Enantioselective hydrogenation of dimethyl itaconate with immobilised rhodium-duphos complex in a recirculating fixed-bed reactor

被引:6
|
作者
Al Herz, M. A. [1 ]
Tsoligkas, A. N. [1 ]
Simmons, M. J. H. [1 ]
Wood, J. [1 ]
机构
[1] Univ Birmingham, Sch Chem Engn, Birmingham B15 2TT, W Midlands, England
关键词
Anchored homogeneous catalyst; Rh; ((R; R)-Me-DuPhos)(COD)]BF(4); Dimethyl itaconate hydrogenation; Shake-flask reactor; Trickle bed reactor; ASYMMETRIC CATALYTIC-HYDROGENATION; ENANTIO-SELECTIVE HYDROGENATION; ANCHORED HOMOGENEOUS CATALYSTS; INDUCED PULSING FLOW; MASS-TRANSFER; 1-PHENYL-1,2-PROPANEDIONE; DERIVATIVES; PROGRESS; GLUCOSE;
D O I
10.1016/j.apcata.2011.02.009
中图分类号
O64 [物理化学(理论化学)、化学物理学];
学科分类号
070304 ; 081704 ;
摘要
The catalytic hydrogenation of dimethyl itaconate was studied in lab-scale shake flask and transferred to continuous flow with recirculation in a trickle bed reactor. All experiments were performed under ambient conditions (20 degrees C and atmospheric pressure). The catalyst complex [Rh((R,R)-Me-DuPhos)(COD)]BF(4) was anchored to powder and trilobe alumina supports using phosphotungstic acid (PTA) as an anchoring agent. For the powder alumina, tests were conducted in the shake flask to ensure that the reaction was not influenced by mass transfer limitations by varying the stirrer speed and catalyst mass, thus ensuring the reported data are in the kinetic regime. In the shake-flask [substrate to catalyst molar ratio of 60, atmospheric pressure (101,317 Pa), room temperature (293.15K), H(2) flow rate of 100 ml min(-1) (1.7 x 10(-6) m(3) s(-1)) and agitation speed of 200 rpm], a turnover frequency (TOF) of 50 h(-1) (1.4 x 10(-2) s(-1)) was achieved with powder alumina support in comparison to a TOF of 20h(-1) (5.6 x 10(-3) s(-1)) obtained with the trilobes. Under these conditions, the enantioselectivities obtained from immobilising the catalyst complex onto the powder and trilobe supports were 96% and 97%, respectively. Fitting Osborn-Wilkinson kinetics to the concentration profiles indicated that complexation with the olefin before reaction with hydrogen was the preferred path. The trickle bed reactor (TBR) was operated in the trickle flow regime using the trilobe support. Optimal gas and liquid flow rates were selected which were found to have a noticeable effect on initial reaction rate and enantioselectivity. Under optimized conditions in the TBR [substrate to catalyst molar ratio of 223, atmospheric pressure (101,317 Pa), room temperature (293.15 K), gas flow rate of 100 ml min-1 (1.7 x 10(-6) m(3) s(-1)) and liquid flow rate of 20 ml min(-1) (3.3 x 10(-7) m(3) s(-1))], 99% conversion and enantioselectivity of up to 99.9% were achieved. (C) 2011 Elsevier B.V. All rights reserved.
引用
收藏
页码:148 / 158
页数:11
相关论文
共 50 条
  • [1] Continuous enantioselective hydrogenation in fixed-bed reactor:: towards process intensification
    Künzle, N
    Solèr, JW
    Baiker, A
    [J]. CATALYSIS TODAY, 2003, 79 (1-4) : 503 - 509
  • [2] Enantioselective hydrogenation on palladium -: Limitations of continuous fixed-bed reactor operation
    Künzle, N
    Solèr, JW
    Mallat, T
    Baiker, A
    [J]. JOURNAL OF CATALYSIS, 2002, 210 (02) : 466 - 470
  • [3] Novel contributions to the mechanism of the enantioselective hydrogenation of dimethyl itaconate with rhodium complexes
    Schmidt, Thomas
    Dai, Zhenya
    Drexler, Hans-Joachim
    Baumann, WoRfgang
    Jaeger, Christian
    Pfeifer, Dietmar
    Heller, Detlef
    [J]. CHEMISTRY-A EUROPEAN JOURNAL, 2008, 14 (15) : 4469 - 4471
  • [4] Hydrogenation of diethyl adipate in a catalytic fixed-bed reactor
    Jaganathan, R
    Chaudhari, ST
    Rode, CV
    Chaudhari, RV
    Mills, PL
    [J]. INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1998, 37 (06) : 2099 - 2106
  • [5] Reversal of the ee in enantioselective hydrogenation of activated ketones in continuous-flow fixed-bed reactor system
    Cserenyi, Szabolcs
    Szollosi, Gyoergy
    Szori, Kornel
    Fueloep, Ferenc
    Bartok, Mihaly
    [J]. CATALYSIS COMMUNICATIONS, 2010, 12 (01) : 14 - 19
  • [6] THE SELECTIVE HYDROGENATION OF SOYBEAN OIL IN A CONTINUOUS FIXED-BED REACTOR
    QUALETTI, GM
    [J]. JOURNAL OF THE AMERICAN OIL CHEMISTS SOCIETY, 1986, 63 (04) : 450 - 450
  • [7] Enantio selective hydrogenation of α, β-unsaturated carboxylic acids in fixed-bed reactor
    Herman, Beata
    Szollosi, Gyorgy
    Fulop, Ferenc
    Bartok, Mihaly
    [J]. APPLIED CATALYSIS A-GENERAL, 2007, 331 : 39 - 43
  • [8] Development of a Robust Fixed-Bed Reactor Model for Supercritical Citral Hydrogenation
    Haering, Hans
    Wilhelm, Steffen
    Horn, Daniel
    Haase, Stefan
    [J]. CHEMICAL ENGINEERING & TECHNOLOGY, 2017, 40 (11) : 2075 - 2083
  • [9] Simulation of an industrial fixed-bed reactor with cocurrent downflow for hydrogenation of PYGAS
    Rojas, Mixef
    Zeppieri, Susana
    [J]. CATALYSIS TODAY, 2014, 220 : 237 - 247
  • [10] Modeling, Simulation and Control of a Tubular Fixed-bed Dimethyl Ether Reactor
    Yasari, E.
    Shahrokhi, M.
    Abedini, H.
    [J]. CHEMICAL AND BIOCHEMICAL ENGINEERING QUARTERLY, 2010, 24 (04) : 415 - 423