• 作者： Chen, Hsi-Jen; Tsai, Shout-Yong
• 中文摘要： 本文以事故動態模擬之安全分析法探討有潛在危險之苯氯化反應器; 傳統的事故樹分析用來決定何種元件失效會造成反應器之特定擾動狀態,其次藉動態模擬預估製程擾動時將有多少時間可採取校正動作,結果顯示「反應器溫度失控」(溫度超出500K)約需1.9小時。
• 英文摘要： Fault-dynamic modeling has been applied for analysis of a potentially hazardous situation in a benzene chlorinator. Traditional fault-tree analysis is used to determine the combinations of component failures that can lead to a particular process upset condition. Realistic dynamic-modeling is then used to calculate the time available for corrective action once the upset has started. The result of the analysis shows the time required for reaction runaway (temperature excursion toward 500 K) is about 1.9 hours.
• 中文關鍵字： 苯; 氯化; 事故動態; 模擬; 安全分析
• 英文關鍵字： Benzene; Chlorination; Fault Dynamic; Model; Safety Analysis