The Impact of Side Reactions in Sulfur Recovery Unit Design

황 회수 공정 설계에서 부 반응의 영향

  • Kim, Sung Ho (Plant Basic Engineering Team, Global Engineering Division, GS Engineering & Construction) ;
  • Jung, Won Seok (Plant Basic Engineering Team, Global Engineering Division, GS Engineering & Construction) ;
  • Lee, Hee Mun (Plant Basic Engineering Team, Global Engineering Division, GS Engineering & Construction) ;
  • Chang, Geun Soo (Plant Basic Engineering Team, Global Engineering Division, GS Engineering & Construction)
  • 김성호 ((주)GS건설, 글로벌 엔지니어링 본부, 플랜트 기본설계팀) ;
  • 정원석 ((주)GS건설, 글로벌 엔지니어링 본부, 플랜트 기본설계팀) ;
  • 이희문 ((주)GS건설, 글로벌 엔지니어링 본부, 플랜트 기본설계팀) ;
  • 장근수 ((주)GS건설, 글로벌 엔지니어링 본부, 플랜트 기본설계팀)
  • Received : 2017.06.09
  • Published : 2017.09.30

Abstract

In the reaction furnace of modified Claus process, chemical equilibrium reactions and kinetic reactions occur simultaneously. The main kinetic components are hydrogen ($H_2$), carbon monoxide (CO), carbonyl sulphide (COS) and carbon disulphide ($CS_2$). The equilibrium calculations, empirical correlations and sulfur recovery technology providers' (licensors) data for kinetic components (COS and $CS_2$) in the reaction furnace were analyzed to evaluate the amount of kinetic components by applying them to five different projects in which GS Engineering & Construction participated. Kinetic components ($H_2$ and CO) are also calculated and the results are analyzed to evaluate the impact of temperature in the reaction furnace and the waste heat boiler. Total required $O_2$ deviations for combustion in the reaction furnace are additionally shown, with and without side reactions. A full understanding of side reactions in the modified Claus process can help to improve sulfur recovery efficiency and optimize equipment design.

황회수 공정의 연소반응기 안에서는 평형반응 및 kinetic 반응이 동시에 일어난다. 주요 kinetic 반응에 참여하는 성분들은 수소($H_2$), 일산화탄소(CO), 카보닐황화물(COS) 그리고 이황화탄소($CS_2$) 이다. 본 연구에서는 평형반응, 상관관계식(empirical correlations) 그리고 황 회수 공정의 라이센서 자료의 비교를 통해 반응기에서 kinetic components (COS와 $CS_2$)의 생성 양을 분석한다. 또한 kinetic components ($H_2$ 와 CO)의 생성 양의 분석을 통해 반응기에서의 생성 양과 온도와의 상관관계를 분석한다. 부 반응이 전체 연소에 필요로 하는 산소의 양에 어떤 영향을 미치는지도 같이 분석을 한다. 황회수 공정의 반응기내의 부 반응에 대한 충분한 이해는 전체 황회수 공정 설계를 할 때 최적의 장치 설계를 가능하게 하고 나아가 황회수 효율을 극대화 하는데 도움이 된다.

Keywords

References

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