scholarly journals Removal of Ethylene and By-products Using Dielectric Barrier Discharge with Ag Nanoparticle-Loaded Zeolite for Keeping Freshness of Fruits and Vegetables

2016 ◽  
Vol 41 (1) ◽  
pp. 41-45 ◽  
Author(s):  
Junki Nishimura ◽  
Katsuyuki Takahashi ◽  
Koichi Takaki ◽  
Shoji Koide ◽  
Masaya Suga ◽  
...  
2015 ◽  
Vol 135 (6) ◽  
pp. 320-327 ◽  
Author(s):  
Junki Nishimura ◽  
Tomoya Kawamura ◽  
Katsuyuki Takahashi ◽  
Yoshiyuki Teramoto ◽  
Koichi Takaki ◽  
...  

2017 ◽  
Vol 100 (2) ◽  
pp. 3-11 ◽  
Author(s):  
JUNKI NISHIMURA ◽  
TOMOYA KAWAMURA ◽  
KATSUYUKI TAKAHASHI ◽  
YOSHIYUKI TERAMOTO ◽  
KOICHI TAKAKI ◽  
...  

Catalysts ◽  
2020 ◽  
Vol 10 (5) ◽  
pp. 511 ◽  
Author(s):  
Wenjun Liang ◽  
Huipin Sun ◽  
Xiujuan Shi ◽  
Yuxue Zhu

In order to make full use of the heat in nonthermal plasma systems and decrease the generation of by-products, a reverse-flow nonthermal plasma reactor coupled with catalyst was used for the abatement of toluene. In this study, the toluene degradation performance of different reactors was compared under the same conditions. The mechanism of toluene abatement by nonthermal plasma coupled with catalyst was explored, combined with the generation of ozone (O3), NO2, and organic by-products during the reaction process. It was found that a long reverse cycle time of the reactor and a short residence time of toluene decreased the internal reactor temperature, which was not beneficial for the degradation of toluene. Compared with the dielectric barrier discharge (DBD) reactor, toluene degradation efficiency in the double dielectric barrier discharge (DDBD) reactor was improved at the same discharge energy level, but the concentrations of NO2 and O3 in the effluent were relatively high; this was improved after the introduction of a catalyst. In the reverse-flow nonthermal plasma reactor coupled with catalyst, the CO2 selectivity was the highest, while the selectivity and amount of NO2 was the lowest and aromatics, acids, and ketones were the main gaseous organic by-products in the effluent. The reverse-flow DBD-catalyst reactor was successful in decreasing organic by-products, while the types of organic by-products in the DDBD reactor were much more than those in the DBD reactor.


2016 ◽  
Vol 2016.26 (0) ◽  
pp. 306
Author(s):  
Katsuyuki TAKAHASHI ◽  
Junki NISHIMURA ◽  
Takuma MOTODATE ◽  
Koichi TAKAKI ◽  
Shoji KOIDE ◽  
...  

2012 ◽  
Vol 39 (3) ◽  
pp. 1021-1035 ◽  
Author(s):  
Hongbo Zhang ◽  
Kan Li ◽  
Tonghua Sun ◽  
Jingping Jia ◽  
Xueli Yang ◽  
...  

Author(s):  
Xin Liu ◽  
Jianqi Liu ◽  
Jia-yao Chen ◽  
Fangchuan Zhong

Abstract A novel strategy for degradation of high gaseous hourly space velocity (GHSV) benzene, toluene, xylene (BTX) by double dielectric barrier discharge (DDBD) coupled with Mn3O4/ activated carbon fibers (ACF) catalysts was proposed in this work. A series of Mn3O4/ACF catalysts were synthesized by hydrothermal method and characterized. The results showed that all the prepared catalysts could improve the degradation of BTX in DDBD system and inhibit the production of ozone. Among the catalysts with different Mn loading, the 5.6%Mn3O4/ACF, with the highest Mn(+3) content (43.2%) and the highest absorbed oxygen content (38.5%), presented the best catalytic performance. In 5.6%Mn3O4/ACF+DDBD system, the degradation efficiency of benzene, toluene and xylene could reach 49.9%, 79.7% and 97.1% respectively with SIE of 400 J L-1. The carbon balance and CO2 selectivity, meanwhile, were 83.3% and 51.1%, respectively. It seemed that Mn(+3) and absorbed oxygen content could be a reference for the catalytic performance of Mn3O4/ACF catalysts. The higher the Mn (Ⅲ) and absorbed oxygen, the better the catalytic performance of the Mn3O4/ACF catalysts. The organic by-products were identified by chromatography-mass spectrometry (GC-MS), and a possible reaction mechanism of BTX in DDBD reactor and catalyst surface was proposed based on the composition of organic by-products.


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