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在用于合成气发酵的搅拌釜式反应器中测量一氧化碳气液传质

Measuring carbon monoxide gas-liquid mass transfer in a stirred tank reactor for syngas fermentation.

作者信息

Riggs Seth S, Heindel Theodore J

机构信息

Department of Mechanical Engineering, 2025 Black Engineering Building, Iowa State University, Ames, Iowa 50011-2161, USA.

出版信息

Biotechnol Prog. 2006 May-Jun;22(3):903-6. doi: 10.1021/bp050352f.

Abstract

Carbon monoxide-liquid mass transfer rates in a water-filled stirred tank reactor are determined using a myoglobin protein method to measure dissolved carbon monoxide concentrations as a function of time. Data are acquired over a range of stirrer speeds (200 < or = N < or = 600 rpm) and gas flow rates (1 < or = Q < or = 6 L/min), corresponding to a gas retention time range of 1.2-7 min. Volumetric CO-water mass transfer coefficients range from 0.003 to 0.043 s(-1) and are well-correlated using the power density and the superficial gas velocity.

摘要

在充满水的搅拌釜式反应器中,采用肌红蛋白蛋白法测定溶解一氧化碳浓度随时间的变化,从而确定一氧化碳-液体传质速率。在一系列搅拌器转速(200≤N≤600转/分钟)和气体流速(1≤Q≤6升/分钟)范围内采集数据,对应的气体停留时间范围为1.2 - 7分钟。体积CO-水传质系数范围为0.003至0.043 s⁻¹,并且使用功率密度和表观气体流速具有良好的相关性。

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