Volatile organic compound adsorption in a gas-solid fluidized bed.
Fluidization finds many process applications in the areas of catalytic reactions, drying, coating, combustion, gasification and microbial culturing. This work aims to compare the dynamic adsorption characteristics and adsorption rates in a bubbling fluidized bed and a fixed bed at the same gas flow-rate, gas residence time and bed height. Adsorption with 520 ppm methanol and 489 ppm isobutane by the ZSM-5 zeolite of different particle size in the two beds enabled the differentiation of the adsorption characteristics and rates due to bed type, intraparticle mass transfer and adsorbate-adsorbent interaction. Adsorption of isobutane by the more commonly used activated carbon provided the comparison of adsorption between the two adsorbent types. With the same gas residence time of 0.79 seconds in both the bubbling bed and fixed bed of the same bed size of 40 mm diameter and 48 mm height, the experimental results showed a higher rate of adsorption in the bubbling bed as compared to the fixed bed. Intraparticle mass transfer and adsorbent-adsorbate interaction played significant roles in affecting the rate of adsorption, with intraparticle mass transfer being more dominant. The bubbling bed was observed to have a steeper decline in adsorption rate with respect to increasing outlet concentration compared to the fixed bed. The adsorption capacities of zeolite for the adsorbates studied were comparatively similar in both beds; fluidizing, and using smaller particles in the bubbling bed did not increase the adsorption capacity of the ZSM-5 zeolite. The adsorption capacity of activated carbon for isobutane was much higher than the ZSM-5 zeolite for isobutane, although at a lower adsorption rate. Fourier transform infra-red (FTIR) spectroscopy was used as an analytical tool for the quantification of gas concentration. Calibration was done using a series of standards prepared by in situ dilution with nitrogen gas, based on the ideal gas law and relating partial pressure to gas concentration. Concentrations up to 220 ppm for methanol and 75 ppm for isobutane were prepared using this method.
Ng
Y L
YL
Institute of Environmental Science and Engineering, Nanyang Technological University, Innovation Centre, Block 2 Unit 237, 18 Nanyang Drive, 637723 Singapore. ngyl@ntu.edu.sg
Yan
R
R
Tsen
L T S
LT
Yong
L C
LC
Liu
M
M
Liang
D T
DT
D000327:Adsorption; D000393:Air Pollutants / Q000302:isolation & purification*; D002073:Butanes / Q000302:isolation & purification*; D002244:Carbon / Q000737:chemistry; D005740:Gases; D000432:Methanol / Q000302:isolation & purification*; D010316:Particle Size; D012997:Solvents / Q000302:isolation & purification*; D014835:Volatilization; D017641:Zeolites / Q000737:chemistry
D000393:Air Pollutants; D002073:Butanes; D005740:Gases; D012997:Solvents; D017641:Zeolites; D002244:Carbon; D000432:Methanol