‐1) due to equilibrium shift by Le Chatelier's principle leading to reduced operating temperatures to produce the same amount of CaF 2 as S‐1. Consequently, annual cost savings of about 7 to 13% were obtained in S‐2 and S‐3 compared to S‐1 and this can serve as a useful guideline for the efficient system design. © 2017 Society of Chemical Industry and John Wiley & Sons, Ltd.

Suggested Citation

  • Boreum Lee & Seonju Jeong & Sunggeun Lee & Ho‐Young Jung & Shin‐Kun Ryi & Hankwon Lim, 2017. "Preliminary techno‐economic analysis of a multi‐bed series reactor as a simultaneous CF 4 abatement and utilization process," Greenhouse Gases: Science and Technology, Blackwell Publishing, vol. 7(3), pages 542-549, June.
    • Handle: RePEc:wly:greenh:v:7:y:2017:i:3:p:542-549
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    File URL: http://hdl.handle.net/10.1002/ghg.1661
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    1. Jae†Yun Han & Chang†Hyun Kim & Boreum Lee & Seonju Jeong & Hankwon Lim & Kwan†Young Lee & Shin†Kun Ryi, 2017. "Experimental and simulation studies for reaction enhancement of catalytic CF4 hydrolysis by consecutive HF removal using a multi†stage catalyst†adsorbent reactor," Greenhouse Gases: Science and Technology, Blackwell Publishing, vol. 7(6), pages 1141-1149, December.

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