CAJ | 학술논문

应用CO_2-MDEA气液吸收体系,对旋转填充床中伴有可逆反应的气液传质过程进行了定量的模型研究.在所有反应都可逆的情况下,根据Higbie渗透理论建立了旋转床中CO_2-MDEA体系的扩散-反应传质模型.通过模型对传质过程的定量描述以及实验结果对模型的验证,超重力旋转床的强化作用可进一步被揭示为:由于不断更新的液膜使得可溶性气体在液膜内形成较大的浓度梯度,从而极大地增大了传质系数,强化了传质;旋转床的强化作用是在动态的传质过程中完成的,液膜的寿命越短则传质系数越大.在不同转速、温度、MDEA浓度和气液流量条件下进行了实验,本文模型的模拟值和实验结果吻合较好.
응용CO_2-MDEA기액흡수체계,대선전전충상중반유가역반응적기액전질과정진행료정량적모형연구.재소유반응도가역적정황하,근거Higbie삼투이론건립료선전상중CO_2-MDEA체계적확산-반응전질모형.통과모형대전질과정적정량묘술이급실험결과대모형적험증,초중력선전상적강화작용가진일보피게시위:유우불단경신적액막사득가용성기체재액막내형성교대적농도제도,종이겁대지증대료전질계수,강화료전질;선전상적강화작용시재동태적전질과정중완성적,액막적수명월단칙전질계수월대.재불동전속、온도、MDEA농도화기액류량조건하진행료실험,본문모형적모의치화실험결과문합교호.
A quantitative study on the absorption of CO_2 by aqueous solutions of N-methyldiethanolamine(MDEA)in a rotating packed bed(RPB)was presented in this paper.The diffusion-reaction process for CO_2-MDEA mass transfer in the RPB is modeled according to Higbie's penetration theory with the assumption that all reactions are reversible.The results from both experiment and model show that the intensification within the RPB is mainly achieved by the larger concentration gradient of the dissolvable gas in the liquid film.The frequent renewal of the film results in short lifetime of liquid film on packing surfaces and increases the mass transfer coefficient significantly.The mass transfer within the RPB is a dynamic process. The shorter the lifetime of liquid film,the larger the mass transfer coefficient.Experiments are carried out at various rotating speeds,MDEA concentrations,temperatures and gas/liquid flow rates.The validity of this model is demonstrated by the fact that the simulated values agree well with the experimental data.