塔201进口条件入入口条件H,KJ/KgH,MJ/h温度,℃200压力,Mpa4.8原料,t/h133975167溶剂,t/h5.69205155合计10322出口温度,℃190压力,Mpa0.7原料,t/h133875031溶剂,t/h5.695%96751425%615172合计10345平衡014汽提塔202闪蒸前条件H,KJ/KgH,MJ/h温度,℃230压力,Mpa4.7原料,t/h5.625460.242589溶剂,t/h3.8其中溶剂分相90%1108.763792溶液中10%933.032355合计6735闪闪蒸后温度,℃223压力,Mpa0.7原料,t/h5.625447.72518.2溶剂,t/h3.8其中溶剂分相(气体)97%1112.94102.3溶液中3%937.2106.86727.4平衡015.高压空冷量空冷入口焓值,KJ/Kg总焓,MJ/h高温溶剂温度,℃120.0压力,Mpa4.6原料,t/h0.2溶剂,t/h65.7585.7638484.43低温溶剂温度,℃300压力,Mpa0.70溶剂,t/h9.3343.0883190.718混合溶剂,t/h75.0混合温度,℃108.0555.668741675.15压力,Mpa4.6合计41675.15空冷出口温度,℃90压力,Mpa4.6溶剂,t/h75.0472.79235459.4ΔH,MJ/h-6215.7516.低压空冷量热流入口温度,℃210 压力,Mpa0.7 气体溶剂,t/h9.3238.439 9989277.94出口温度,℃30 压力,Mpa0.7 液体溶剂,t/h9.382 3433190.718放热量,MJ/h -6087.22四、产物收率性质1.萃取分离条件及产物性质组成萃取分离操作条件与收率塔101温度,℃90塔102温度,℃200压力,MPa4.8压力,MPa4.7
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