Land treatment Methods A review on available methods and its ability to remove pollutants
Mohammad Mousavinezhad1*, Mojtaba Rezazadeh1, Farshad Golbabayee1, Ehsan Sadati2
1Department of Environment, University of Tehran, Tehran, Iran, 14155-6135 2Aras International Campus, Tehran University, Tehran, Iran, 14155-6135 Email: mousavy_mh@yahoo.com
DOI : http://dx.doi.org/10.13005/ojc/310241
Article Received on :
Article Accepted on :
Article Published : 08 Jun 2015
One of the most cost effective way of wastewater treatment is land treatment. This process is defined as the application of wastewater to the land at a controlled rate in adesigned and engineered setting. The purpose of the activity isto obtain beneficial use of these materials, to improve environmental quality, and to achieve treatment and disposal goals in a cost-effective manner. Land treatment systems include slow rate (SR), overland flow (OF), and soil aquifer treatment (SAT) or rapid infiltration (RI). These systems require minimal effort for operation and maintenance. This paper first describe each of these methods by: hydraulic pathways, the way of treatment, and there pros and cons. In the next part some standards and ability of each method in removal of pollutions and chemical compounds described. In this part also some successful application of land treatment reviewed and the ability of these method for crop irrigation and its limitations reviewed.
KEYWORDS:Land Treatment; slow rate; overland flow; rapid infiltration
Download this article as:Copy the following to cite this article: Mousavinezhad M, Rezazadeh M, Golbabayee F, Sadati E. Land treatment Methods A review on available methods and its ability to remove pollutants. Orient J Chem 2015;31(2). |
Copy the following to cite this URL: Mousavinezhad M, Rezazadeh M, Golbabayee F, Sadati E. Land treatment Methods A review on available methods and its ability to remove pollutants. Available from: http://www.orientjchem.org/?p=9119 |
Introduction
The process of land treatment is the controlled application of wastewater to soil to achieve treatment of constituents in the wastewater. All three major processes (include slow rate (SR), overland flow (OF), and rapid infiltration (RI)) use the natural physical, chemical, and biological mechanisms within the soil–plant–water matrix. The SR processes use the soil matrix for treatment after infiltration of the wastewater, the major difference between the processes being the rate at which the wastewater is loaded onto the site. The OF process uses the soil surface and vegetation for treatment, with limited percolation, and the treated effluent is collected as surface runoff at the bottom of the slope1.
These systems can often be the most cost-effective option in terms of both construction and operation and are therefore, frequently being used in small communities and rural areas2.
The use of domestic wastewater emanating from these communities on fast growing plant species can be an effective way of wastewater treatment as well as a source of water and nutrients for growing plants. The application of domestic wastewater for irrigation to food crops generally fulfills their nutrient requirement but in other hand make them more vulnerable to the attack of insects and pathogens. Hence, the irrigation of trees with this
wastewater is considered as more economical and eco-friendly method of fertilization. The species like Poplar and Salix have longer growing seasons and deeper, longer lasting root systems than annual crops, which enables them to have a better utilization of the nutrients from wastewater. Secondly, these plant species possess high rate of evapotranspiration which further enhances the LTS treatment efficiency3.
The technical design of the land treatment system mainly depends on the mode of wastewater application, and characteristics of wastewater and on-site soil profile. The parameters that should be given utmost consideration during land application are dissolved salts, suspended solids, nutrients like nitrogen and phosphorus, organic matter, cations like sodium and magnesium, and toxic substances. The important site conditions include the depth of the soil mantle, depth of ground water table, slope and permeability. The land based treatment of wastewater based on how it is applied over land can be classified as:
1. Slow rate (SR) method
2. Rapid infiltration (RI)
3. Overland Flow (OF)
Types of natural treatment systems
There are three basic types of natural treatment systems. Here we describe each type
Slow Rate Process
Slow rate (SR) land treatment is the controlled application of wastewater to vegetated land surface at a rate typically measured in terms of a few centimeters of liquid per week (see Figure 1).The design flow path depends on infiltration, percolation, and usually lateral flow within the boundaries of the treatment site.
Treatment occurs at the soil surface and as the wastewater percolates through the plant root-soil matrix. Depending on the specific system design, some to most of the water may be used by the vegetation, some may reach the groundwater, and some may be recovered for other beneficial uses. Off-site runoff of any of the applied wastewater is specifically avoided by the system design4.
The hydraulic pathways of the applied water can include:
- Vegetation irrigation with incremental percolation for salt leaching
- Some vegetative uptake with percolation the major pathway
- Percolation to under drains or wells for water recovery and reuse
- Percolation to groundwater and/or lateral subsurface flow to adjacent surface waters
Wastewater applications can be via ridge and furrow or border strip flood irrigation or with sprinklers using fixed nozzles or moving sprinkler systems. The selection of the application method is dependent on site conditions. The surface vegetation is an essential component in all SR systems.
Slow rate land treatment can be operated to achieve a number of objectives including:
- Treatment of the applied wastewater
- Economic return from the use of water and nutrients to produce marketable crops
- Exchange of wastewater for potable water for irrigation purposes in arid climates to achieve overall water conservation
- Development and preservation of open space and greenbelts
These goals are not mutually exclusive, but it is unlikely that all can be brought to an optimum level within the same system. In general, maximum cost-effectiveness for both municipal and industrial systems will be achieved by applying the maximum possible amount of wastewater to the smallest possible land area. That will in turn limit the choice of suitable vegetation and possibly the market value of the harvested crop. In the more humid optimization of treatment is usually the major objective for land treatment systems5.
Optimization of a system for wastewater treatment usually results in the selection of perennial grasses because a longer application season, higher hydraulic loadings, and greater nitrogen removals are possible compared to other agricultural crops.
Rapid Infiltration Process
Rapid infiltration (RI) land treatment is the controlled application of wastewater to earthen basins in permeable soils at a rate typically measured in terms of meter of liquid per week. The hydraulic loading rates for RI are usually at least an order of magnitude higher than for SR systems. Any surface vegetation that is present has a marginal role for treatment owing to the high hydraulic loadings. However, vegetation is sometimes critical for stabilization of surface soils and the maintenance of acceptable infiltration rates. In these cases, water-tolerant grasses are typically used6. Treatment in the RI process is accomplished by biological, chemical, and physical interactions in the soil matrix, with the near surface layers being the most active zone.The design flow path involves surface infiltration, subsurface percolation, and lateral flow away from the application site (see Figure 2). A cyclic application is the typical operational mode with a flooding period followed by days or weeks of drying. This allows aerobic restoration of the infiltration surface and drainage of the applied percolate7.
Figure1: Hydraulic pathways for slow rate (SR) land treatment8 |
The geo-hydrological aspects of the RI site are more critical than for the other processes, and a proper definition of subsurface conditions and the local groundwater system is essential for design.
The purpose of a rapid infiltration system is wastewater treatment, so the system design and operating criteria are developed to achieve that goal. However, there are several alternatives with respect to the utilization or final disposal of the treated water:
- Groundwater recharge
- Recovery of treated water for subsequent reuse or discharge
- Recharge of adjacent surface streams
- Seasonal storage of treated water beneath the site with seasonal recovery for agriculture
The recovery and reuse of the treated RI effluent is particularly attractive in arid regions, and studies in Arizona and California9have demonstrated that the recovery of the treated water is suitable for unrestricted irrigation on any type of crop. Groundwater recharge may also be attractive, but special attention is required for nitrogen if drinking water aquifers are involved. Unless special measures are employed, it is unlikely that drinking water levels for nitrate nitrogen (10 mg/L as N) can be routinely attained immediately beneath the application zone with typical municipal waste-waters10. If special measures are not employed, there must then be sufficient mixing and dispersion with the native groundwater prior to the down gradient extraction points. In the more humid regions neither recovery nor reuse is typically considered11.
Figure2: Hydraulic pathway for rapid infiltration (RI)8 |
In these cases groundwater impacts can often be avoided by locating the RI site adjacent to a surface water body. The quality of the sub flow entering the surface water will generally exceed that which could be produced by an advanced wastewater treatment plant.
Overland Flow Process
Overland flow (OF) is the controlled application of wastewater to relatively impermeable soils on gentle grass covered slopes. The hydraulic loading is typically several inches of liquid per week and is usually higher than for most SR systems.
Since costs tend to be directly related to hydraulic loading, OF systems are usually more cost-effective than SR systems for equivalent water quality requirements.
Vegetation, consisting of perennial grasses, is an essential component in the OF system, for its contribution both to slope stability and erosion protection and to its function as a treatment component12.
The design flow path is essentially sheet flow down the carefully prepared vegetated surface with runoff collected in ditches or drains at the toe of each slope (see Figure 3). Treatment occurs as the applied wastewater interacts with the soil, the vegetation, and the biological surface growths. Many of the treatment responses are similar to those occurring in trickling filters and other attached growth processes. Wastewater is typically applied from gated pipe or nozzles at the top of the slope or from sprinklers located on the slope surface. Industrial wastewaters and those with higher solids content typically use the latter approach13.
Figure3: Hydraulic pathways for overland flow (OF)8 |
A small portion of the applied water maybe lost to deep percolation and a larger fraction to evapotranspiration, but the major portion is collected in the toe ditches and discharged, typically to an adjacent surface water. The SR and RI concepts may include percolate recovery and discharge but the OF process almost always includes a surface discharge, and the necessary permits are required. The purpose of overland flow is cost-effective wastewater treatment. The harvestand sale of the cover crop may provide some secondary benefit and help offset operational costs, but the primary objective is treatment of the wastewater. One of the largest municipal overland flow systems in the United States was in Davis, California designed for 22 thousand m3/day flow14.
System Interactions
Biochemical Oxygen Demand
All land treatment concepts are very efficient at removal of biodegradable organics, typically characterized as biochemical oxygen demand (BOD5). Removal mechanisms include filtration, adsorption, and biological reduction and oxidation. Most of the responses in slow rate (SR) and rapid infiltration (RI) occur at the ground surface or in the near surface soils where microbial activity is most intense. Essentially all of the responses in overland flow (OF) occur at the soil surface or in the mat of plant litter and microbial material15.
Settling of most particulate matter occurs rapidly in OF systems as the applied wastewater flows in a thin film down the slope. Algae removal is an exception, since the detention time on the slope is not usually sufficient to permit complete removal by physical settling16. The biological growths and slimes which develop on the OF slope are primarily responsible for ultimate pollutant removal.
Since the basic treatment mechanism is biological, all three systems have a continually renewable capacity for BOD5 removal as long as the loading rate and cycle allows for preservation and/or restoration of aerobic conditions in the system. Pilot studies17in1998 with soil columns indicate that BOD5 removal to low “background” levels was independent of the level of pretreatment , independent of soil type, and essentially independent ofinfiltration rate. These responses confirm the results presented in (Table 1) and also confirm the fact that high levels of pre-application treatment are not necessary for effective BOD5 removal in land treatment systems.
Organic loading
A comparison of the values in (Table 2) indicates that land treatment systems have a very high capacity for treatment of the degradable organics characterized as BOD5. The RI systems produce an effluent close to that of the SR systems with an organic loading which is typically an order of magnitude higher.
A study at five SR systems applying potato processing wastewater in Idaho utilized chemical oxygen demand (COD) loadings ranging from 45 to 310 Kg/(ha . day) with removals up to 98 percent after 1.5 m of percolation in the soil. 18 Pilot-scale OF with high-strength snack food processing wastewaters was successful at BOD5 loading rates ranging from 55 to 110Kg/ (ha. day).19 Pilot RI studies in Montana with partially treated kraft process paper mill wastes with BOD5 concentrations up to 600 mg/L at hydraulic loadings of about 6cm/day were also successful.20
Some of the industrial systems discussed above successfully operate with applied BOD5 concentrations of 1000 mg/L or more.
It can therefore be concluded that neither BOD5 nor COD is likely to be the limiting factor for design of municipal land treatment systems. Typical organic loadings in current use are summarized in (Table 2).
Table1: BOD5 Removal at Typical Land Treatment Systems21
Process/location | Hydraulic loading, m/year | BOD5, mg/L Applied | BOD5,mg/LEffluent | Sample depth, m |
Hanover, N.H. San Angelo, Tex. | 1–7.53 | 40–9289 | 0.9–1.70.7 | 1.5 |
Rapid Infiltration | ||||
Lake George, N.Y. | 40 | 38 | 1.2 | 3 |
Phoenix, Ariz. | 110 | 15 | 1.0 | 9 |
Hollister, California. | 15 | 220 | 8.0 | 7.5 |
Overland Flow | ||||
Hanover, N.H. | 7 | 72 | 9 | |
Easley, S.C. | 8 | 200 | 23 | |
Davis, California. | 12.5 | 112 | 10 |
Table 2: Typical Organic Loading Rates for Land Treatment Systems21b, 22
Process | Organic loading, Kg BOD5/ (ha. Day) |
Slow rate (SR) | 50-500 |
Rapid infiltration (RI) | 145-1000 |
Overland flow (OF) | 40-110 |
Pathogenic Organisms
The pathogens of concern in land treatment systems are parasites, bacteria, and virus. The pathways, or vectors, of concern are to groundwater, contamination of crops, translocation or ingestion by grazing animals, and off-site transmission via aerosols or runoff. The removal of pathogens in land treatment systems is accomplished by adsorption, desiccation, radiation, filtration, predation, and exposure to other adverse conditions .The SR process is the most effective, removing about five logs (105) of fecal coliforms within a depth of a meter. The RI process typically can remove two to three logs of fecal coliforms within few meter of travel, and the OF process can remove about 90 percent of the applied fecal coliforms.
Metals
The slow rate (SR) land treatment process is the most effective for metals removal because of the finer-textured soils and the greater opportunity for contact and adsorption. Rapid infiltration (RI) can also be quite effective, but a longer travel distance in the soil will be necessary owing to the higher hydraulic loadings and coarser- textured soils. Overland flow (OF) systems allow minimal contact with the soil and typically remove between 60 and 90 percent depending on the hydraulic loading and the particular metal23.
Adsorption of most trace elements occurs on the surfaces of clay minerals, metal oxides, and organic matter; as a result, fine-textured and organic soils have a greater adsorption capacity for trace elements than sandy soils have.
The major concern with respect to metals is the potential for accumulation in the soil profile and then subsequent translocation, via crops or animals, through the food chain to man .The metals of greatest concern are cadmium (Cd), lead (Pb), zinc (Zn), copper (Cu), and nickel (Ni). The World Health Organization (WHO) has published guidelines for annual and cumulative metal additions to agricultural crop land (Error! Reference source not found.) and (Table 3)
Table 3: Metals Concentrations in Wastewaters and Suggested Concentrations in Drinking and Irrigation Waters24
Irrigation water, mg/L | ||||
Element | Raw sewagemg/L
|
Drinking watermg/L
|
20 years* | Continuous† |
Cadmium | 0.004–0.14 | 0.01 | 0.05 | 0.005 |
Chromium | 0.02–0.70 | 0.05 | 20 | 5.0 |
Lead | 0.05–1.27 | 0.05 | 20 | 5.0 |
Zinc | 0.05–1.27 | 0.05 | 20 | 5.0 |
*For fine-textured soils only. Normalirrigationpracticefor20years.
†For any soil, normal irrigation practice, no time limit
Table4: WHO Recommended Annual and Cumulative Limits for Metals Applied to Agricultural Cropland2526
Metal rate,† | Annual loading rate,*kg/ha | Cumulative loadingkg/ha |
Arsenic | 1.995 | 41 |
Cadmium | 1.905 | 39 |
Chromium | 149.066 | 3000.382 |
Copper | 75.094 | 1499.63 |
Lead | 14.57 | 300.374 |
Mercury | 0.852 | 17.036 |
Molybdenum | 0.897 | 18.045 |
Nickel | 20.959 | 420.3 |
Selenium | 5.044 | 99.751 |
Zinc | 140.1 | 2799.758 |
Nitrogen
The removal of nitrogen in land treatment systems is complex and dynamic owing to the many forms of nitrogen (N2, organic N, NH3, NH4, NO2, and NO3) and the relative ease of changing from one oxidation state to the next.
It is important in the design of all three land treatment concepts to identify the total concentration of nitrogen in the wastewater to be treated as well as the specific forms (i.e., organic, ammonia, nitrate, etc.) expected. Experience with all three land treatment processes demonstrates that the less oxidized the nitrogen is when entering the land treatment system the more effective will be the retention and overall nitrogen removal.
The ammonia fraction can be lost by volatilization, taken up by the crop, or adsorbed by the clay minerals in the soil.27
Under favorable conditions (i.e., sufficient alkalinity, suitable temperatures, etc.)Nitrification ranging from 5 to 50 mg/ (L. day) is possible.
Assuming that these reactions are occurring with the adsorbed ammonia ions in the top 10cm of a fine-textured soil means that up to 67 Kg. of ammonia nitrogen per hectare can be converted to nitrate each day.
Nitrification is a conversion process, not a removal process for nitrogen. Denitrification, volatilization, and crop uptake are the only true removal pathways available. Crop uptake is the major pathway considered in the design of most slow rate systems, but the contribution from denitrification and volatilization can be significant depending on site conditions and wastewater type.
In RI, ammonia adsorption on the soil particles followed by nitrification typically occurs, but denitrification is the only important actual removal mechanism. For OF, crop uptake, volatilization, and denitrification can all contribute to nitrogen removal.
Mineralization rates developed for wastewater bio-solids are given in (Table 5). The values are the percent of the organic nitrogen present that is mineralized (i.e., converted to inorganic forms such as ammonia and nitrate) in a given year.
Phosphorus
Phosphorus is present in municipal wastewater as orthophosphate, polyphosphate, and organic phosphates. The orthophosphates are immediately available for biological reactions in soil ecosystems. The necessary hydrolysis of the polyphosphates proceeds very slowly in typical soils, so these forms are not as readily available28.
Phosphorus removal in land treatment systems can occur through plant uptake, biological, chemical, and/or physical processes. Phosphorus removal in the soil depends to a significant degree on chemical reactions which are not necessarily renewable. As a result, the retention capacity for phosphorus will be gradually reduced over time, but not exhausted29.
There is no crop uptake in RI systems, and the soil characteristics and high hydraulic loading rates typically used require greater travel distances in the soil for effective phosphorus removal.
The opportunities for contact between the applied wastewater and the soil are limited to surface reactions in OF systems, and as a result phosphorus removals typically range from 40 to 60percent. Phosphorus removal in overland flow can be improved by chemical addition and then precipitation on the treatment slope30.
Table5: Mineralization Rates for Organic Matter in Biosolids
Mineralization rate, % | ||||
Time after biosolids application, years | Unstabilized primary | Aerobically digested | Anaerobically digested | Composted |
0–1 | 40 | 30 | 30 | 10 |
1–2 | 20 | 15 | 10 | 5 |
2–3 | 10 | 8 | 5 | |
3–4 | 5 | 4 |
Arsenic
Arsenic is nonessential for all life forms. In significant concentrations it can be moderately toxic to plants and very toxic to animals. The food chain is protected at land treatment sites, since the crops should show adverse effects from arsenic before hazardous levels were reached in the edible portions of the plants. Arsenic is removed in the soil system by adsorption by the soil colloids with clay and the iron and aluminum oxides performing essentially the same function as described previously for phosphorus removal31.
Poultry manure with 15 to 20 ppm arsenic has been applied for up to 20 years [225 to 450g. As/ (ha. year)] without any adverse effects on either alfalfa or clover. Field tests are recommended for industrial effluents with high arsenic concentrations to develop criteria for loading rates and vegetation to be used at a specific location.32
Sulfur
Sulfur is usually present in most wastewaters in either the sulfate or the sulfite form .Crop uptake can account for some sulfur removal. Error! Reference source not found. summarizes typical values for several crops .It is prudent to assume that all of the sulfur compounds applied to the land will be mineralized to sulfate. The 250 mg/L standard for drinking water sulfate would then apply at the project boundary when drinking water aquifers are involved. It should be assumed in sizing the system that the major permanent removal pathway is to the harvested crop, and the values in (Error! Reference source not found.) can be used for estimating purposes.
Table6: Sulfur Uptake by Selected Crops33
Crop | Harvested mass | Sulfur removed kg./ha |
Corn | 12.5 ton/ha | 49.32 |
Wheat | 5.2ton/ha | 24.66 |
Barley | 6.3ton/ha | 28.02 |
Alfalfa | 14.8ton/ha | 33.62 |
Clover | 9.8ton/ha | 20.17 |
Coastal Bermuda grass | 25ton/ha | 50.44 |
Orchard grass | 17.3ton/ha | 56.04 |
Cotton | 1.5ton/ha | 25.78 |
Conclusion
The selection of a natural wastewater treatment system requires the consideration of a number of factors, including wastewater volume and pollutant characteristics, site soils and geology, and climate. Land application systems also require a large land area. Not all sites will be candidates for land application, but for those sites that do qualify, natural treatment will offer the owner and operator many benefits over systems that employ mechanical and chemical treatment.
Land treatment is the most cost effective way of wastewater treatment however there are some difficulty in its application. Land treatment can’t be used for large cities due to its hydraulic load limitations. But it can be used in villages and small countries and wherever it’s difficult to use huge water treatment facilities. It’s also possible to use wastewater as a source of nutrition for crops but in this case it need restrict supervision.
To overcome this restriction it’s possible to use land treatment of wastewater for non-food crop which needs much less supervisions and restrictions.
References
- Crites, R. W.; Middlebrooks, E. J.; Bastian, R. K., Natural wastewater treatment systems. CRC Press: 2014.
- Kivaisi, A. K., The potential for constructed wetlands for wastewater treatment and reuse in developing countries: a review. Ecological Engineering 2001,16 (4), 545-560.
- (a) Liu, J.; Qiu, C.; Xiao, B.; Cheng, Z., The role of plants in channel-dyke and field irrigation systems for domestic wastewater treatment in an integrated eco-engineering system. Ecological Engineering 2000,16 (2), 235-241;(b) Muga, H. E.; Mihelcic, J. R., Sustainability of wastewater treatment technologies. Journal of environmental management 2008,88 (3), 437-447.
- Tzanakakis, V.; Paranychianakis, N.; Angelakis, A., Performance of slow rate systems for treatment of domestic wastewater. Water Science & Technology 2007,55 (1), 139-147.
- Paranychianakis, N. V.; Angelakis, A. N.; Leverenz, H.; Tchobanoglous, G., Treatment of wastewater with slow rate systems: a review of treatment processes and plant functions. Critical reviews in environmental science and technology 2006,36 (3), 187-259.
- Nema, P.; Ojha, C.; Kumar, A.; Khanna, P., Techno-economic evaluation of soil-aquifer treatment using primary effluent at Ahmedabad, India. Water Research 2001,35 (9), 2179-2190.
- Guo, W.; Li, P.; Zhao, T.; Li, J., Effect of LAS on removing TN in artificial rapid infiltration land treatment system [J]. Journal of Liaoning Technical University (Natural Science) 2008,5, 044.
- EPA, Process Design Manual-Land Treatment of Municipal Wastewater Effluents. Cincinnati, Ohio, 2006; p 193.
- Idelovitch, E. In Unrestricted Irrigation with Municipal Wastewater, Environmental Engineering (1981), ASCE: 1981; pp 243-256.
- Ma, L.; Sun, X.; Liang, X.; Cui, C., Biological nitrogen removal by nitrification-denitrification in constructed rapid infiltration land system to treat municipal wastewater. Journal of Food, Agriculture & Environment 2009,7 (3&4), 795-798.
- Guo, J.-s.; Wang, C.; Fang, F.; Yin, L.; Yao, R., Influence of wet/dry ratio on pollutants removal performance by rapid infiltration system. China Water & Wastewater 2006,22 (17), 9.
- Thullen, J. S.; Sartoris, J. J.; Nelson, S. M., Managing vegetation in surface-flow wastewater-treatment wetlands for optimal treatment performance. Ecological Engineering 2005,25 (5), 583-593.
- McDowell, R.; Muirhead, R.; Monaghan, R., Nutrient, sediment, and bacterial losses in overland flow from pasture and cropping soils following cattle dung deposition. Communications in soil science and plant analysis 2006,37 (1-2), 93-108.
- Smith, R.; Schroeder, E., Demonstration of the Overland Flow Process for the Treatment of Municipal Wastewater—Phase II Field Studies. Report to California State Water Resources Control Board, Dept. of Civil Engineering, University of California, Davis 1982.
- Karathanasis, A.; Potter, C.; Coyne, M. S., Vegetation effects on fecal bacteria, BOD, and suspended solid removal in constructed wetlands treating domestic wastewater. Ecological engineering 2003,20 (2), 157-169.
- Qi-Xing, Z.; Zhang, Q.-R.; Tie-Heng, S., Technical innovation of land treatment systems for municipal wastewater in northeast China. Pedosphere 2006,16 (3), 297-303.
- Kinney, C. A.; Furlong, E. T.; Zaugg, S. D.; Burkhardt, M. R.; Werner, S. L.; Cahill, J. D.; Jorgensen, G. R., Survey of organic wastewater contaminants in biosolids destined for land application. Environmental science & technology 2006,40 (23), 7207-7215.
- Smith, J., Treatment of potato processing waste water on agricultural land. Journal of Environmental Quality 1976,5 (1), 113-116.
- Perry, L. E.; Reap, E. J.; Gilliland, M. In Pilot scale overland flow treatment of high strength snack food processing wastewaters, Environmental Engineering (1981), ASCE: 1981; pp 460-467.
- Wallace, A.; Grimestad, G.; Luoma, D.; Olson, M. In Rapid-infiltration disposal of kraft mill effluent, Proceedings Industrial Wastes Conference, Purdue University, 1977.
- (a) Leach, L. E.; Enfield, C. G.; Harlin, C., Summary of long-term rapid infiltration system studies. 1980;(b) Maine, M.; Sune, N.; Hadad, H.; Sánchez, G.; Bonetto, C., Removal efficiency of a constructed wetland for wastewater treatment according to vegetation dominance. Chemosphere 2007,68 (6), 1105-1113.
- Asano, T., Wastewater Reclamation and Reuse. Vol. 10. Water Quality Management Library. Technomic Publishing Inc. Lancaster, PA EE. UU: 1998.
- Jinbing, Z., Constructed Rapid Infiltration System For Treating Domestic Wastewater In Dongguan Huaxing Electrical Equipment Factory [j]. Environmental Engineering 2003,6, 008.
- Peijun, J. H. S. T. L.; Shijun, T. P. Z. Q. C.; Xuejun, M., New advances in the land treatment technology for wastewater [J]. Technigues and Equipment For Enviro. poll. cont 2001,1, 012.
- Mapanda, F.; Mangwayana, E.; Nyamangara, J.; Giller, K., The effect of long-term irrigation using wastewater on heavy metal contents of soils under vegetables in Harare, Zimbabwe. Agriculture, Ecosystems & Environment 2005,107 (2), 151-165.
- Chang, A. C.; Page, A. L.; Asano, T., Developing human health-related chemical guidelines for reclaimed wastewater and sewage sludge applications in agriculture. World Health Organization Geneva, Switzerland: 1995.
- Houlbrooke, D.; Horne, D.; Hedley, M.; Hanly, J.; Snow, V., A review of literature on the land treatment of farm‐dairy effluent in New Zealand and its impact on water quality. New Zealand Journal of Agricultural Research 2004,47 (4), 499-511.
- Liu, P.; Hu, C.-m., Influence of Red Mud on Phosphorous Removal by Vegetation Assimilation in Land Treatment System. Urban Environment & Urban Ecology 2011,1, 012.
- Hu, C.; Zhang, T. C.; Huang, Y. H.; Dahab, M. F.; Surampalli, R., Effects of long-term wastewater application on chemical properties and phosphorus adsorption capacity in soils of a wastewater land treatment system. Environmental science & technology 2005,39 (18), 7240-7245.
- Hu, C.; Zhang, T.; Kendrick, D.; Huang, Y.; Dahab, M.; Surampalli, R., Muskegon wastewater land treatment system: Fate and transport of phosphorus in soils and life expectancy of the system. Engineering in Life Sciences 2006,6 (1), 17-25.
- Mohan, D.; Pittman, C. U., Arsenic removal from water/wastewater using adsorbents—a critical review. Journal of hazardous materials 2007,142 (1), 1-53.
- Rahman, K.; Wiessner, A.; Kuschk, P.; Mattusch, J.; Kästner, M.; Müller, R., Dynamics of Arsenic Species in Laboratory‐Scale Horizontal Subsurface‐Flow Constructed Wetlands Treating an Artificial Wastewater. Engineering in Life Sciences 2008,8 (6), 603-611.
- (a) Overcash, M. R.; Pal, D., Design of land treatment systems for industrial wastes; theory and practice. Ann Arbor Science: 1981;(b) Tzanakakis, V.; Paranychianakis, N.; Angelakis, A., Nutrient removal and biomass production in land treatment systems receiving domestic effluent. Ecological Engineering 2009,35 (10), 1485-1492.
This work is licensed under a Creative Commons Attribution 4.0 International License.