摘要
针对天然气吸附储存罐,建立了快速绝热充气过程的二维传热传质模型,并进行了数值模拟计算。给出了充气过程中储罐内吸附床层的温度和吸附量的分布特征:随着吸附进行,储罐沿轴向从入口温度逐渐升高,储罐后部温度升幅最大,导致吸附床层后部的吸附量较低;与等温吸附相比,快速绝热充气的吸附效率只有65%。因此,要提高吸附量,就必须强化储罐内部吸附床层的热量传递过程,如加入热交换管、导热肋片等,以降低储罐吸附床层的温度。
Based on the quick charge process of the adsorbed natural gas storage system, a two-dimensional, adiabatic model was established and thereafter numerical solved. The characteristics of the temperature and the mass adsorption distribution were obtained. As the charging process proceeds, the temperature increases from the inlet, and the largest temperature increase appears at the end section and this large temperature increase results in lower mass adsorption. The average adsorption ratio is only 0.65 compared with that of a constant-adsorption process. Therefore, it is very important to enhance the heat transfer between the system and the environment and thus reduce the temperature increase for improving the adsorption efficiency.
出处
《热科学与技术》
CAS
CSCD
2009年第3期231-235,共5页
Journal of Thermal Science and Technology
基金
国家自然科学基金资助项目(50676002)
教育部高等学校博士学科点专项科研基金资助项目(20040005008)
关键词
天然气
吸附储存
传热传质
数值模拟
natural gas
adsorption storage
numerical simulation
strengthen heat transfer