沈阳化工大学学报
瀋暘化工大學學報
침양화공대학학보
Journal of Shenyang Institute of Chemical Technology
2015年
3期
211-215
,共5页
黄动昊%张志刚%郑立娇%吕明%贾鹏%李文秀
黃動昊%張誌剛%鄭立嬌%呂明%賈鵬%李文秀
황동호%장지강%정립교%려명%가붕%리문수
模拟%AspenPlus%四氢呋喃-水%萃取精馏%灵敏度分析
模擬%AspenPlus%四氫呋喃-水%萃取精餾%靈敏度分析
모의%AspenPlus%사경부남-수%췌취정류%령민도분석
simulation%Aspen Plus%tetrahydrofuran-water%extractive distillation%sensitivity analysis
以从制药废液中回收四氢呋喃为例,详细研究萃取精馏过程的Aspen Plus模拟和优化.通过实验与热力学模型预测的对比确定NRTL方程能更准确地描述THF-水-DMSO三元混合物系气液相平衡;分析THF-水-DMSO三元混合物系剩余曲线说明DMSO是萃取精馏分离该共沸物系的可行萃取剂;设计萃取精馏分离工艺流程并以萃取精馏塔为例,运用灵敏度分析对过程进行优化,结果表明:200 kmol/h进料量的常压萃取精馏,塔板数22,萃取剂和原料液分别在第4和第18块板进料,回流比 1. 0,溶剂比 0. 45 的条件下可得到纯度高于 99. 85 %的 THF,回收率高于99. 5 %.
以從製藥廢液中迴收四氫呋喃為例,詳細研究萃取精餾過程的Aspen Plus模擬和優化.通過實驗與熱力學模型預測的對比確定NRTL方程能更準確地描述THF-水-DMSO三元混閤物繫氣液相平衡;分析THF-水-DMSO三元混閤物繫剩餘麯線說明DMSO是萃取精餾分離該共沸物繫的可行萃取劑;設計萃取精餾分離工藝流程併以萃取精餾塔為例,運用靈敏度分析對過程進行優化,結果錶明:200 kmol/h進料量的常壓萃取精餾,塔闆數22,萃取劑和原料液分彆在第4和第18塊闆進料,迴流比 1. 0,溶劑比 0. 45 的條件下可得到純度高于 99. 85 %的 THF,迴收率高于99. 5 %.
이종제약폐액중회수사경부남위례,상세연구췌취정류과정적Aspen Plus모의화우화.통과실험여열역학모형예측적대비학정NRTL방정능경준학지묘술THF-수-DMSO삼원혼합물계기액상평형;분석THF-수-DMSO삼원혼합물계잉여곡선설명DMSO시췌취정류분리해공비물계적가행췌취제;설계췌취정류분리공예류정병이췌취정류탑위례,운용령민도분석대과정진행우화,결과표명:200 kmol/h진료량적상압췌취정류,탑판수22,췌취제화원료액분별재제4화제18괴판진료,회류비 1. 0,용제비 0. 45 적조건하가득도순도고우 99. 85 %적 THF,회수솔고우99. 5 %.
In this paper,we take the instance of recovering THF from pharmaceutical wastes to investi-gate the simulation and optimization of extractive distillation process using Aspen Plus. Firstly,the contrast of experimental data with thermodynamic model prediction indicates that NRTL model describes the VLE behavior of THF-water-DMSO system more accurately. Analyzing the residue curve map of THF-water-DMSO system shows that DMSO is a feasible entrainer. The extractive distillation process is established and optimized taking extraction distillation column as an instance through sensitivity analysis. The influ-ences of process parameters are explored. The results show that while the feed rate is set as 200 kmol/h under atmospheric pressure,stage number 22,entrainer and the binary mixture fed on 4th and 18th stage respectively, reflux ratio 1. 0,solvent ratio 0. 45 is optimized condition under which we can obtain THF purer than 99. 85 %,and the recovery of THF can be higher than 99. 5 % meeting the requirements of industrial design.