Development of evaluation method for photocatalytic ability by ion chromatography combined with a flow-type reactor: Application to immobilized photocatalyst materials prepared by double-layer coating method

Author(s):  
Tsuyoshi Sugita ◽  
Kentaro Kobayashi ◽  
Taiki Yamazaki ◽  
Mayu Isaka ◽  
Hideyuki Itabashi ◽  
...  
2018 ◽  
Vol 34 (12) ◽  
pp. 1449-1453 ◽  
Author(s):  
Masanobu MORI ◽  
Tsuyoshi SUGITA ◽  
Kengo FUJII ◽  
Taiki YAMAZAKI ◽  
Mayu ISAKA ◽  
...  

2018 ◽  
Vol 59 (4) ◽  
pp. 444-449 ◽  
Author(s):  
Yu. V. Popov ◽  
V. M. Mokhov ◽  
D. N. Nebykov ◽  
S. E. Latyshova ◽  
K. V. Shcherbakova ◽  
...  

2018 ◽  
Vol 10 (4) ◽  
pp. 344-352 ◽  
Author(s):  
R. G. Kukushkin ◽  
P. M. Eletskii ◽  
O. O. Zaikina ◽  
G. A. Sosnin ◽  
O. A. Bulavchenko ◽  
...  

2020 ◽  
Vol 8 (13) ◽  
pp. 6183-6189 ◽  
Author(s):  
Fei Shen ◽  
Kaiming Wang ◽  
Yuting Yin ◽  
Le Shi ◽  
Dingyuan Zeng ◽  
...  

A PAN fiber/PI sphere double-layer coating serves as an interfacial functional layer to guide uniform Li deposition.


1964 ◽  
Vol 19 (12) ◽  
pp. 994-996 ◽  
Author(s):  
J.G. van de Vusse

Catalysts ◽  
2020 ◽  
Vol 10 (11) ◽  
pp. 1270
Author(s):  
Yuanyuan Zhao ◽  
Kansei Konishi ◽  
Eiji Minami ◽  
Shiro Saka ◽  
Haruo Kawamoto

Ru-Sn/TiO2 is an effective catalyst for hydrogenation of aqueous acetic acid to ethanol. In this paper, a similar hydrogenation process was investigated in a flow-type rather than a batch-type reactor. The optimum temperature was 170 °C for the batch-type reactor because of gas production at higher temperatures; however, for the flow-type reactor, the ethanol yield increased with reaction temperature up to 280 °C and then decreased sharply above 300 °C, owing to an increase in the acetic acid recovery rate. The selectivity for ethanol formation was improved over the batch process, and an ethanol yield of 98 mol % was achieved for a 6.7 min reaction (cf. 12 h for batch) (liquid hourly space velocity: 1.23 h−1). Oxidation of ethanol to acetic acid (i.e., the reverse reaction) adversely affected the hydrogenation. On the basis of these results, hydrogenation mechanisms that include competing side reactions are discussed in relation to the reactor type. These results will help the development of more efficient catalytic procedures. This method was also effectively applied to hydrogenation of lactic acid to propane-1,2-diol.


1986 ◽  
Vol 72 (8) ◽  
pp. 976-983 ◽  
Author(s):  
Toru HONJO ◽  
Kazuaki KYONO ◽  
Koji YAMATO ◽  
Toshio ICHIDA ◽  
Toshio IRIE

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