Influence of operating parameters on gas phase photocatalytic oxidation of methyl-ethyl-ketone in a light emitting diode (LED)-fluidized bed reactor

被引:10
|
作者
Hajaghazadeh, Mohammad [1 ]
Vaiano, Vincenzo [2 ]
Sannino, Diana [2 ]
Kakooei, Hossein [3 ]
Sotudeh-Gharebagh, Rahmat [4 ]
机构
[1] Urmia Univ Med Sci, Hlth Fac, Dept Occupat Hlth, Orumiyeh, Iran
[2] Univ Salerno, Dept Ind Engn, Fisciano, Italy
[3] Univ Tehran Med Sci, Sch Publ Hlth, Dept Occupat Hlth, Tehran, Iran
[4] Univ Tehran, Oil & Gas Proc Ctr Excellence, Sch Chem Engn, Coll Engn, Tehran, Iran
关键词
Photocatalytic Oxidation; Relative Humidity; Temperature; Fluidized Bed Reactor; Ultraviolet Light Intensity; Selectivity to CO2 and CO; TIO2; PHOTOCATALYSIS; ORGANIC-COMPOUNDS; AIR PURIFICATION; TITANIUM-DIOXIDE; VISIBLE-LIGHT; WASTE-WATER; DEGRADATION; FORMALDEHYDE; KINETICS; TOLUENE;
D O I
10.1007/s11814-014-0239-4
中图分类号
O6 [化学];
学科分类号
0703 ;
摘要
The effect of operating parameters on gas phase photocatalytic oxidation of methyl ethyl ketone (MEK) has been investigated over P25 and PC500 photocatalysts. The parameters were gas flow rate, relative humidity (RH), reaction temperature, and ultraviolet intensity. The photoreactor was composed of two LEDs matrices and a fluidized bed reactor (LED-FBR). No mass transfer limitation phenomena occurred at flow rates in the range 30-70 NL/h. The oxidation of MEK over the two photocatalysts did not highly depend on the presence or absence of humidity in the air stream. Temperature was determined as an important parameter in conversion of MEK over 60 to 120 A degrees C, influencing also the selectivity to carbon dioxide and carbon monoxide. The simultaneous influence of RH and temperature was observed in the reaction at different temperatures and RHs, evidencing the decrease in the selectivity towards CO with increase of RH. With the increase of ultraviolet intensity, the rate of MEK oxidation increased over both catalysts, with the better activity of PC500 than P25 particularly at higher light intensities. The main effect of temperature was both to promote the MEK conversion and to limit the competitive water adsorption in the PCO reaction over the tested titanias.
引用
收藏
页码:636 / 642
页数:7
相关论文
共 6 条
  • [1] Influence of operating parameters on gas phase photocatalytic oxidation of methyl-ethyl-ketone in a light emitting diode (LED)-fluidized bed reactor
    Mohammad Hajaghazadeh
    Vincenzo Vaiano
    Diana Sannino
    Hossein Kakooei
    Rahmat Sotudeh-Gharebagh
    Korean Journal of Chemical Engineering, 2015, 32 : 636 - 642
  • [2] Heterogeneous photocatalytic oxidation of methyl ethyl ketone under UV-A light in an LED-fluidized bed reactor
    Hajaghazadeh, Mohammad
    Vaiano, Vincenzo
    Sannino, Diana
    Kakooei, Hossein
    Sotudeh-Gharebagh, Rahmat
    Ciambelli, Paolo
    CATALYSIS TODAY, 2014, 230 : 79 - 84
  • [3] PHOTOCATALYTIC DEGRADATION OF METHYL ETHYL KETONE BY NANO TiO2 IN A FLUIDIZED BED REACTOR
    Hajaghazadeh, Mohammad
    Kakooei, Hossein
    Dashliborun, Amir Motamed
    Sotudeh-Gharebagh, Rahmat
    Golbabaie, Farideh
    Afshar, Shahrara
    Foroushani, Abbas Rahimi
    FRESENIUS ENVIRONMENTAL BULLETIN, 2013, 22 (02): : 435 - 442
  • [4] PHOTOCATALYTIC DEGRADATION OF METHYL ETHYL KETONE IN A FLUIDIZED BED REACTOR: A FACTORIAL DESIGN ANALYSIS
    Hajaghazadeh, Mohammad
    Kakooei, Hossein
    Dashliborun, Amir Motamed
    Sotudeh-Gharebagh, Rahmat
    Golbabaie, Farideh
    Foroushani, Abbas Rahhimi
    Afshar, Shahrara
    FRESENIUS ENVIRONMENTAL BULLETIN, 2013, 22 (06): : 1719 - 1726
  • [5] Modeling of the photocatalytic degradation of methyl ethyl ketone in a fluidized bed reactor of nano-TiO2/γ-Al2O3 particles
    Dashliborun, Amir Motamed
    Sotudeh-Gharebagh, Rahmat
    Hajaghazadeh, Mohammad
    Kakooei, Hossein
    Afshar, Shahrara
    CHEMICAL ENGINEERING JOURNAL, 2013, 226 : 59 - 67
  • [6] TiO2 coating types influencing the role of water vapor on the photocatalytic oxidation of methyl ethyl ketone in the gas phase
    Raillard, C
    Héquet, V
    Le Cloirec, P
    Legrand, J
    APPLIED CATALYSIS B-ENVIRONMENTAL, 2005, 59 (3-4) : 213 - 220