pH, conductivity and TDS
In this section, the results of the experiments which were conducted in various rates and heights or the three considered pilots are presented and discussed in Tables 5, 6 and 7. In each 30 cm from the top to down of each pilots an output sample was tested which we name them O1, O2 and O3. It should be mentioned that the input of the pilots was the output of pre-treatment section.
Table 5
The results of the experiment at the rate of 0.2 ml/min
Table 6
The results of the experiment at the rate of 0.6 ml/min
Table 7
The results of the experiment at the rate of 1 ml/min
Due to the Tables 5, 6 and 7 the rate of EC decline in various rates for all the pilots was determined. The best efficiency was obtained at the medium rate (0.2 ml/min) at pilot C for the sample O3. Moreover, the amount of TDS was decreased along the soil profile. However, the maximum reduction rate was obtained at the medium rate of 0.2 ml/min at pilot C for the sample O3. This can be defined by passing the leachate throw the various layer of the soil, biomasses are being formed which lead to the adsorption of some ions by the soil and decrease the TDS.
With regards to the achieved P-value, the amount of EC and TDS are 0.015 and 0.044, respectively. According to the assumed α = 0.05, the p-value is less than α which implies that with varying the flow rate and the pilots cause negligible changes to amounts of EC and TDS.
COD & BOD5
Tables 8, 9, 10 present the COD and BOD5 values which were determined due to various rates in the three studied pilots.
Table 8
The results of the experiment at the rate of 0.2 ml/min
Table 9
The results of the experiment at the rate of 0.6 ml/min
Table 10
The results of the experiment at the rate of 1 ml/min
The output COD and BOD5 values due to various rates in the three studied pilots are shown in Figures 2 and 3 which were compared with standards discharging to surface waters, agricultural purposes and irrigation.
With respect to the Tables 8, 9 and 10, the variation of COD and BOD5 values due to different rates for each samples are illustrated. Moreover, the special trends are shown and discussed in following. The best efficiency was reached at the medium rate (0.2 ml/min) at the pilot C for the sample O3. Moreover, the output results at the speed of 0.2 ml/min at the pilot C for the sample O3 meets the both standards discharging to surface waters and agricultural purposes and irrigation.
Along the soil profile the amounts of COD and BOD5 were declined. Some parts of particulate COD were decreased by the mechanism of sedimentation and colloidal material adsorbed and then deposited. Some parts of organic materials were reduced by anaerobic decomposition mechanism. BOD5/COD ratio was decreased, because microorganisms that were present in the biofilm layer consumed organic matter, also biodegradable organic matter was decomposed thus this ratio is reduced.
In addition, the most elimination rate is founded in the pilot A at the first 30 cm (O1), all the three flow rates. However, as much as the soil aggregation gets finer the retention time and the elimination efficiency increased more.
As can be seen, if the organic loading gets more intense (increase the input flow rate), the percentage of removal efficiency would decreases due to the declination of the hydraulic retention time which leads to descend the rate of reduction.
In pilot C in addition to the natural soil zone, the plant growth with the spray roots is effective in the elimination of leachate pollutants. The plant growth regards to the Rhizosphere which is the gathering place of microorganisms and the level of the biological activities are high, with the coexistence between the microorganisms and the absorption of plant roots, lead to more elimination of the leachate pollutants.
The p-values for the COD and the BOD5 are 0.28 and 0.411, respectively. However, it can be concluded that due to varying the flow rates and the pilots the amounts of COD and BOD5 are fluctuated.
TSS & TOC
Tables 11, 12, 13 show the results of TSS and TOC which were measured for the outputs of the three pilots due to the various speed ratios.
Table 11
The results of the experiment at the rate of 0.2 ml/min
Table 12
The results of the experiment at the rate of 0.6 ml/min
Table 13
The results of the experiment at the rate of 1 ml/min
The measured values of TSS for the samples due to different speed ratios are illustrated in Due to the Tables 11, 12, 13, the best efficiency was achieved at the medium rate of 0.2 ml/min in the sample of O3 at pilot C. Moreover, TOC along the profile of soil was decreased and the maximum reduction caused at the medium speed ratio of 0.2 ml/min at sample O3 at pilot C. To sum up, the best efficiency was obtained at the pilot C, sample O3 whilst the average amounts of TSS and TOC removal were %98.2 and %94.9.
The solid suspended materials are separated before the other materials caused by the flowing throw the soil. A proportion of TSS is eliminated by the screening and sedimentation mechanism and another proportion of fine, soluble and colloidal materials are adsorbed. However, due to the low flow rate the sedimentation is increased. It should be mentioned that, in the systems with rapid penetration most of the solid materials are separated in the surface of the soil. Therefore, it would be possible that the wastewater materials blocking the surface. Hence, drainage systems are suggested.
As can be seen in the above tables, growth in the load of organic materials leads to decrease the elimination efficiency which is caused by increasing the retention time.
As can be seen, in Table 14 a brief literature review of attenuation of landfill leachate with compared to the results of this study is given.
Table 14
Literature data of land treatment techniques for reduction of organic material