Influence of Purge Gas Flow and Heating Rates on Volatile Organic Compound Decomposition during Regeneration of an Activated Carbon Fiber Cloth

Five-cycle adsorption/regeneration experiments using 1,2,4-trimethylbenzene (TMB) were completed at different purge gas flow and heating rates to identify their impact on heel buildup. Regeneration of a saturated activated carbon fiber cloth was completed at 400 °C using resistive heating at different heating rates and purge gas flow. At 1 standard liter per minute (SLPM) desorption purge gas, increasing the regeneration heating rate from 5 to 100 °C/min increased heel buildup from 4.6 to 10.4 wt % and adsorption capacity loss from 7.8 to 52.0%. On the other hand, at 70 °C/min heating rate, increasing the purge gas flow rate from 0.1 to 5 SLPM decreased heel buildup from 14.6 to 1.4% and capacity loss from 82.3 to 2.1%. Increasing the heating rate or decreasing the purge gas flow results in higher TMB concentrations being exposed to the high desorption temperature and higher residence time of TMB in the adsorbent pores. This increases adsorbate decomposition, causing deposition of pore-blocking, high carbon content residue (coke) onto the adsorbent surface. These results show the importance of optimizing desorption conditions to minimize heel buildup during cyclic use, contrary to conventional wisdom, suggesting that higher heating rates are consistently preferred, and provide improvements in energy use.

[1]  Masoud Jahandar Lashaki,et al.  Effect of desorption purge gas oxygen impurity on irreversible adsorption of organic vapors , 2016 .

[2]  Masoud Jahandar Lashaki,et al.  Heel formation during volatile organic compound desorption from activated carbon fiber cloth , 2016 .

[3]  Hongfei Lin,et al.  Understanding capacity loss of activated carbons in the adsorption and regeneration process for denitrogenation and desulfurization of diesel fuels , 2014 .

[4]  J. F. González,et al.  Two stage thermal regeneration of exhausted activated carbons. Steam gasification of effluents , 2013 .

[5]  J. Ancheyta Modeling of Processes and Reactors for Upgrading of Heavy Petroleum , 2013 .

[6]  James E. Anderson,et al.  Adsorption and desorption of mixtures of organic vapors on beaded activated carbon. , 2012, Environmental science & technology.

[7]  J. A. Menéndez,et al.  Low temperature regeneration of activated carbons using microwaves: revising conventional wisdom. , 2012, Journal of environmental management.

[8]  Masoud Jahandar Lashaki,et al.  Effect of adsorption and regeneration temperature on irreversible adsorption of organic vapors on beaded activated carbon. , 2012, Environmental science & technology.

[9]  David L Johnsen,et al.  Capture and recovery of isobutane by electrothermal swing adsorption with post-desorption liquefaction. , 2010, Environmental science & technology.

[10]  P. Carrott,et al.  Adsorption of volatile organic compounds onto activated carbon cloths derived from a novel regenerated cellulosic precursor. , 2010, Journal of hazardous materials.

[11]  D. Cazorla-Amorós,et al.  Regeneration of activated carbons saturated with benzene or toluene using an oxygen-containing atmosphere , 2010 .

[12]  B. Feng,et al.  Desorption of CO2 from activated carbon fibre-phenolic resin composite by electrothermal effect , 2010 .

[13]  J. Bernhard,et al.  Role of functional groups on the microwave attenuation and electric resistivity of activated carbon fiber cloth , 2009 .

[14]  G. Sorial,et al.  The effect of functional groups on oligomerization of phenolics on activated carbon. , 2007, Journal of hazardous materials.

[15]  L. Luo,et al.  Electrothermal swing adsorption of toluene on an activated carbon monolith Experiments and parametric theoretical study , 2007 .

[16]  J. A. Menéndez,et al.  Effect of microwave and conventional regeneration on the microporous and mesoporous network and on the adsorptive capacity of activated carbons , 2005 .

[17]  M. Rood,et al.  Activated carbon fiber cloth electrothermal swing adsorption system. , 2004, Environmental Science and Technology.

[18]  G. Sorial,et al.  Adsorption of phenolics on activated carbon--impact of pore size and molecular oxygen. , 2004, Chemosphere.

[19]  P. Cloirec,et al.  Adsorption onto Activated Carbon Cloths and Electrothermal Regeneration: Its Potential Industrial Applications , 2004 .

[20]  M. Rood,et al.  Capture of Organic Vapors Using Adsorption and Electrothermal Regeneration , 2004 .

[21]  M. Rood,et al.  Organic vapor recovery and energy efficiency during electric regeneration of an activated carbon fiber cloth adsorber , 2004 .

[22]  G. Sorial,et al.  The role of adsorbent pore size distribution in multicomponent adsorption on activated carbon , 2004 .

[23]  J. J. Pis,et al.  Microwave-induced regeneration of activated carbons polluted with phenol. A comparison with conventional thermal regeneration , 2004 .

[24]  J. Rouquerol,et al.  Sample Controlled Thermal Analysis , 2003 .

[25]  P. Cloirec,et al.  Electrical behaviour of activated carbon cloth heated by the joule effect: desorption application , 2001 .

[26]  S. Vinitnantharat,et al.  Quantitative Bioregeneration of Granular Activated Carbon Loaded with Phenol and 2,4-Dichlorophenol , 2001, Environmental technology.

[27]  S. Vinitnantharat,et al.  Competitive Removal of Phenol and 2,4-Dichlorophenol in Biological Activated Carbon System , 2000 .

[28]  S. Larson,et al.  Activated carbon cloth adsorption-cryogenic system to recover toxic volatile organic compounds , 1996 .

[29]  C. Moreno-Castilla,et al.  Thermal desorption of chlorophenols from activated carbons with different porosity , 1995 .

[30]  C. King,et al.  Mechanism of irreversible adsorption of phenolic compounds by activated carbons , 1990 .

[31]  M. Manes,et al.  Adsorptive displacement analysis of many-component priority pollutants on activated carbon. , 1987, Environmental science & technology.

[32]  C. Cramers,et al.  Mechanisms of the thermal degradation of alkylbenzenes , 1974 .