Maltodextrin hydrolysis in a fluidized-bed immobilized enzyme reactor

1986 ◽  
Vol 28 (2) ◽  
pp. 151-159 ◽  
Author(s):  
I. Vallat ◽  
P. Monsan ◽  
J. P. Riba
Keyword(s):  
Fluidized Bed ◽  
Immobilized Enzyme ◽  
Enzyme Reactor ◽  
Immobilized Enzyme Reactor

scholarly journals Performance of a zigzag fluidized bed as an immobilized enzyme reactor.

1984 ◽  
Vol 48 (5) ◽  
pp. 1131-1137 ◽  
Author(s):  
Kozo NAKAMURA ◽  
Hitoshi KUMAGAI ◽  
Toshimasa YANO
Keyword(s):  
Fluidized Bed ◽  
Immobilized Enzyme ◽  
Enzyme Reactor ◽  
Immobilized Enzyme Reactor

scholarly journals Performance of a Zigzag Fluidized Bed as an Immobilized Enzyme Reactor

1984 ◽  
Vol 48 (5) ◽  
pp. 1131-1137
Author(s):  
Kozo Nakamura ◽  
Hitoshi Kumagai ◽  
Toshimasa Yano
Keyword(s):  
Fluidized Bed ◽  
Immobilized Enzyme ◽  
Enzyme Reactor ◽  
Immobilized Enzyme Reactor

scholarly journals Study of the geometry of open channels in a layer-bed-type microfluidic immobilized enzyme reactor

2021 ◽  
Author(s):  
Cynthia Nagy ◽  
Robert Huszank ◽  
Attila Gaspar
Keyword(s):  
Immobilized Enzyme ◽  
High Surface ◽  
Volume Ratio ◽  
Volumetric Flow Rate ◽  
Enzyme Reactor ◽  
Channel Pattern ◽  
Immobilized Enzyme Reactor ◽  
Split Flow ◽  
Parallel Streams ◽  
Enzymatic Microreactors

AbstractThis paper aims at studying open channel geometries in a layer-bed-type immobilized enzyme reactor with computer-aided simulations. The main properties of these reactors are their simple channel pattern, simple immobilization procedure, regenerability, and disposability; all these features make these devices one of the simplest yet efficient enzymatic microreactors. The high surface-to-volume ratio of the reactor was achieved using narrow (25–75 μm wide) channels. The simulation demonstrated that curves support the mixing of solutions in the channel even in strong laminar flow conditions; thus, it is worth including several curves in the channel system. In the three different designs of microreactor proposed, the lengths of the channels were identical, but in two reactors, the liquid flow was split to 8 or 32 parallel streams at the inlet of the reactor. Despite their overall higher volumetric flow rate, the split-flow structures are advantageous due to the increased contact time. Saliva samples were used to test the efficiencies of the digestions in the microreactors. Graphical abstract

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