Removal Of Hydrogen Sulfide From Biogas Using Ceo2 Naoh Psac Synthesis And Performance From Laboratory Scale To Scale Up Process Design
In this study, CeO2/NaOH/PSAC sorbent was successfully synthesized and applied in hydrogen sulfide removal from biogas. Preliminary study showed that the best synthesis route was using soaking method to impregnate cerium oxide and sodium hydroxide onto palm shell activated carbon (PSAC). In addit...
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| 格式: | Thesis |
| 语言: | English |
| 出版: |
2015
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| 主题: | |
| 在线阅读: | http://eprints.usm.my/47075/1/Removal%20Of%20Hydrogen%20Sulfide%20From%20Biogas%20Using%20Ceo2%20Naoh%20Psac%20Synthesis%20And%20Performance%20From%20Laboratory%20Scale%20To%20Scale%20Up%20Process%20Design.pdf |
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| 总结: | In this study, CeO2/NaOH/PSAC sorbent was successfully synthesized and
applied in hydrogen sulfide removal from biogas. Preliminary study showed that the
best synthesis route was using soaking method to impregnate cerium oxide and
sodium hydroxide onto palm shell activated carbon (PSAC). In addition, calcination
must be applied as final step of the preparation because it increased the sorption
capacity. Preparation parameters studied were impregnation time (0 – 180 min),
cerium amount (1 – 10% wt Ce), sodium hydroxide concentration (0.2 – 1.0M
NaOH), calcination temperature (250 – 500oC) and duration (1 – 4 hours).
Optimization of sorbent preparation parameters was successful and the optimum
values were 1.5 hours impregnation time, 5 wt% cerium, 1.0 M NaOH, 400oC
calcination temperature and 3 hours of calcination time. Operating parameters that
were found to affect the sorption capacity were sorption temperature, H2S
concentration, sorbent amount, and flow rate. Maximum value of sorption capacity
can be identified for each of these operating parameters. Moreover, other gas
components such as water, carbon dioxide and methane can also affect the sorption
capacity differently. Data analysis showed that Freundlich sorption isotherm can best
described the sorption behavior. Thermodynamic study showed that enthalpy change
(ΔH) and entropy change (ΔS) were calculated to be –6.0 kJ/mol and 25.7 J/mol.K.
The sorption was pseudo–second order with activation energy 11.7 kJ/mol and rate
constant was between 2.387–4.066 X 10-6 g/mg.min for temperature 30–70oC.
Breakthrough curve was fitted well by using breakthrough model developed by Chu
(2004). Up to 78% of original sorption capacity was achieved in the regeneration
study using heat treatment under inert atmosphere. The regeneration temperature and
time were 500oC and 4 hours, respectively. Scale up sorption process using the
developed CeO2/NaOH/PSAC sorbent was successfully designed with a rate of
return (ROR) of two years. Simulation study was also performed and increased
efficiency at higher flow rate and smaller sorption column was discovered. |
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