| Literature DB >> 24027589 |
Asghar Ebrahimi1, Ensiyeh Taheri, Mohammad Hassan Ehrampoush, Sara Nasiri, Fatemeh Jalali, Rahele Soltani, Ali Fatehizadeh.
Abstract
The treatment of municipal wastewater from Yazd city (center of Iran) by constructed wetland vegetated with Cyperus alternifolius was assessed. Two identical wetlands with a total working volume of 60 L and 10 cm sandy layer at the bottom were used. First wetland (W1) was control and had no Cyperus alternifolius plant. Second wetland (W2) had 100 Cyperus alternifolius shrubs with 40 cm height. Influent wastewater was provided from Yazd's septic tanks effluents and after a 4-day retention time in wetlands, reactors effluent was sampled for parameters analysis. Results show that chemical oxygen demand (COD), NO3 (-)-N, NH4 (+)-N, and PO4 (-3)-P in W1 were reduced to 72%, 88%, 32%, and 0.8%, and in W2, these parameters were removed in values of 83%, 81%, 47%, and 10%, respectively. In both wetlands, the highest and lowest removal efficiencies were related to COD and phosphorus, respectively. Also, the removed phosphorus can be released to stream when the soil saturated or influent phosphorus decreased and when the plant died. After a 4-day-retention time, the W2 wetland showed a statistically significantly lower COD and NH4 (+)-N in comparison with W2 wetland.Entities:
Mesh:
Substances:
Year: 2013 PMID: 24027589 PMCID: PMC3762078 DOI: 10.1155/2013/815962
Source DB: PubMed Journal: J Environ Public Health ISSN: 1687-9805
Figure 1Design of constructed wetland vegetated with Cyperus alternifolius.
Figure 2Effect of initial COD concentration on effluent and removal percentage of COD in W1 and W2 (HRT: 42 d and 16.5°C).
Comparison of effluent concentration and removal efficiency of COD by each reactor.
| Reactor | Effluent | Removal | ||||
|---|---|---|---|---|---|---|
| Mean | SD |
| Mean | SD |
| |
| W1 | 124.67 | 27.23 | 0.004 | 72.15 | 6.72 | 0.007 |
| W2 | 75.5 | 18.33 | 83.15 | 4.45 | ||
Figure 3Variation of effluent NO3 −–N concentration in W1 and W2 (HRT: 42 d and 16.5°C).
Comparison of effluent concentration and removal efficiency of NO3-N by each reactor.
| Reactor | Effluent | Removal | ||||
|---|---|---|---|---|---|---|
| Mean | SD |
| Mean | SD |
| |
| W1 | 2.15 | 0.58 | 0.52 | 86.22 | 5.68 | 0.75 |
| W2 | 3.27 | 2.57 | 76.15 | 26.22 | ||
Figure 4Effluent concentration and removal efficiency of PO4 −3–P as functions of initial concentration (HRT: 42 d and 16.5°C).
Comparison of effluent concentration and removal efficiency of PO4 −3-P by each reactor.
| Reactor | Effluent | Removal | ||||
|---|---|---|---|---|---|---|
| Mean | SD |
| Mean | SD |
| |
| W1 | 5.29 | 1.38 | 0.59 | 1.17 | 9.29 | 0.11 |
| W2 | 4.81 | 1.55 | 11.41 | 10.91 | ||
Figure 5Influence of initial NH4 +–N concentration on effluent and removal efficiency of NH4 +–N in W1 and W2 (HRT: 42 d and 16.5°C).
Comparison of effluent concentration and removal efficiency of NH4 +-N by each reactor.
| Reactor | Effluent | Removal | ||||
|---|---|---|---|---|---|---|
| Mean | SD |
| Mean | SD |
| |
| W1 | 40.5 | 6.42 | 0.068 | 32.36 | 7.22 | 0.039 |
| W2 | 31.5 | 8.65 | 47.19 | 13.53 | ||