.4%和95.8%。Р6.中试设备一览表Р 中试设备如表1。Р表1 设备一览表Р序号Р设备位号Р名称Р规格Р材质Р数量Р备注Р1РV101Р30% H2O2进料储罐РV=3m3Р304LР1Р2РV102Р丙酸进料储罐РV=9m3Р316L SSР1Р3РV103Р环己酮进料储罐РV=3m3РQ235Р1Р4РV104Р环己烷进料储罐РV=3m3РQ235Р1Р5РV105Р油水分离器РV=0.5m3Р316L SSР1Р6РV106Р过滤储罐РV=20m3Р316L SSР2Р7РV107Р缓冲罐РV=1m3РQ235Р1Р8РV201РE201储罐РV=2m3Р316L SSР1Р9РV202РE202储罐РV=2m3Р316L SSР1Р10РV203РE203储罐РV=2m3Р316L SSР1Р11РV204Рε-己内酯成品储罐РV=100m3Р316L SSР1Р12Р—Р丙酸原料储罐РV=200m3Р316L SSР1Р13Р—Р30% H2O2原料储罐РV=100m3Р304LР1Р14Р—Р环己烷原料储罐РV=50m3РQ235Р1Р15Р—Р环己酮原料储罐РV=50m3РQ235Р1Р16РR101Р过氧化反应釜РV=2m3;电机N=22Kw; ST型减速机;Р304LР1Р与物料接触处Р用OCr18Ni9或Р1Cr18Ni9TiР Р 续表Р序号Р设备位号Р名称Р规格Р材质Р数量Р备注Р17РR102Р合成反应釜РV=2 m3;电机N=22Kw; ST型减速机;Р304LР1Р与物料接触处Р用OCr18Ni9或Р1Cr18Ni9TiР18РF101Р过滤器Р型号GGG-20;Р过滤面积=5 m3;Р316L SSР1Р19РT201Р精馏塔ⅠР316L SSР1Р20РT202Р精馏塔ⅡР316L SSР1Р21РT203Р精馏塔ⅢР316L SSР1