Continuous Homogeneous Hydroformylation of 1-Octene with in Situ Membrane Filtration for Separation of Soluble Polymer Bound Rhodium Complexes

Friday, November 13, 2009: 8:55 AM
Governor's Chamber C (Gaylord Opryland Hotel)

Jing Fang, Chemical Engineering, Univ. Kansas, Lawrence, KS
Ranjan Jana, Department of Chemistry, University of Kansas, Lawrence, KS
Kirk Snavely, Cebc, University of Kansas, Lawrence, KS
Jon Tunge, Chemistry, Univ. Kansas, Lawrence, KS
Bala Subramaniam, Chemical & Petroleum Engineering, University of Kansas, Lawrence, KS

In previous work, it as shown that rhodium catalyzed hydroformylation of higher olefin (1-octene as model substrate) was enhanced by CO2 addition, giving reasonable turnover frequency (~300 h-1) and higher selectivity towards the linear aldehyde (~90%) at mild pressures (~40 bar) and temperatures (60 °C).[1] Preliminary economical analysis indicates that greater than 99.8% of Rh-based catalyst has to be recovered for economic viability.[2] To achieve the targeted Rh recovery rate, CEBC researchers synthesized a series of bulky, soluble and recyclable polymer bound phosphorus ligands to facilitate quantitative Rh retention in homogeneous hydroformylation reaction mixtures using nano/ultra-filtration membrane techniques.  Both batch and continuous filtrations were conducted in a commercially available high-pressure MET cell under air-free operation equipped with a solvent-resistant, polyimide STARMEM® membrane.  The retention of the catalyst precursor Rh(acac)(CO)2 bound to various ligands, including TPPine, bidentate ligands and polymer bound ligands, were investigated.  As expected, the size of the ligands significantly affects the Rh retention. During continuous filtration of a toluene-based solution containing bidentate polymer bound Rh complexes, the Rh and P concentrations in the permeate, quantified using ICP analysis, were on the order of a few tens of ppb. The catalyst activity, regioselectivity and Rh retention for continuous homogeneous hydroformylation of 1-olefin in stirred reactors with in situ membrane filtration of such catalyst complexes will be presented.

 


[1].      H. Jin, A. Ghosh, J. A. Tunge and B. Subramaniam, "Intensification of Catalytic Olefin Hydroformylation in CO2-expanded Media", AIChE Journal,  52(7), 2575-2591 (2006).

           

[2].      J. Fang, H. Jin, T. Ruddy, K. Pennybaker, D. Fahey and B. Subramaniam, “Economic and Environmental Impact Analyses of Catalytic Olefin Hydroformylation in CO2-Expanded Liquid (CXL) Media,” Industrial and Engineering Chemistry Research, 46, 8687-8692 (2007).

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