欢迎来到天天文库
浏览记录
ID：32632184
大小：235.98 KB
页数：12页
时间：2019-02-13
《三甘醇灵敏度分析》由会员上传分享，免费在线阅读，更多相关内容在工程资料-天天文库。
1、萃取塔总塔板数与产品纯度关系萃取塔原料进料位置与产品纯度关系—异丙醇质量含量4681012141618202224262830323436原料进料板位置9卜609260萃取塔原料进料位置对热负荷的影响—O—condenser—O^—reboiler98901匚9989.09896工Hn2、汽萃収剂进料位置对热负荷的影响9寸V9卜寸・T工Hn3、boiler20002500300035004000萃取剂循环量kg/h45005000萃取塔的质量回流比与产品纯度关系工Hn4、^o-Go,crHn5、3（水）温度/°c热负荷/(GJ/hr)塔顶0.998277574.89E-060.0017175481.9044828-4.9076324塔釜0.015457430.918658220.06588434140.6741253.83474042回收塔塔板数原料进料板质量回流比1070.9测位0)(IPA)3（二甘醇）（0（水）温度/°c热负荷/(GJ/hr)塔顶0.163640960.138866510.6974925387.1010598-1.3326074塔釜1.54E-070.999999661.86、6E-07299.5709552.82275767
2、汽萃収剂进料位置对热负荷的影响9寸V9卜寸・T工Hn3、boiler20002500300035004000萃取剂循环量kg/h45005000萃取塔的质量回流比与产品纯度关系工Hn4、^o-Go,crHn5、3（水）温度/°c热负荷/(GJ/hr)塔顶0.998277574.89E-060.0017175481.9044828-4.9076324塔釜0.015457430.918658220.06588434140.6741253.83474042回收塔塔板数原料进料板质量回流比1070.9测位0)(IPA)3（二甘醇）（0（水）温度/°c热负荷/(GJ/hr)塔顶0.163640960.138866510.6974925387.1010598-1.3326074塔釜1.54E-070.999999661.86、6E-07299.5709552.82275767
3、boiler20002500300035004000萃取剂循环量kg/h45005000萃取塔的质量回流比与产品纯度关系工Hn4、^o-Go,crHn5、3（水）温度/°c热负荷/(GJ/hr)塔顶0.998277574.89E-060.0017175481.9044828-4.9076324塔釜0.015457430.918658220.06588434140.6741253.83474042回收塔塔板数原料进料板质量回流比1070.9测位0)(IPA)3（二甘醇）（0（水）温度/°c热负荷/(GJ/hr)塔顶0.163640960.138866510.6974925387.1010598-1.3326074塔釜1.54E-070.999999661.86、6E-07299.5709552.82275767
4、^o-Go,crHn5、3（水）温度/°c热负荷/(GJ/hr)塔顶0.998277574.89E-060.0017175481.9044828-4.9076324塔釜0.015457430.918658220.06588434140.6741253.83474042回收塔塔板数原料进料板质量回流比1070.9测位0)(IPA)3（二甘醇）（0（水）温度/°c热负荷/(GJ/hr)塔顶0.163640960.138866510.6974925387.1010598-1.3326074塔釜1.54E-070.999999661.86、6E-07299.5709552.82275767
5、3（水）温度/°c热负荷/(GJ/hr)塔顶0.998277574.89E-060.0017175481.9044828-4.9076324塔釜0.015457430.918658220.06588434140.6741253.83474042回收塔塔板数原料进料板质量回流比1070.9测位0)(IPA)3（二甘醇）（0（水）温度/°c热负荷/(GJ/hr)塔顶0.163640960.138866510.6974925387.1010598-1.3326074塔釜1.54E-070.999999661.8
6、6E-07299.5709552.82275767
此文档下载收益归作者所有
