Gas holdup, liquid circulating velocity and mass transfer properties in a mini-scale external loop airlift bubble column
Gas holdup, liquid circulating velocity and mass transfer properties in a mini-scale external loop airlift bubble column
复制标题
微型外循环气升泡罩塔中的含气率、液体循环速度和传质特性
DOI:
10.1016/s0009-2509(03)00207-0
复制
发表时间:
2003
影响因子:
4.7
通讯作者:
K. Nakao
中科院分区:
文献类型:
--
作者:
Shaoqing Wang;Y. Arimatsu;Kenichi Koumatsu;Keiji Furumoto;M. Yoshimoto;K. Fukunaga;K. Nakao
The external loop airlift bubble column has been regarded as a promising type of gas–liquid or gas–liquid–solid biooreactor because of the liquid circulating flow between the riser and downcomer. A mini-scale column is useful and efficient in the process research and development for highly specialized materials such as fine chemicals, advanced bioproducts and biocatalysts utilized in two or three phase system. In this work, a mini-scale glass column of 20 ml in volume was designed and characterized. The gas holdup εGin the riser was obtained by measuring the volume expansion through photographs taken with a digital camera. The liquid circulating velocity ULwas measured by observing the time required for a tracer particle to travel a fixed distance (3.5 cm ) in the downcomer through analysis of the images taken by a video camera. The gas–liquid volumetric oxygen transfer coefficient kLa and liquid–solid oxygen transfer coefficient kSwere determined by our previous method in which the air oxidation of glucose was catalysed by the immobilized glucose oxidase gel beads suspended in the column to obtain a pseudo steady state concentration of the dissolved oxygen and the corresponding constant rate of glucose consumption. It was shown that even such a mini-scale external loop bubble column could be characterized in terms of gas holdup, liquid circulating velocity and mass transfer properties according to our previous correlations proposed for the bench to pilot scale column.