Regeneration of granular activated carbon saturated with acetone and isopropyl alcohol via a recirculation process under H2O2/UV oxidation

被引:43
作者
Horng, Richard S. [1 ]
Tseng, I. -Chin [1 ]
机构
[1] I Shou Univ, Dept Chem Engn, Kaohsiung 840, Taiwan
关键词
carbon regeneration; advanced oxidation; hydrogen peroxide; pH; GAC;
D O I
10.1016/j.jhazmat.2007.10.033
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
This study examines a water-based system, coupling an adsorber and a photoreactor, for regeneration of granular activated carbon (GAC) saturated with acetone and isopropyl alcohol (IPA). Through water recirculation the regeneration reaction was operated in both intermittent and continuous ultraviolet illumination modes. With a periodic dosage of hydrogen peroxide not only was regeneration efficient but it was also catalyzed by GAC in the adsorber. The concentrations of acetone, solution chemical oxygen demand (COD), pH and organic residues on GAC surfaces were measured during regenerations. Both pH and solution COD were found to correlate with regeneration completion as measured by organic residue on GAC surfaces in four regeneration cycles with acetone. Solution pH decreased to the acidic values and then returned to near its original value when organic residues were 0.085-0.255 mg/g GAC, that is, destruction efficiency of adsorbed acetone on the GAC surface was more than 99%. Likewise, solution COD became low (<100 mg/l) at regeneration completion. The pH variation pattern was then applied to another four cycles of regeneration with IPA, and successfully reflected the timing of complete regeneration. The final levels of organic residue on GAC surfaces were between 0.135 and 0.310 mg/g GAC in each of four regeneration cycles, each of which had been stopped based on the measurements of pH and solution COD. Furthermore, nearly the same batch of GAC could be repeatedly used with little changes in physicochemical properties in each of eight cycles: adsorptive capacities were 95 +/- 7 mg acetone/g GAC and 87 +/- 3 mg IPA/g GAC, and breakthrough time was 0.86 +/- 0.05 for acetone and 0.78 +/- 0.03 h for IPA. An economic assessment of the system showed that the operating cost was about 0.04 USD for treating every gram of acetone in the air. (C) 2007 Elsevier B.V. All rights reserved.
引用
收藏
页码:366 / 372
页数:7
相关论文
共 32 条
[1]   Comparison between thermal and ozone regenerations of spent activated carbon exhausted with phenol [J].
Alvarez, PM ;
Beltrán, FJ ;
Gómez-Serrano, V ;
Jaramillo, J ;
Rodríguez, EM .
WATER RESEARCH, 2004, 38 (08) :2155-2165
[2]   Microwave-induced regeneration of activated carbons polluted with phenol.: A comparison with conventional thermal regeneration [J].
Ania, CO ;
Menéndez, JA ;
Parra, JB ;
Pis, JJ .
CARBON, 2004, 42 (07) :1383-1387
[3]  
[Anonymous], 1992, STAND METH EX WAT WA
[4]   Supercritical CO2 regeneration of activated carbon loaded with organic adsorbates [J].
Chihara, K ;
Oomori, K ;
Oono, T ;
Mochizuki, Y .
WATER SCIENCE AND TECHNOLOGY, 1997, 35 (07) :261-268
[5]  
Clifford A. L., 1997, US Pat., Patent No. [5702587, 5702587 A]
[6]   Impact of drinking water preozonation on granular activated carbon quality and performance [J].
Dussert, BW ;
Kovacic, SL .
OZONE-SCIENCE & ENGINEERING, 1997, 19 (01) :1-11
[7]  
GOMEZSERRANO V, 1996, INFORM TECNOL, V7, P61
[8]   PH indications in aqueous organic photodecompositions with carbonyl and hydroxyl groups [J].
Horng, RS .
CHEMOSPHERE, 2004, 55 (05) :757-762
[9]   Combination of activated carbon adsorption with light-enhanced chemical oxidation via hydrogen peroxide [J].
Ince, NH ;
Apikyan, IG .
WATER RESEARCH, 2000, 34 (17) :4169-4176
[10]   Activated carbon and carbon black catalyzed transformation of aqueous ozone into OH-radicals [J].
Jans, U ;
Hoigne, J .
OZONE-SCIENCE & ENGINEERING, 1998, 20 (01) :67-90