A continuous-flow biodiesel production process using a rotating packed bed

2010 ◽  
Vol 101 (2) ◽  
pp. 668-673 ◽  
Author(s):  
Yi-Hung Chen ◽  
Yu-Hang Huang ◽  
Rong-Hsien Lin ◽  
Neng-Chou Shang
Keyword(s):  
Production Process ◽  
Continuous Flow ◽  
Packed Bed ◽  
Biodiesel Production ◽  
Rotating Packed Bed

scholarly journals Biodiesel production in a rotating packed bed using K/γ-Al2O3 solid catalyst

2011 ◽  
Vol 42 (6) ◽  
pp. 937-944 ◽  
Author(s):  
Yi-Hung Chen ◽  
Yu-Hang Huang ◽  
Rong-Hsien Lin ◽  
Neng-Chou Shang ◽  
Ching-Yuan Chang ◽  
...  
Keyword(s):  
Packed Bed ◽  
Biodiesel Production ◽  
Solid Catalyst ◽  
Rotating Packed Bed

scholarly journals Continuous-flow Esterification of Free Fatty Acids in a Rotating Packed Bed

2010 ◽  
Vol 49 (9) ◽  
pp. 4117-4122 ◽  
Author(s):  
Yi-Hung Chen ◽  
Liang-Chi Wang ◽  
Cheng-Hsien Tsai ◽  
Neng-Chou Shang
Keyword(s):  
Fatty Acids ◽  
Free Fatty Acids ◽  
Continuous Flow ◽  
Packed Bed ◽  
Rotating Packed Bed

Design of a continuous flow immobilized-cell reactor for biosynthetical production of L-aspartic acid

1985 ◽  
Vol 50 (10) ◽  
pp. 2122-2133 ◽  
Author(s):  
Jindřich Zahradník ◽  
Marie Fialová ◽  
Jan Škoda ◽  
Helena Škodová
Keyword(s):  
Aspartic Acid ◽  
Continuous Flow ◽  
Immobilized Cells ◽  
Scale Up ◽  
Fixed Bed ◽  
Packed Bed ◽  
Fixed Bed Reactor ◽  
Experimental Program ◽  
Design Parameters ◽  
Immobilized Cell

An experimental study was carried out aimed at establishing a data base for an optimum design of a continuous flow fixed-bed reactor for biotransformation of ammonium fumarate to L-aspartic acid catalyzed by immobilized cells of the strain Escherichia alcalescens dispar group. The experimental program included studies of the effect of reactor geometry, catalytic particle size, and packed bed arrangement on reactor hydrodynamics and on the rate of substrate conversion. An expression for the effective reaction rate was derived including the effect of mass transfer and conditions of the safe conversion-data scale-up were defined. Suggestions for the design of a pilot plant reactor (100 t/year) were formulated and decisive design parameters of such reactor were estimated for several variants of problem formulation.

Support vector regression-based model for phenol adsorption in rotating packed bed adsorber

2021 ◽  
Author(s):  
Rameez Ahmad Aftab ◽  
Sadaf Zaidi ◽  
Mohd Danish ◽  
Sayed Mohammad Adnan ◽  
Khursheed B. Ansari ◽  
...  
Keyword(s):  
Support Vector Regression ◽  
Packed Bed ◽  
Support Vector ◽  
Phenol Adsorption ◽  
Rotating Packed Bed

Multilevel cross flow rotating packed bed to enhance gas film control mass transfer process

2021 ◽  
Vol 161 ◽  
pp. 108321
Author(s):  
Qing-Qing Duan ◽  
Zhi-Guo Yuan ◽  
You-Zhi Liu ◽  
Shan-Shan Duan ◽  
Xi-Fan Duan
Keyword(s):  
Mass Transfer ◽  
Transfer Process ◽  
Cross Flow ◽  
Mass Transfer Process ◽  
Packed Bed ◽  
Rotating Packed Bed

Enhancement of dispersion of nano-catalysts for catalytic hydrogenation of cinnamaldehyde by a rotating packed bed

2021 ◽  
Vol 240 ◽  
pp. 116641
Author(s):  
Kun Dong ◽  
Xiaoke Ma ◽  
Guang-Wen Chu ◽  
Hai-Kui Zou ◽  
Yong Luo ◽  
...  
Keyword(s):  
Catalytic Hydrogenation ◽  
Packed Bed ◽  
Rotating Packed Bed ◽  
Nano Catalysts

Rotating packed bed reactor for enzymatic synthesis of biodiesel

2017 ◽  
Vol 224 ◽  
pp. 292-297 ◽  
Author(s):  
Juntao Xu ◽  
Changsheng Liu ◽  
Meng Wang ◽  
Lei Shao ◽  
Li Deng ◽  
...  
Keyword(s):  
Enzymatic Synthesis ◽  
Packed Bed ◽  
Packed Bed Reactor ◽  
Rotating Packed Bed
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