Abstract:-A bench-scale, continuous vortex flow reactor (VFR), with a radius ratio, , equal to 0.48 and an aspect ratio, , equal to 11.19 was studied. This reactor may be used in the enzymatic hydrolysis of polypeptides obtained from sweet cheese whey with enzymes immobilized on agarose gel. Operational conditions were 2410 < Re < 11793 and 30-min residence time for glycerol-water, 14% w/w, 27 o C (Re ax = 1.1) and for water, 38 o C (Re ax = 1.5). Residence time distributions (RTDs) were obtained after pulse injections… Show more
“…This can be assumed equivalent to increasing the rate constant. To examine this modeling analog, we have conducted simulations of fractional conversion at different flow rates while varying the diffusion coefficient (D = 1.6 × 10 −10 m 2 /s for methylene blue [34,49]) and pseudo-first order rate constant (k = 0.2238 min −1 ), respectively (Fig. 10).…”
“…This can be assumed equivalent to increasing the rate constant. To examine this modeling analog, we have conducted simulations of fractional conversion at different flow rates while varying the diffusion coefficient (D = 1.6 × 10 −10 m 2 /s for methylene blue [34,49]) and pseudo-first order rate constant (k = 0.2238 min −1 ), respectively (Fig. 10).…”
“…The performance of the reactor was close to that of a plug flow reactor for low rotational speeds, although at higher ω the by-pass flow and the mixing between vortices decreased the performance and were worse than a stirred tank 42 . Subsequently, the authors applied immobilized enzymes in the protein cleavage of cheese whey in a continuously operated TCR to obtain a uniform molecular weight distribution without damaging the fragile catalyst beads 117 . Another example is the utilization of immobilized Penicillin G acylase is immobilized in bi-dispersed gel matrix particles for the synthesis of β-lactam antibiotics like ampicillin for which, again, the low strain on solid enzyme supports is also required.…”
Section: Applications In Enzymatic Transformations and Biotechnologymentioning
confidence: 99%
“…This is also evident in the correlations for Pe presented below. Giordano et al investigated water and water glycerol mixtures in a TCR (Λ = 0.48, Γ = 11.19) with low axial velocity Re ax = 1–1.5 for 2,410 < Ta < 11,793 76 . For this range, Pe was described by Equation ().…”
Section: Engineering Aspects and Geometric Descriptorsmentioning
The Taylor-Couette reactor (TCR) is an apparatus that capitalizes on the Taylor-Couette flow, which allows many flow regimes and conditions to perform (bio-)chemical conversions with precise control of various reactor characteristics. With the possibility to continuously perfuse the reactor with a reaction medium, the TCR becomes interesting for chemical engineering applications. In this review we introduce this reactor type and provide an overview of its history, principles of the flow regimes, and a description and design aspects of the reactors and their elements. Available information in the literature is summarized and harmonized to present available formulas and correlations in a consistent set of variables. Additionally, a wide number of applications in process technology is covered, including reactions in homogeneous, photo and enzymatic catalysis, polymer synthesis, and crystallization and aggregation-flocculation processes. Focusing on this reactor configuration, this article intends to be used as a hub for scientific groups interested in TCRs. This article has been accepted for publication and undergone full peer review but has not been through the copyediting, typesetting, pagination and proofreading process which may lead to differences between this version and the Version of Record. Please cite this article as
“…This kind of reactor is a good option when the catalysts are fragile but need to be homogenously suspended and mixed in the reaction medium, due to their gentle but efficient stirring system [53,54,55,56]. The reaction medium is confined in the gap between two concentric cylinders, the inner rotating and the outer generally stationary [54,57]. The agitation promoted by the inner cylinder is less aggressive than that one obtained with conventional stirrers [55,56].…”
Due to the heterogeneity of oils, the use of mixtures of lipases with different activity for a large number of glycerol-linked carboxylic acids that compose the substrate has been proposed as a better alternative than the use of one specific lipase preparation in the enzymatic synthesis of biodiesel. In this work, mixtures of lipases from different sources were evaluated in their soluble form in the ethanolysis of soybean oil. A mixture of lipases (50% of each lipase, in activity basis) from porcine pancreas (PPL) and Thermomyces lanuginosus lipase (TLL) gave the highest fatty acid ethyl ester (FAEE) yield (around 20 wt.%), while the individual lipases gave FAEE yields 100 and 5 times lower, respectively. These lipases were immobilized individually by the cross-linked enzyme aggregates (CLEAs) technique, yielding biocatalysts with 89 and 119% of expressed activity, respectively. A mixture of these CLEAs (also 50% of each lipase, in activity basis) gave 90.4 wt.% FAEE yield, while using separately CLEAs of PPL and TLL, the FAEE yields were 84.7 and 75.6 wt.%, respectively, under the same reaction conditions. The mixture of CLEAs could be reused (five cycles of 6 h) in the ethanolysis of soybean oil in a vortex flow-type reactor yielding an FAEE yield higher than 80% of that of the first batch.
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