4楼的朋友，aspen中怎么调节平衡温距？ 平衡温距 在 gibbs反应器的 反应 选项里面选择，你自己看看吧，既可以限定所有的反应的平衡温距，也可以设定 特定 反应的 平衡温距。

问题已经解决，谢谢多位马友的关注！ 我也在做相同的模拟，你能共享一下嘛？你的问题是怎么解决的？

显示的错误如下。（组分都是输好的） ! calculations stopped because of missing property parameters

就是你的速率方程中浓度的指数项 太感谢了！

看错误提示，貌似是温度出了问题，好好检查看看，反应热是不是不对

学习学习学习学习

可能是因为你那个输入组分后没有被识别出来的原因。 要在components-->specifications里全部有显示

可用于模拟吸收的反应器是批反应器加蒸馏塔，模拟水被高温烟气蒸干是换热器……。

就是盐酸和氧化铝、氧化铁反应。 ->processing input specifications ... information pure component parameters for some components are retrieved from sdf table. these parameters are used with the elecnrtl option set unless you enter your own parameters in prop-data paragraphs parameters retrieved for component hcl are: cpdiec plxant parameters retrieved for component h2o are: vlbroc plxant ** error hypothetical liquid component hcl cannot be processed because there are no solid data--cpsxp1 is missing mw available for component tio2 is different from mw calculated from formula (atomno/noatom). calculated value is used. available mw = 79.86580 calculated mw = 79.87880 * warning in physical property system parameter dhform/element 1 (data set 1) upper bound violated for component fe+3 value = 0.57128e+10, upper bound = 0.50000e+10 * warning in physical property system parameter dhform/element 1 (data set 1) upper bound violated for component al+3 value = 0.54832e+10, upper bound = 0.50000e+10 * warning in the "stream" paragraph which begins on line 125 stream name: 1 component mass fractions are normalized to unity. * warning in the "stream" paragraph which begins on line 129 stream name: 2 component mass fractions are normalized to unity. * warning while checking input specifications block name: b5 model name: rstoic no combustion reactions are possible - oxygen (o2) has not been defined as a component. ! errors while processing input specifications

求大神们指教啊！！！