(674b) Continuous Homogeneous Hydroformylation of 1-Octene with in Situ Membrane Filtration for Separation of Soluble Polymer Bound Rhodium Complexes | AIChE

(674b) Continuous Homogeneous Hydroformylation of 1-Octene with in Situ Membrane Filtration for Separation of Soluble Polymer Bound Rhodium Complexes

Authors 

Fang, J. - Presenter, Univ. Kansas
Jana, R. - Presenter, University of Kansas
Snavely, K. - Presenter, University of Kansas
Subramaniam, B. - Presenter, Center for Environmentally Beneficial Catalysis, University of Kansas
Tunge, J. - Presenter, Univ. Kansas

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).