A Comparison of Chemical Bath Deposition of CdS from a Batch Reactor and a Continuous-Flow Microreactor

2007 ◽  
Vol 154 (9) ◽  
pp. D482 ◽  
Author(s):  
P. H. Mugdur ◽  
Y.-J. Chang ◽  
S-.Y. Han ◽  
Y-W. Su ◽  
A. A. Morrone ◽  
...  
2009 ◽  
Vol 12 (7) ◽  
pp. H244 ◽  
Author(s):  
Y.-J. Chang ◽  
Y.-W. Su ◽  
D.-H. Lee ◽  
S. O. Ryu ◽  
C.-H. Chang

2015 ◽  
Vol 80 (7) ◽  
pp. 853-866 ◽  
Author(s):  
Jun Wang ◽  
Gong An ◽  
Shuangshuang Gu ◽  
Hongsheng Cui ◽  
Xiangyang Wu

Isoquercitrin is a rare flavonol glycoside with a wide range of biological activities and is a key synthetic intermediate for the production of enzymatically modified isoquercitrin. In order to establish an ultrafast bioprocess for obtaining isoquercitrin, a novel continuous flow biosynthesis of isoquercitrin using the hesperidinase-catalyzed hydrolysis of rutin in a glass-polydimethylsiloxane (PDMS) microreactor was first carried out. Using the developed microchannel reactor (200?m width, 50?m depth, and 2 m length) with one T-shaped inlet and one outlet, the maximum yield of isoquercitrin (98.6%) was achieved in a short time (40 min) under the following optimum conditions: rutin concentration at 1 g L-1, hesperidinase concentration at 0.1 g mL-1, reaction temperature at 40?C, and a flow rate at 2 ?L min-1. The activation energy value Ea of the enzymatic reaction was 4.61 kJ mol-1, and the reaction rate and volumetric productivity were approximately 16.1-fold and 30% higher, respectively, than those in the batch reactor. Thus, the use of a continuous-flow microreactor for the enzymatic hydrolysis of rutin is an efficient and simple approach to achieve a relative high yield of isoquercitrin.


1992 ◽  
Vol 57 (4) ◽  
pp. 869-881 ◽  
Author(s):  
Italo Ferino ◽  
Roberto Monaci ◽  
Vincenzo Solinas ◽  
Lucio Forni ◽  
Antonio Rivoldini ◽  
...  

The behaviour of several zeolites as catalysts for the title reaction has been investigated by means of a continuous flow microreactor. Runs performed at atmospheric pressure indicated that at 423 K the completely protonic forms of the zeolites catalyze just the isomerization reaction. In the case of Y zeolites, oligomerization occurs only over the partially decationated samples, in the temperature range between 373 and 423 K and W/F between 0.2 and 22 gcath/g1-but, to an extent which depends on the reaction conditions. Most of the catalysts were tested also under pressure (4.05 MPa) at 423 K. The protonic forms of Y and ZSM-5 zeolites seem promising catalysts in terms of both conversion and selectivity to oligomers. The 1-olefins account for 30% of the entire olefinic mixture. The octenes, which account for 70% of the liquid mixture, are mostly formed of dimethylhexenes. Trimers are also formed during the reaction and, in the very particular case of H[B]ZSM-5, tetramers are produced.


2019 ◽  
Vol 144 ◽  
pp. 247-257 ◽  
Author(s):  
Haiyun Ma ◽  
Nan Jin ◽  
Peng Zhang ◽  
Yufei Zhou ◽  
Yuchao Zhao ◽  
...  

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