Development of an ultrahigh-temperature process for the enzymatic hydrolysis of lactose. IV. Immobilization of two thermostable ?-glycosidases and optimization of a packed-bed reactor for lactose conversion

2002 ◽  
Vol 77 (6) ◽  
pp. 619-631 ◽  
Author(s):  
Inge Petzelbauer ◽  
Bernhard Kuhn ◽  
Barbara Splechtna ◽  
Klaus D. Kulbe ◽  
Bernd Nidetzky
Keyword(s):  
Enzymatic Hydrolysis ◽  
Packed Bed ◽  
Packed Bed Reactor ◽  
Ultrahigh Temperature ◽  
Hydrolysis Of ◽  
Lactose Conversion

An approach in mathematical modeling of an upflow packed-bed reactor for enzymatic hydrolysis of wheat straw

1989 ◽  
Vol 34 (2) ◽  
pp. 242-251 ◽  
Author(s):  
G. Gonzàlez ◽  
G. Caminal ◽  
C. de Mas ◽  
J. Lòpez-Santín
Keyword(s):  
Mathematical Modeling ◽  
Enzymatic Hydrolysis ◽  
Wheat Straw ◽  
Packed Bed ◽  
Packed Bed Reactor ◽  
Hydrolysis Of

Modeling and Optimization of Lipase-Catalyzed Partial Hydrolysis for Diacylglycerol Production in Packed Bed Reactor

2016 ◽  
Vol 12 (7) ◽  
pp. 681-689 ◽  
Author(s):  
Eng-Tong Phuah ◽  
Yee-Ying Lee ◽  
Teck-Kim Tang ◽  
Oi-Ming Lai ◽  
Thomas Shean-Yaw Choong ◽  
...  
Keyword(s):  
Immobilized Enzyme ◽  
Rhizomucor Miehei ◽  
Packed Bed ◽  
Packed Bed Reactor ◽  
Partial Hydrolysis ◽  
Optimal Conditions ◽  
Lack Of Fit ◽  
Bed Height ◽  
Hydrolysis Of ◽  
Quadratic Models

Abstract Response surface methodology (RSM) was employed to optimize the process variables namely packed bed height (cm) and flow rates (ml/min) on diacylglycerol (DAG) production via partial hydrolysis of palm oil using immobilized Rhizomucor miehei lipase in packed bed reactor (PBR). Quadratic models were successfully developed for both DAG(y) and unhydrolyzed triacylglycerol ((un)TAG) with determination coefficient (R2) of 0.9931 and 0.9986, respectively coupled with insignificant lack of fit (p > 0.05). Optimal conditions for DAG synthesis were evaluated to be 10 cm packed bed height and 3.8 ml/min flow rate. Immobilized enzyme can be reused up to 10 times without significant changes in enzymatic activity. The partial hydrolysis under studied was found to be mass transfer-controlled.

Hydrolysis of carbonyl sulfide over modified Al2O3 by platinum and barium in a packed-bed reactor

2019 ◽  
pp. 1-10 ◽  
Author(s):  
K. Nimthuphariyha ◽  
A. Usmani ◽  
N. Grisdanurak ◽  
E. Kanchanatip ◽  
M. Yan ◽  
...  
Keyword(s):  
Carbonyl Sulfide ◽  
Packed Bed ◽  
Packed Bed Reactor ◽  
Hydrolysis Of

Hydrolysis of milk lactose in a packed bed reactor system using immobilized yeast cells

2010 ◽  
Vol 86 (1) ◽  
pp. 42-46 ◽  
Author(s):  
Reeba Panesar ◽  
Parmjit S. Panesar ◽  
Ram S. Singh ◽  
John F. Kennedy
Keyword(s):  
Packed Bed ◽  
Reactor System ◽  
Packed Bed Reactor ◽  
Yeast Cells ◽  
Immobilized Yeast ◽  
Immobilized Yeast Cells ◽  
Hydrolysis Of

Lipase-mediated hydrolysis of hempseed oil in a packed-bed reactor and in-line purification of PUFA as mono- and diacylglycerols

2020 ◽  
Vol 123 ◽  
pp. 345-353
Author(s):  
T. Bavaro ◽  
I. Benucci ◽  
A. Pedrali ◽  
G. Marrubini ◽  
M. Esti ◽  
...  
Keyword(s):  
Packed Bed ◽  
Packed Bed Reactor ◽  
Hydrolysis Of
Sign in / Sign up

Export Citation Format

Share Document