| Literature DB >> 31909250 |
José Lugo-Arias1, Javier Burgos-Vergara2, Elkyn Lugo-Arias3, Audrey Gould3, David Ovallos-Gazabon4.
Abstract
Water purification is indispensable to guarantee safe human consumption and to prevent diseases caused by the ingestion of contaminated water. This requires a series of water treatment processes which require investment. However, the economic limitations of rural communities hinder their ability to implement such water-treatment systems, as is the case in Ciénaga Grande of Santa Marta ("Large Swamp", in English) in Colombia. Low-cost systems can be used instead as simple and safe alternatives. Therefore, the objective of this work was to evaluate non-conventional, low-cost water processes to purify the water from the collection point of two stilt house villages in Ciénaga Grande of Santa Marta. These include: 1) Using two natural coagulants, Moringa Oleifera and Cassia Fistula; 2) filtration through a biosand filter and a carbon activated filter; and 3) disinfection through UV-C Radiation and through solar disinfection. The results showed a turbidity values reduction between 52% and 96% using the two natural coagulants; both turbidity and total coliforms achieved reductions of 98.4% and 76.9%, respectively in the filtration process; and removal of total coliforms up to 98.8% in the disinfection process. Despite the high rates of reduction in the different parameters, the water does not comply with the recommended limits for safe drinking water.Entities:
Keywords: Ciénaga Grande of Santa Marta; Environmental chemical engineering; Environmental health; Green engineering; Low-cost water purification; Non-conventional treatment; Public health; Stilt house villages; Water treatment
Year: 2019 PMID: 31909250 PMCID: PMC6938825 DOI: 10.1016/j.heliyon.2019.e03062
Source DB: PubMed Journal: Heliyon ISSN: 2405-8440
Figure 1Area of study: location of stilt-house towns and the access routes to safe drinking water in the Ciénaga Grande of Santa Marta. Source: Google Earth Modified.
Figure 2(a) Stilt-house. (b) Transport canoes. Source: Authors.
Figure 3Coagulation test. (a) Water samples before applying the coagulants. (b) Samples after applying the coagulant and sedimentation time; Moringa is in Row A and Cañadonga in Row B.
Figure 4Biosand filter.
Figure 5Carbon activated filter.
Figure 6UV radiation device.
Evaluated parameters of the water quality in the water source and distribution site in the stilt-house towns.
| Parameters | 23/03/2017 | 26/04/2017 | 4/05/2017 | 16/05/2017 | Colombian Law (drinking water) 2115/2007 | ||
|---|---|---|---|---|---|---|---|
| Aguas Negras spout | Storage Tank | Aguas Negras spout | Storage Tank | Aguas Negras spout | Aguas Negras spout | ||
| pH | 7.22 | 7.16 | 7.18 | 7.23 | 7.12 | 7.43 | 6.5–9 |
| Temperature (°C) | 25.1 | 26.7 | 27.5 | 27.8 | 29.8 | 28.1 | N/A |
| Conductivity (μS/cm) | 174 | 188.1 | 234 | 208 | 345 | 205 | 1000 |
| Turbidity (NTU) | 633* | 17.4* | 650* | 19.1* | 645* | 662* | 2 |
| Alkalinity (mg/L CaCO3) | 71.6 | 52.8 | 85.8 | 61.8 | 65.4 | 52.8 | 200 |
| Total hardness (mg/L CaCO3) | 346.6* | 332.8* | 276.2 | 248.6 | 357.8* | 330.8* | 300 |
| Chlorides (mg/L Cl-) | 42.54 | 60.97 | 49.63 | 56.72 | 61.68 | 42.54 | 250 |
| Sulfates (mg/L) | 27 | 29 | 33 | 36 | 58 | 57 | 250 |
| Nitrates (mg/L) | 0.7 | 0.6 | 1.6 | 1.4 | 2.1 | 1.3 | 10 |
| Total coliforms (CFU/100 ml | 6700* | 203* | 8530* | 122* | 12100* | 13700* | 0 |
[*]: Non-compliance with the water quality parameter according to Colombian Resolution 2115/2007.
Figure 7Turbidity variation at the time of sedimentation of the employed coagulants. (a) Turbidity in the first lab test. (b) Turbidity in the second test.
Measured data of the water quality parameters after the filtration versus the initial simple.
| Coagulant Filter type | Initial sample | Optimal Moringa | Optimal Cañandonga | Without coagulants | Colombian law: Resolution 2115/2007 | ||||
|---|---|---|---|---|---|---|---|---|---|
| Biosand filter | Activiated carbon filter | Biosand filter | Activated carbon filter | Biosand filter | Activated carbon filter | ||||
| First sampling (4/05/2017) | pH | 7.12 | 7.04 | 6.85 | 6.65 | 7.02 | 6.93 | 7.1 | 6.5–9 |
| Temperature (°C) | 29.8 | 29.5 | 29.4 | 29.7 | 29.6 | 29.6 | 29.5 | N/A | |
| Conductivity (μS/cm) | 345 | 341 | 339 | 290 | 312 | 291 | 314 | 1000 | |
| Turbidity (NTU) | 645 | 7.7 | 6.9 | 9.1 | 8.8 | 11.2 | 10.2 | 2 | |
| Alkalinity (mg/L CaCO3) | 65.4 | 57.62 | 54.41 | 52.98 | 61.47 | 63.92 | 59.64 | 200 | |
| Total hardness (mg/L CaCO3) | 357.8 | 315 | 307.6 | 324.4 | 318 | 322.4 | 324.6 | 300 | |
| Chlorides (mg/L Cl-) | 61.68 | 42.54 | 49.63 | 35.45 | 42.54 | 28.38 | 35.45 | 250 | |
| Sulfates (mg/L) | 58 | 35 | 26 | 57 | 52 | 46 | 41 | 250 | |
| Nitrates (mg/L) | 2.1 | 1.9 | 1.5 | 2.1 | 1.8 | 2.1 | 1.9 | 10 | |
| Total coliforms (CFU/100 ml) | 12100 | 3100 | 2800 | 3500 | 3800 | 5200 | 4300 | 0 | |
| Second sampling (16/05/2017) | pH | 7.43 | 7.39 | 7.49 | 7.3 | 7.31 | 7.41 | 7.4 | 6.5–9 |
| Temperature (°C) | 28.1 | 28 | 27.9 | 27.8 | 27.7 | 27.6 | 27.4 | N/A | |
| Conductivity (μS/cm) | 205 | 199.94 | 203 | 201 | 200.1 | 203.1 | 204 | 1000 | |
| Turbidity (NTU) | 662 | 8.1 | 7.5 | 10.2 | 7.9 | 11.7 | 10.6 | 2 | |
| Alkalinity (mg/L CaCO3) | 52.8 | 46.8 | 48.3 | 50.8 | 52.8 | 52.8 | 52.7 | 200 | |
| Total hardness (mg/L CaCO3) | 330.8 | 293.8 | 289.3 | 302.1 | 286.2 | 295.4 | 303.4 | 300 | |
| Chlorides (mg/L Cl-) | 42.54 | 35.27 | 31.9 | 32.36 | 29.45 | 42.54 | 39.43 | 250 | |
| Sulfates (mg/L) | 57 | 57 | 48 | 56 | 41 | 57 | 53 | 250 | |
| Nitrates (mg/L) | 1.3 | 1.1 | 0.9 | 1.2 | 1.1 | 1.3 | 1.2 | 10 | |
| Total coliforms (CFU/100 ml) | 13700 | 3800 | 3400 | 4200 | 4600 | 6300 | 5200 | 0 | |
Figure 8Turbidity variation after filtration.
Figure 9Turbidity removal after filtration – [FB]: Biosand filter, [FCA] – Activated carbon filter.
Figure 10Total hardness variation after filtration.
Figure 11Total hardness removal after filtration.
Figure 12Total coliforms variation after filtration.
Figure 13Total coliforms removal after filtration.
The comparison between filters and combinations of filters with coagulants of the average of median of the evaluated parameters were considered most important.
| Comparison | Parameters | Test | P-value |
|---|---|---|---|
| Filters (Activated carbon and biosand) | Turbidity | ANOVA | 0.288 |
| Total hardness | ANOVA | 0.641 | |
| Total coliforms | ANOVA | 0.18 | |
| Natural coagulant - filter combination | Turbidity | Kruskal-Wallis | 0.103 |
| Total hardness | Kruskal-Wallis | 0.761 | |
| Total coliforms | Kruskal-Wallis | 0.227 |
Total coliforms after filtration versus the filtered water sample.
| Sampling | First sampling (4/05/2017) | Second sampling (16/05/2017) | ||||||
|---|---|---|---|---|---|---|---|---|
| Coagulant | Type of filter | Disinfection technique | Total coliforms (CFU/100 ml) | Total coliforms (CFU/100 ml) | ||||
| Influent | Effluent | Removal (%) | Influent | Effluent | Removal (%) | |||
| Optimal Moringa | Biosand filter | SODIS | 3100 | 57 | 98.16 | 3800 | 73 | 98.08 |
| UV radiation | 3100 | 43 | 98.61 | 3800 | 56 | 98.53 | ||
| Activated carbon filter | SODIS | 2800 | 51 | 98.18 | 3400 | 58 | 98.29 | |
| UV radiation | 2800 | 33 | 98.82 | 3400 | 41 | 98.79 | ||
| Optimal Cañandonga | Biosand filter | SODIS | 3500 | 71 | 97.97 | 4200 | 92 | 97.81 |
| UV radiation | 3500 | 45 | 98.71 | 4200 | 79 | 98.12 | ||
| Activated carbon filter | SODIS | 3800 | 55 | 98.55 | 4600 | 82 | 98.22 | |
| UV radiation | 3800 | 51 | 98.66 | 4600 | 71 | 98.46 | ||
| Without coagulants | Biosand filter | SODIS | 5200 | 87 | 98.33 | 6300 | 95 | 98.49 |
| UV radiation | 5200 | 73 | 98.6 | 6300 | 84 | 98.67 | ||
| Activated carbon filter | SODIS | 4300 | 78 | 98.19 | 5200 | 86 | 98.35 | |
| UV radiation | 4300 | 65 | 98.49 | 5200 | 93 | 98.21 | ||
Total coliforms comparison (after the disinfection) between SODIS and the UV-C radiation.
| Comparison | Parameters | Test | P-value |
|---|---|---|---|
| Disinfection (SODIS and UV-radiation) | Total coliforms | ANOVA | 0.09 |