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Original article

Comparative study of soils and other adsorbents for decolorizing sewage and livestock wastewater

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Pages 189-197 | Received 12 Aug 2006, Accepted 11 Dec 2006, Published online: 17 Dec 2010

Figures & data

Table 1 Soil classification, pH, particle size distribution, total carbon (TC), total nitrogen (TN), effective cation exchange capacity (eCEC) of Andisol, sandy soil and red soil used in the experiment

Table 2 pH value, original source, total surface area of micropores (A1), total outside surface area of micropores (A2), total surface area of mesopores (Ap), total volume of micropores (Vp) and mesopores (Vp), peak of the diameter of micropore distribution (Dp) and peak of the radius of mesopore distribution (Rp) of some of the activated carbon and charcoal used in the experiment

Table 3 Names, composition material, mixing percentage and bulk density of the columns in the recovery experiment

Figure 1  Experimental process for the recovery experiment. (a) Process for 7-day and 14-day incubation with saturation and (b) process for 3-day incubation without saturation.

Figure 1  Experimental process for the recovery experiment. (a) Process for 7-day and 14-day incubation with saturation and (b) process for 3-day incubation without saturation.

Table 4 Names, composition material, mixing percentage and bulk density of the columns in the continuous column experiment

Table 5 Experimental period, time, applied wastewater, hydraulic loading rate (HLR) and aeration conditions during the continuous column experiment period

Figure 2  Effect of the amount of adsorbent on the decolorization rates of sewage plant effluent. (a) Decolorization rates by soil and (b) decolorization rates by activated carbon and charcoal.

Figure 2  Effect of the amount of adsorbent on the decolorization rates of sewage plant effluent. (a) Decolorization rates by soil and (b) decolorization rates by activated carbon and charcoal.

Figure 3  The effect of the amount of adsorbent on the decolorization rate of livestock wastewater diluted by different amounts. (a) Decolorization rates by Andisol and zeolite for fivefold, 20-fold and 50-fold diluted wastewater, (b) decolorization rates by activated carbons (ACs) and charcoal for 5-fold diluted wastewater, (c) decolorization rates by ACs and charcoal for 20-fold diluted wastewater and (d) decolorization rates by ACs and charcoal for 50-fold diluted wastewater. Andi, andisol; zeo, zeolite.

Figure 3  The effect of the amount of adsorbent on the decolorization rate of livestock wastewater diluted by different amounts. (a) Decolorization rates by Andisol and zeolite for fivefold, 20-fold and 50-fold diluted wastewater, (b) decolorization rates by activated carbons (ACs) and charcoal for 5-fold diluted wastewater, (c) decolorization rates by ACs and charcoal for 20-fold diluted wastewater and (d) decolorization rates by ACs and charcoal for 50-fold diluted wastewater. Andi, andisol; zeo, zeolite.

Figure 4  Effect of incubation time on the recovery rates of Andisol-based and zeolite-based systems during the recovery experimental period. (a) Decolorization rates by andisol (Andi), andisol plus charcoal (Andi+Char) and Zeolite, (b) recovery rates by Andi, Andi+Char and Zeolite, (c) decolorization rates by sandy soil plus Shirasagi M (San+Shira-M), red soil plus Shirasagi M (Red+Shira-M), andisol plus Shirasagi M (Andi+Shira-M) and Andisol+MD5 and (d) recovery rates by San+Shira-M, Red+Shira-M, Andi+Shira-M and Andisol+MD5.

Figure 4  Effect of incubation time on the recovery rates of Andisol-based and zeolite-based systems during the recovery experimental period. (a) Decolorization rates by andisol (Andi), andisol plus charcoal (Andi+Char) and Zeolite, (b) recovery rates by Andi, Andi+Char and Zeolite, (c) decolorization rates by sandy soil plus Shirasagi M (San+Shira-M), red soil plus Shirasagi M (Red+Shira-M), andisol plus Shirasagi M (Andi+Shira-M) and Andisol+MD5 and (d) recovery rates by San+Shira-M, Red+Shira-M, Andi+Shira-M and Andisol+MD5.

Figure 5  Effect of colored substance concentration, hydraulic loading rate (HLR) and aeration on the decolorization rates of Andisol-based and zeolite-based systems during the continuous column experiment period. Column AC30′ was at double the HLR during Period 1 and 2. AC, activated carbon; Andi, andisol; Char, charcoal; HDTMA, hexadecyltrimethyl ammonium; Zeo, zeolite.

Figure 5  Effect of colored substance concentration, hydraulic loading rate (HLR) and aeration on the decolorization rates of Andisol-based and zeolite-based systems during the continuous column experiment period. Column AC30′ was at double the HLR during Period 1 and 2. AC, activated carbon; Andi, andisol; Char, charcoal; HDTMA, hexadecyltrimethyl ammonium; Zeo, zeolite.

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