Abstract:Intensification is intrinsic to better chemical and process engineering and has always been used in practice. Multiphase reactions and reactors are ubiquitous in chemical and allied industries and are of great economic and ecological importance. There is a great scope for intensifying multiphase reactions and reactors for realizing productivity enhancements, which are crucial for sustainable manufacturing. These enhancements can be in terms of increased throughput; better yield, conversion, and selectivity; sm… Show more
“…[40,[108][109][110][111] In this respect, continuous flow processing is essential. [115] Above that, steady state processing in flow allows a fine product tuning and can decrease deviations in the product properties and composition.…”
Section: Reactor Engineering Aspects For Biomass Conversionmentioning
confidence: 99%
“…[114] Many newly developed process intensification methods (e. g., reactive distillation, centrifugal reactors, microreactors, reactors assisted by ultrasonic or microwave irradiation) are rarely used in the industry to this date or at least is not a common practice yet. [115]…”
Section: Reactor Engineering Aspects For Biomass Conversionmentioning
Biomass as a renewable and abundantly available carbon source is a promising alternative to fossil resources for the production of chemicals and fuels. The development of biobased chemistry, along with catalyst design, has received much research attention over recent years. However, dedicated reactor concepts for the conversion of biomass and its derivatives are a relatively new research field. Continuous flow microreactors are a promising tool for process intensification, especially for reactions in multiphase systems. In this work, the potential of microreactors for the catalytic conversion of biomass derivatives to value-added chemicals and fuels is critically reviewed. Emphases are laid on the biphasic synthesis of furans from sugars, oxidation and hydrogenation of biomass derivatives. Microreactor processing has been shown capable of improving the efficiency of many biobased reactions, due to the transport intensification and a fine control over the process. Microreactors are expected to contribute in accelerating the technological development of biomass conversion and have a promising potential for industrial application in this area.
“…[40,[108][109][110][111] In this respect, continuous flow processing is essential. [115] Above that, steady state processing in flow allows a fine product tuning and can decrease deviations in the product properties and composition.…”
Section: Reactor Engineering Aspects For Biomass Conversionmentioning
confidence: 99%
“…[114] Many newly developed process intensification methods (e. g., reactive distillation, centrifugal reactors, microreactors, reactors assisted by ultrasonic or microwave irradiation) are rarely used in the industry to this date or at least is not a common practice yet. [115]…”
Section: Reactor Engineering Aspects For Biomass Conversionmentioning
Biomass as a renewable and abundantly available carbon source is a promising alternative to fossil resources for the production of chemicals and fuels. The development of biobased chemistry, along with catalyst design, has received much research attention over recent years. However, dedicated reactor concepts for the conversion of biomass and its derivatives are a relatively new research field. Continuous flow microreactors are a promising tool for process intensification, especially for reactions in multiphase systems. In this work, the potential of microreactors for the catalytic conversion of biomass derivatives to value-added chemicals and fuels is critically reviewed. Emphases are laid on the biphasic synthesis of furans from sugars, oxidation and hydrogenation of biomass derivatives. Microreactor processing has been shown capable of improving the efficiency of many biobased reactions, due to the transport intensification and a fine control over the process. Microreactors are expected to contribute in accelerating the technological development of biomass conversion and have a promising potential for industrial application in this area.
“…Various engineering strategies have been devised for process intensification in O 2 ‐dependent biocatalysis (Gemoets et al, ; Karande et al, ; Mallia & Baxendale, ; Utikar & Ranade, ). The k L a was common target in an overall approach aimed at OTR optimization.…”
Section: Introductionmentioning
confidence: 99%
“…Microreaction technology offers different ways of gas–liquid contacting with high efficiency (Karande et al, ; Kashid, Renken, & Kiwi‐Minsker, ; Stone, Hilliard, He, & Wang, ; Utikar & Ranade, ; Yue, ). The specific surface area ( a ), the mass transfer coefficient ( k L ) or both are enhanced in consequence of the reactor's internal microstructure and the resulting fluidics of the two‐phase flow (Brzozowski, O'Brien, Ley, & Polyzos, ; Dencic, Hessel, et al, ; Dencic, Meuldijk, et al, ; Utikar & Ranade, ). k L a values of up to 30 min −1 were reported for segmented gas–liquid flow in microchannels (Kashid et al, ).…”
Oxidative O
2
‐dependent biotransformations are promising for chemical synthesis, but their development to an efficiency required in fine chemical manufacturing has proven difficult. General problem for process engineering of these systems is that thermodynamic and kinetic limitations on supplying O
2
to the enzymatic reaction combine to create a complex bottleneck on conversion efficiency. We show here that continuous‐flow microreactor technology offers a comprehensive solution. It does so by expanding the process window to the medium pressure range (here, ≤34 bar) and thus enables biotransformations to be conducted in a single liquid phase at boosted concentrations of the dissolved O
2
(here, up to 43 mM). We take reactions of glucose oxidase and
d
‐amino acid oxidase as exemplary cases to demonstrate that the pressurized microreactor presents a powerful engineering tool uniquely apt to overcome restrictions inherent to the individual O
2
‐dependent transformation considered. Using soluble enzymes in liquid flow, we show reaction rate enhancement (up to six‐fold) due to the effect of elevated O
2
concentrations on the oxidase kinetics. When additional catalase was used to recycle dissolved O
2
from the H
2
O
2
released in the oxidase reaction, product formation was doubled compared to the O
2
supplied, in the absence of transfer from a gas phase. A packed‐bed reactor containing oxidase and catalase coimmobilized on porous beads was implemented to demonstrate catalyst recyclability and operational stability during continuous high‐pressure conversion. Product concentrations of up to 80 mM were obtained at low residence times (1–4 min). Up to 360 reactor cycles were performed at constant product release and near‐theoretical utilization of the O
2
supplied. Therefore, we show that the pressurized microreactor is practical embodiment of a general reaction‐engineering concept for process intensification in enzymatic conversions requiring O
2
as the cosubstrate.
“…Van Gerven and Stankiewicz give a detailed review of the history of process intensification and a perspective on the ongoing practical challenges in process intensification recently graced these pages . Additionally, researchers have worked to develop computational process intensification design tools for process design and for the intensification of multiphase reactions and reactors …”
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