Partial Hydrogenation of Soybean Oil in a Piston Oscillating Monolith Reactor

被引:7
|
作者
Waghmare, Yogesh G. [1 ]
Bussard, Alan G. [1 ]
Forest, Robert V. [1 ]
Knopf, F. Carl [1 ]
Dooley, Kerry M. [1 ]
机构
[1] Louisiana State Univ, Dept Chem Engn, Baton Rouge, LA 70803 USA
基金
美国国家科学基金会;
关键词
TRICKLE-BED REACTORS; MASS-TRANSFER; PULSING FLOW; FIXED-BED; COMMERCIAL CATALYSTS; PERIODIC OPERATION; NICKEL CATALYSTS; LIQUID MEMBRANES; COTTONSEED OIL; VEGETABLE-OILS;
D O I
10.1021/ie902000e
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The partial hydrogenation of soybean oil was carried out in a novel piston oscillating monolith reactor (POMR). POMR performance was studied under the application of low frequency (0-17.5 Hz) and amplitude (2.5 mm) vibrations at 110 degrees C and 0.41 MPa H-2 using a Pd/Al2O3 monolith catalyst. Results show observed rate improvements of up to 220% for 17.5 Hz, 2.5 mm piston oscillations over low frequency pulsing conditions. For comparison purposes, the reaction was also carried out in a stirred tank reactor using the monolith catalyst. The POMR showed better activity at an equivalent power per unit volume when compared to a stirred tank. With the monolith catalyst, both external and internal mass transfer limitations exist. Using standard diffusion-reaction calculations and measurements over a range of particle sizes it was shown that the vibrations improve external mass transfer rates as well as internal transport within the washcoat. The POMR showed equal or better serial pathway selectivity than a stirred tank, except at the highest frequency, but gave higher trans fatty acid formation.
引用
收藏
页码:6323 / 6331
页数:9
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