研究了不同宽度的隔板式环流反应器中的气含率,循环比和体积传递系数。
The gas hold-up, circulation ratio and the volumetric transfer coefficient of liquid in reactor with a separate plate of different sizes were investigated.
结果显示在不同的循环方式中,平行流系统产生最大的热力系数而逆串联系统的最高发生温度和压力比其他系统都低。
The results show that the parallel-flow cycle yields the highest coefficient of performance among the cycles while the maximum pressure and temperature in the reverse-flow cycle are lowest.
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