化工进展
化工進展
화공진전
CHEMICAL INDUSTRY AND ENGINEERING PROGRESS
2015年
2期
571-575
,共5页
吕太%刘力萌%郭东方%牛红伟%尚航
呂太%劉力萌%郭東方%牛紅偉%尚航
려태%류력맹%곽동방%우홍위%상항
烟气预处理%模拟%优化%SO2脱除%烟气降温
煙氣預處理%模擬%優化%SO2脫除%煙氣降溫
연기예처리%모의%우화%SO2탈제%연기강온
flue gas pretreatment%simulation%optimization%SO2 removal%flue gas cooling
在燃煤电厂 CO2捕集中,为了提高其捕集效率,需对进入系统的烟气进行预处理。为进一步提高进入系统烟气的质量,本文用Aspen Plus模拟优化烟气预处理系统,通过研究在预洗塔中组合填料、填料层高度、吸收剂进量和分层进吸收剂对出口烟气中SO2的含量、脱硫效率以及出口烟气温度的影响,得出最佳的工艺条件。模拟结果表明,加入不同种类组合填料,同种类不同型号组合填料和分层进吸收剂都使烟气脱硫效率增加,出口烟气温度降低;随着填料层高度和吸收剂进量的增加,出口烟气中 SO2的含量和出口烟气温度降低,其中最佳的高度为2~4m,最佳的吸收剂进量为(250~350)×103kg/h。
在燃煤電廠 CO2捕集中,為瞭提高其捕集效率,需對進入繫統的煙氣進行預處理。為進一步提高進入繫統煙氣的質量,本文用Aspen Plus模擬優化煙氣預處理繫統,通過研究在預洗塔中組閤填料、填料層高度、吸收劑進量和分層進吸收劑對齣口煙氣中SO2的含量、脫硫效率以及齣口煙氣溫度的影響,得齣最佳的工藝條件。模擬結果錶明,加入不同種類組閤填料,同種類不同型號組閤填料和分層進吸收劑都使煙氣脫硫效率增加,齣口煙氣溫度降低;隨著填料層高度和吸收劑進量的增加,齣口煙氣中 SO2的含量和齣口煙氣溫度降低,其中最佳的高度為2~4m,最佳的吸收劑進量為(250~350)×103kg/h。
재연매전엄 CO2포집중,위료제고기포집효솔,수대진입계통적연기진행예처리。위진일보제고진입계통연기적질량,본문용Aspen Plus모의우화연기예처리계통,통과연구재예세탑중조합전료、전료층고도、흡수제진량화분층진흡수제대출구연기중SO2적함량、탈류효솔이급출구연기온도적영향,득출최가적공예조건。모의결과표명,가입불동충류조합전료,동충류불동형호조합전료화분층진흡수제도사연기탈류효솔증가,출구연기온도강저;수착전료층고도화흡수제진량적증가,출구연기중 SO2적함량화출구연기온도강저,기중최가적고도위2~4m,최가적흡수제진량위(250~350)×103kg/h。
In coal-fired power plant CO2capture, in order to improve capture efficiency, flue gas pretreatment is required. In order to further improve flue gas quality at pretreatment outlet, Aspen Plus simulation was used to optimize flue gas pretreatment to study combination packing, packing layer height, absorbent quantity, and absorbent placed in separated layers,and investigate their influence on content of SO2at outlet, desulfurization efficiency and flue gas outlet temperature to determine the optimal process conditions. Adding different kinds of combination packing, different models of combination packing and absorbent placed in separated layers increased desulfurization efficiency and reduced flue gas pretreatment ioutlet temperature. With the increase of packing layer height and quantity of absorbent, flue gas temperature and content of SO2at flue gas pretreatment outlet decreased. Optimal packing layer height was 2—4m,and optimal absorbent quantity was (250—350)×103kg/h.