Improvement of Ethylene Removal Performance by Adsorption/Oxidation in a Pin-Type Corona Discharge Coupled with Pd/ZSM-5 Catalyst

被引:17
|
作者
Saud, Shirjana [1 ]
Duc Ba Nguyen [1 ,2 ]
Kim, Seung-Geon [1 ]
Lee, Ho Won [1 ]
Kim, Seong Bong [3 ]
Mok, Young Sun [1 ]
机构
[1] Jeju Natl Univ, Dept Chem & Biol Engn, Jeju 63243, South Korea
[2] Duy Tan Univ, Inst Res & Dev, Ctr Adv Chem, 03 Quang Trung, Da Nang 550000, Vietnam
[3] Natl Fus Res Inst, Plasma Technol Res Ctr, Jeollabuk Do 54004, South Korea
关键词
ethylene removal; Pd; ZSM-5; adsorption; corona discharge; plasma-catalytic oxidation; ATMOSPHERIC-PRESSURE PLASMAS; DECOMPOSITION; OXIDATION; STORAGE; GAS;
D O I
10.3390/catal10010133
中图分类号
O64 [物理化学(理论化学)、化学物理学];
学科分类号
070304 ; 081704 ;
摘要
The adsorption and plasma-catalytic oxidation of dilute ethylene were performed in a pin-type corona discharge-coupled Pd/ZSM-5 catalyst. The catalyst has an adsorption capacity of 320.6 mu mol gcat-1. The catalyst was found to have two different active sites activated at around 340 and 470 degrees C for ethylene oxidation. The removal of ethylene in the plasma catalyst was carried out by cyclic operation consisting of repetitive steps: (1) adsorption (60 min) followed by (2) plasma-catalytic oxidation (30 min). For the purpose of comparison, the removal of ethylene in the continuous plasma-catalytic oxidation mode was also examined. The ethylene adsorption performance of the catalyst was improved by the cyclic plasma-catalytic oxidation. With at least 80% of C2H4 in the feed being adsorbed, the cyclic plasma-catalytic oxidation was carried out for the total adsorption time of 8 h, whereas it occurred within 2 h of early adsorption in the case of catalyst alone. There was a slight decrease in catalyst adsorption capability with an increased number of adsorption cycles due to the incomplete release of CO2 during the plasma-catalytic oxidation step. However, the decreased rate of adsorption capacity was negligible, which is less than one percent per cycle. Since the activation temperature of all active sites of Pd/ZSM-5 for ethylene oxidation is 470 degrees C, the specific input energy requirement by heating the feed gas in order to activate the catalyst is estimated to be 544 J/L. This value is higher than that of the continuous plasma-catalytic oxidation (450 J/L) for at least 86% ethylene conversion. Interestingly, the cyclic adsorption and plasma-catalytic oxidation of ethylene is not only a low-temperature oxidation process but also reduces energy consumption. Specifically, the input energy requirement was 225 J/L, which is half that of the continuous plasma-catalytic oxidation; however, the adsorption efficiency and conversion rate were maintained. To summarize, cyclic plasma treatment is an effective ethylene removal technique in terms of low-temperature oxidation and energy consumption.
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页数:13
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