2004
DOI: 10.1016/j.ces.2004.09.011
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Analysis of the performance of single capillary and multiple capillary (monolith) reactors for the multiphase Pd-catalyzed hydrogenation of 2-Butyne-1,4-Diol

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Cited by 28 publications
(19 citation statements)
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References 15 publications
(16 reference statements)
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“…First, the support is deposited on the monolith by washcoating using a slurry of the support material with or without a binder. In the second step, the active metal is impregnated on the washcoated support (Kreutzer et al, 2001;Boger et al, 2004;Naitividad et al, 2004;Zhao et al, 2008). In multiphase reactions, the reactor performance is a combined effect of both internal and external mass transfer resistances.…”
Section: Introductionmentioning
confidence: 99%
“…First, the support is deposited on the monolith by washcoating using a slurry of the support material with or without a binder. In the second step, the active metal is impregnated on the washcoated support (Kreutzer et al, 2001;Boger et al, 2004;Naitividad et al, 2004;Zhao et al, 2008). In multiphase reactions, the reactor performance is a combined effect of both internal and external mass transfer resistances.…”
Section: Introductionmentioning
confidence: 99%
“…Scheme 1: 2-Butyne-1,4-diol hydrogenation scheme [29]. low cost and environmentally friendly since the support is a waste material, the solvent is water, and the calcination step is eliminated.…”
Section: Discussionmentioning
confidence: 99%
“…The withdrawn liquid samples were analyzed by gas chromatography with a flame ionization detector using a VARIAN CP3800 GC (DB-WAX 52 column, length 32 m, inner diameter = 0.3 mm) and helium (30 ml/min) as carrier gas, according to previous reported analysis methods [29,31,32]. Reaction samples were injected into the GC and analyzed under the following conditions: temperature detector was set at 518 K, injector temperature was set at 513 K, initial oven temperature was 353 K, and this was raised up to 493 K at a rate 10 (K/min).…”
Section: Hydrogenation Of 2-butyne-14-diolmentioning
confidence: 99%
“…7 They considered that, compared with other flow patterns, Taylor flow was the optimum with the reaction rate dependent on the liquid slug length. 7 Natividad et al 18 and Tsoligkas et al 19 studied the hydrogenation of 2-butyne-1,4-diol on Pd catalyst under Taylor flow in monolith and capillary reactors. Their experiments showed that the operating condition of Taylor flow influenced remarkably the initial reaction rate.…”
mentioning
confidence: 99%
“…Their experiments showed that the operating condition of Taylor flow influenced remarkably the initial reaction rate. 18,19 It was well known that, compared with circular channels, square channel monolith reactors were more widely used in practice. The flow states of reactants in square channels were remarkably different from that in circular channels.…”
mentioning
confidence: 99%