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Benzene Removal In Horizontal Subsurface Flow Constructed Wetlands Treatment

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Although much information is available about conventional water quality parameters in subsurface flow (SSF) constructed wetlands, few data are available regarding specific contaminants. In this paper we focus on the behavior of Benzene in three types of constructed wetlands (CWs) (two of them were planted with two different species of macrophytes -Phragmitesaustralis and Typhalatifolia-and the third was used as a control -unplanted), located in Southern Italy (Apulia region, Lecce). The objectives of this study are to compare hydraulic behavior of the CWs with the trend of the model by varying the hydraulic conditions, to evaluate the effect of the clogging and then to assess the efficiency of the different species of macrophytes in removing Benz ene. At the beginning of the experience and after 24 months, the results show a good correlation in the hydraulic behavior between model and physical data by modifying input parameters as a consequence of the clogging. The Benzene removal from the planted fields is higher than the unplanted one.
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International Journal of Applied Engineering Research
ISSN 0973-4562 Volume 10, Number 6 (2015) pp. 14603-14614
© Research India Publications
http://www.ripublication.com
Benzene Removal In Horizontal Subsurface Flow
Constructed Wetlands Treatment
Ezio Ranieria, Angela Gorgoglionea*, Andrea Petrellaa, Valentina Petruzzellia,
PetrosGikasb
aDICATECh, Polytechnic University of Bari, viaOrabona 4, Bari70125, Italy;
E-mails: ezio.ranieri@poliba.it; andrea.petrella@poliba.it;
valentina.petruzzelli@poliba.it
bDepartment of Environmental Engineering, Technical University of Crete, Chania
campus, Chania74100, Greece;
E-mail: petros.gikas@enveng.tuc.gr
*Corresponding author: Tel. +39 3356781687; Fax: +39 0805481395; email:
angela.gorgoglione@poliba.it
Abstract
Although much information is available about conventional water quality
parameters in subsurface flow (SSF) constructed wetlands, few data are
available regarding specific contaminants. In this paper we focus on the
behavior of Benzene in three types of constructed wetlands (CWs) (two of
them were planted with two different species of macrophytes
Phragmitesaustralis and Typhalatifolia- and the third was used as a control -
unplanted), located in Southern Italy (Apulia region, Lecce). The objectives of
this study are to compare hydraulic behavior of the CWs with the trend of the
model by varying the hydraulic conditions, to evaluate the effect of the
clogging and then to assess the efficiency of the different species of
macrophytes in removing Benzene. At the beginning of the experience and
after 24 months, the results show a good correlation in the hydraulic behavior
between model and physical data by modifying input parameters as a
consequence of the clogging. The Benzene removal from the planted fields is
higher than the unplanted one.
Keywords:Benzene, Constructed wetlands, Phragmitesaustralis, Typhalatifolia
Introduction
Benzene, toluene, xylene, phenol, halogenated aromatic compounds, chloroform and
trichloroethylene are the major products of the petroleum and fine chemical industries
and the most frequently used organic solvents (Yeom and Yoo, 1999). Exploration,
14604 Ezio Ranieri
production, refining, storage, transportation, distribution and utilization of petroleum
hydrocarbons, accidental spills, improper practices and leaching landfills resulted in
the frequent occurrence of these anthropogenic organic compounds in air, water and
soil (Tang et al., 2009). Losing these substances to the receiving environments may
lead to an adverse impact and might endanger public health and welfare. Therefore,
considerable research has been conducted to remove these compounds from
contaminated environments (Nickelsen and Cooper, 1992; Lu et al., 2002).
In recent years, an increasing number of full-scale constructed wetlands (CWs) have
been put into operation (Garcìa, 2004; Puigagut at al., 2007). This rise in the
implementation of such treatment systems is because CWs have several advantages
over conventional wastewater treatment systems, particularly in small villages (≤
2000 population equivalent): staff do not require specific training, the operation and
maintenance costs are lower, and they integrate well into the surrounding landscape
(Vymazal, 2005; Rousseau et al., 2008; Pedescoll et al., 2009;Raboni et al., 2014).
Constructed wetlands are designed to use natural wetland processes that are
associated with wetland hydrology, soils, microbes and plants to treat wastewater
(Lee et al., 2005; Tang at al., 2009). CWs are artificial wastewater treatment systems
consisting of shallow (usually less than 1 m deep) ponds or channels which have been
planted with aquatic plants and which rely upon natural microbial, biological,
physical, and chemical processes to treat wastewater. They typically have impervious
clay or synthetic liners, and engineered structures to control the flow direction, liquid
detention time, and water level. Depending on the type of system, they may or may
not contain an inert porous media such as rock, gravel, or sand (Ranieri et al., 2014).
CWs can also remove Benzene from wastewater. This topic has been studied
increasingly in recent years (Eke and Scholz, 2008; Ranieri et al., 2013a).Benzene is a
hydrocarbon that occurs as a volatile liquid that is capable of rapidly evaporating,
colorless and highly flammable. In the atmosphere the most significant source of
benzene is represented by vehicular traffic, mainly from the exhaust gases of gasoline
powered vehicles. Therefore the highest concentrations are found in the proximity of
areas of intense traffic and large parking lots.
Otherwise hydraulic considerations have a significant role in prediction of the actual
removal percentages for every contaminant. This study assesses and elaborates the
hydraulic performance in the pilot-scale horizontal subsurface flow constructed
wetlands (HSFCWs) and observes trends over time. Design parameters such as aspect
ratio, size of the porous media, and hydraulic loading rate can improve the hydraulic
behavior of constructed wetland systems by imparting a hydraulic flow behavior that
approaches that of an ideal flow system (Ranieri, 2012; Ranieri and Young, 2012).
The experiments were conducted using tracer tests (KBr), which provided the
residence time distribution (RTD). Particularly, after 24 months of operating,
clogging conditions in experimental HSFCWs result in a lower hydraulic conductivity
values (Ranieri et al., 2013b).
The objectives of this study are: 1) to evaluate the hydraulic behavior of constructed
wetlands not planted and planted with different species (Phragmitesaustralis and
Typhalatifolia), by varying hydraulic conductivity; 2) to assess the correlation of the
experimental RTD curves with the curve of the model, as a function on the variation
Benzene Removal In Horizontal Subsurface Flow Constructed Wetlands 14605
of hydraulic characteristics and clogging; 3) to evaluate Benzene removal as a
function of the hydraulic residence time (HRT).
Material and Methods
Experimental Constructed Wetlands
The experimental area includes three constructed wetland fields, two containing
different species of plants and the third serving as a control reactor. Water is supplied
to the fields from four high density polyethylene (HDPE) tanks; samples are obtained
from eighteen sampling ports and effluent is stored in two lagoon ponds. Fig. 1
depicts the plan view of the site (Fig. 1A) and the longitudinalsection of one planted
constructed wetland bed (Fig. 1B). Each wetland has a planted area equal to 15 m2 (3
x 5 m), a water depth ranging from 0.6 m to 0.65 m and a resulting total volume of
approximately 9.4 m3. The constructed wetlands have a bottom slope of 1% to
facilitate the outflow of water by gravity. The stability of the side banks is ensured by
providing a 45° inclination. Five perforated tubes with 200 mm internal diameter are
positioned within each field to permit collection of water samples and control of water
levels. The bottom of each reactor is waterproofed with a bentonite liner that is
permeable to plant roots but largely impermeable to water. The liner consists of three
layers: an upper geotextile 220 g/m2, a lower geo-textile 110 g/m2, and sodic
powdered bentonite 4670 g/m2, containing approximately 90% montmorillonite. The
total weight of the geo-composite is 5000 g/m2 and its total dry thickness is 6 mm.
The hydraulic conductivity of the installed liner is k < 10-11 m/s.
Raw water is supplied at the reactor inlet and passes slowly through the filtration
medium under the surface of the bed in a generally horizontal path until it reaches the
outlet zone where it is collected and discharged to the lagoon. The filtration medium
consists of three layers: 0.1 m of soil, 0.2 m of stones, and 0.30 - 0.35 m gravel as
shown in Fig. 1B. The mineral composition of the substrate is 59% calcium carbonate,
32% silica and 9% iron oxide for the rocks and gravel. The soil is a mixture of red
clay and organic matter. The unplanted bed served as a control reactor to isolate the
impact of macrophytes and any microorganisms associated with their root mass on
Benzene removal. At no time during the study was the water depth above the top of
the media in any of the reactors, i.e., all flow was subsurface.
Residence time distribution (RTD) curves were assessed by introducing 30 L of a 10
g/L solution of lithium bromide along the first cross section of each wetland unit as a
conservative tracer.
Water samples were collected every 30 min from each of the sampling points. The
experiments were carried out from March to June during the vegetation period of the
macrophytes. Daily average temperatures during the four months of experimentation
range from 14 °C to 24 °C.
14606 Ezio Ranieri
Figure 1: Constructed wetlands pilot plant in Lecce, Italy, shown in (A) plan view
and (B) longitudinal section.
Tracer injection
Sampling for HRT measurements
The tracer used in the experimental plant was the potassium bromide (KBr), because
it is highly soluble, non-degradable, relatively inexpensive, and can be measured
quantitatively in very low concentrations. Tracer solution was added in 10 min mixed
with wastewater flow in order to reduce sinking effects related to density differences.
Composite samples of the effluent from each constructed wetland were collected in
500 mL amber glass bottles using an auto sampler. Effluent grab samples were taken
approximately every 12 h from the morning of day 3 until the evening of day 9. From
the morning of day 10 to the morning of day 12, samples were taken every 24 h. Tests
finished on the fourth day after a total sampling period of approximately 330 h. For a
Benzene Removal In Horizontal Subsurface Flow Constructed Wetlands 14607
time of approximately 300 h, the tracer concentration was not detected and, therefore,
a period of time of 300 h was enough to obtain a complete response of the tracer
injection. RTD curves were assessed by introducing 6 kg/m3solution of KBr in 10 min
along the first cross-section of each wetland unit as a conservative tracer.
Benzene sampling and analysis
Benzene solution was conveyed to the CWs from the supply tanks containing tap
water at a constant initial concentration of 0.5 mg/L, respectively, for each compound,
for all tests. Composite samples of the effluent from each constructed wetland were
collected in 500 mL amber glass bottles every 6 h using an auto sampler for a time
period of 220 d. Samples were collected at inlet and outlet two times per week and
were kept refrigerated at 4°C until analyses. Samples were analyzed according to
Standard Methods (APHA, 2005) using an HP 5890 series II Gas Chromatograph
equipped flame ionization detector and a split/splitless injector. Standard deviation
(SD) was calculated for each measurement series and was less than 5% for each
compound considered. For all measurements, standard Quality Control (QC) was
performed. QC samples consisted of triplicate samples and spiked samples.
Plug flow with dispersion reactor model
The RTD curves have been calculated using the plug flow with dispersion reactor
(PFDR) model by adjusting the HRT (θ) and the reactor Peclet number to minimize
the sum of the squared errors between the experimental bromide concentration data
and the analytical solution to the PFDR model given by Levenspiel and Smith (1975):
(1)
where iCi t is the area under the RTD curve, Pe is Peclet number, and θ is the HRT.
The equation has been modified from its original dimensionless form by multiplying
the summation of CiΔt, which approximates the area under the RTD curve.
Results and Discussion
Effect of Clogging
In the pilot HSFCWs, experimental curves have been collected at time t = 0 and at
time t = 24 months to the aim of evaluating the different clogging conditions. Table 1
reports the hydraulic parameters adopted for the experimental HSFCWs and utilized
in the model at the beginning of the experience and after two years for both planted
and unplanted fields.
14608 Ezio Ranieri
Table 1:Values of parameters that define hydraulic behavior of the tested
experimental plants and after 24 months (planted and unplanted).
Parameter
Symbol
Parameter Name
Value (at the
beginning)
Value (after
24 months for
planted fields)
Value (after 24
months for
unplanted field)
K
Hydraulic
Conductivity
30 [m/d]
25 [m/d]
30 [m/d]
Hout
Hydraulic head at
the outlet
0.6 [m]
0.6 [m]
0.6 [m]
αL
Longitudinal
Dispersion
0.2 [m]
0.35 [m]
0.35 [m]
αT
Tranversal
Dispersion
0.02 [m]
0.02 [m]
0.02 [m]
DKBr
Diffusion
2.02-5 [cm2/s]
2.02-5 [cm2/s]
2.02-5 [cm2/s]
p
Porosity
0.16
0.16
0.15
Fig. 2(A) shows the comparison between the experimental and the simulated RTD
curves, measured at the beginning of the experience in the experimental plant. A good
correspondence, R2 = 0.98, according to well-recognized model evaluation techniques
(Moriasi et al., 2007) between the simulation curve and the tracer test has been found.
A less-pronounced plug flow behavior in the Lecce plant is probably due to lower
porosity of the substrate. Phragmites HSFCWs behavior is quite similar to the Typha
ones, whereas the unplanted field showing a clearer plug flow behavior. The variation
from the ideal plug flow behavior and the coefficient correlation (R2) was equal to
0.92 for the unplanted field, 0.87 for the Phragmites field and 0.86 for the Typha
field.
(a)
Br [mg/L]
Time [h]
Bromide concentration at time t2= 24 months
(Phragmites and Typha)
Model t1
Model t2
Phragmites
Typha
Benzene Removal In Horizontal Subsurface Flow Constructed Wetlands 14609
(b)
(c)
Figure 2: Bromide concentration trends vs HRT at time t=0 (A) and t=24 months (B)
and (C).
After 24 months, tracer tests were performed and the results are illustrated in Fig.
2(B). The correlation between the model and the experimental data was less evident.
In particular, while the unplanted field still maintains a good plug flow behavior, the
Phragmites and the Typha plants show a decrease of the peak with lower concavity of
the curve and a higher distance from the model interpolation curve. This is probably
due to the lower hydraulic conductivity measured in the field hydraulic conductivity
decreasing from 30 to 25m/d for the Phragmites field and 25.2 m/d for the Typha
field, as reported in previous experiences. The RTDs for the unplanted wetland have
been assessed after 24 months. Results are shown in Fig. 2(C). It is observed that the
model curve interpolate very well the tracer experimental data in the unplanted field
where the hydraulic conductivity still remain equal to 30 m/d and only the porosity
decrease from 0.16 to 0.15 as measured in the field. The RTD curves have been
calculated using the PFDR model. All of the PFDR model fits to the tracer data had
Br [mg/L]
Time [h]
Bromide concentration at time t1=0
Phragmites
Typha
unplanted
model
Br [mg/L]
Time [h]
Bromide concentration at time t2= 24 months
(unplanted field)
unplanted
model
unplanted
14610 Ezio Ranieri
R2 values greater than 0.975. The differences between the RTD curves for the planted
reactors are probably related to the different root structures of the two species. The
roots of Phragmitesaustralis penetrate to a depth of approx. 51 cm, while
Typhalatifolia roots are not likely to extend beyond about 29 cm, according to
previous experience with these species (Bedessem et al., 2007). The differential root
penetration depth is likely to be responsible for the slightly different flow regimes in
the two wetland beds. Clogging was more significant in the Phragmites bed, and this
favors the development of preferential flow paths and causes the slightly shorter HRT
compared to the Typha one bed and the slightly lower Peclet number of 26.7 in
contrast to Pe for the Typha bed of 29.7. The unplanted bed had a Peclet number of
24.9.
Benzene Removal
The residual concentrations at the sampling points for Phragmites field ranged
between 0.88 mg/L at the out and 0.77 mg/L at the lagoon pond. The final residual
concentration in the Typha field was 0.83 mg/L, while in the pond it was 0.75 mg/L.
In the unplanted field the residual concentrations were 1.09 mg/L at the out and 0.74
mg/L at the pond (Fig. 3). Based on the above, the average removal efficiencies are
equal to 39.78% for the Phragmites field, 35.14% for the Typha field and 29.67% for
the unplanted one (Fig.4).
Figure 3: Benzene concentration at the sampling points in the Phragmites field, in the
Typha field and in the unplanted one.
0
0.5
1
1.5
2
2.5
Benzene (mg/l)
Phragmites
Typha
Soil
Benzene Removal In Horizontal Subsurface Flow Constructed Wetlands 14611
Figure 4:Percentage removal of Benzene measured in each sampling point from the
input in the Phragmites field, in the Typhafield and in the unplanted one.
The removal efficiencies determined in the present work are lower or similar
compared with a similar experimental work (Eke and Scholze, 2008;Machate et al.,
1999). The latter may be attributed to the fact that the inflow concentration at the
present concentration was lower (0.5 mg/L here, instead of 2 mg/L) (Gikas et al.,
2013). The observed removals in the Phragmites field were, on average, 11.67%
higher than the Typha field and 25.42% higher than the unplanted field. However,
because of the low affinity of the Benzene compounds with plant tissues, the direct
effect of vegetation should be less significant compared with the net effect of sorption
(Mitsch and Gosselink, 2000). However the effect of macrophytes is more evident
approx after 30 h HRT piezometer E and D where the difference between
percentage values of planted and unplanted is higher than 20% (Fig. 4). Higher
removal is probably due to the microbial communities associated with the plant
rhizosphere which create an environment conducive to degradation for many volatile
organic compounds (Schnoor et al., 1995). Benzene overall removal after pond
settlement is around 60 %.
Conclusions
CWs offer a potential for the removal of more than 50% of Benzene from wastewater
at HRT higher than 100 h, however, the latter correlation should be evaluated as a
function of inlet concentrations. Percentages removal at the outlet of plants varies
from 45.4% (unplanted) to 55.6% (Phragmites) and 58.6 (Typha).
Hydraulic residence time have been also evaluated in CWs experimental plants.
Model shows a good agreement with experimental data for plants. After 24 months
the hydraulic conductivity is varied from 30 m/d to 25 m/d for both Phragmites and
Typha plants in HSFCWs due to clogging and the model curve is capable of
0
10
20
30
40
50
60
70
Piez. A
Piez. B
Piez. C
Piez. D
Piez. E
Out
Pond
% removal
Phragmites
Typha
Soil
14612 Ezio Ranieri
interpolating this hydraulic behaviour variation. The lack of the vegetation in the
unplanted constructed wetland results in a constant value of the hydraulic
conductivity after 24 months of operating. In the unplanted field only a slightly
decrease of the porosity has been evidence. This causes a shift of the experimental
curve towards lower HRTs. The field measurement of hydraulic conductivity appears
to be one crucial parameter useful to predict the actual hydraulic behaviour.
Further large-scale experimental tests should be carried out to validate the results
presented in this paper.
Acknowledgements
This research has been partially financed by the PRIN Program, Italian Minister of
University.
Conflict of Interests
The authors declare that there is no conflict of interests regarding the publication of
this paper.
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... In the same manner, differences in the removal of pollutants among plants were also observed in this review. For example, the benzene removal potential (%) of a horizontal subsurface CW in South Italy showed different values using Phragmites australis (39.78%) and Typha latifolia (35.14%) [63]. The types of microorganisms present in a CW also affect the removal efficiency. ...
... In the same manner, differences in the removal of pollutants among plants were also observed in this review. For example, the benzene removal potential (%) of a horizontal subsurface CW in South Italy showed different values using Phragmites australis (39.78%) and Typha latifolia (35.14%) [63]. The types of microorganisms present in a CW also affect the removal efficiency. ...
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... A huge amount of pollutants is nowadays poured into all the environmental compartments and the effect on human health has been only partially evaluated Spasiano et al., 2017Spasiano et al., , 2019Alimi et al., 2018;Lucattini et al. 2018). These molecules are of inorganic and organic nature and must be removed to minimize risks to living species ( Petrella et al., 2013;2016a;Ranieri et al., 2015;Asfaram et al., 2016;Saad et al., 2017a, Saad and and Tahir, 2017Istrate et al., 2018;Fang et al., 2018;Papailias et al., 2018;Sillanp€ a€ a et al., 2018). In this respect, the continuous release of heavy metals (HM) has pushed the scientific community to deal with the problems related to soil and water pollution ( Petrella et al., 2010;Petruzzelli et al., 2011;Ranieri et al., 2016;Fang et al., 2018;Kom ınkov a et al., 2018) because of the biopersistence and toxicity of these contaminants (B anfalvi, 2011;Satyro et al., 2014;Ranieri et al., 2016;Mehta et al., 2018) which are produced by different sources such as leather tanning, electroplating, metals smelting and metal finishing operations ( Azimi et al., 2017;Femina Carolin et al., 2017). ...
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Agricultural wastes derived from olive oil production were used in wastewater engineering as lead, cadmium, and nickel ions sorbents. Experiments were carried out in distilled water (Troom) by the use of packed bed columns filled with grains (1–3 mm) which were eluted with single and multimetal solutions in the 3–10 mg/L concentration range. Operations were performed with different sorbent dosage (4–8 g) at flow rates ranging 0.3–0.7 L/h until exhaustion. Best retention capacities were 8.15, 3.5, and 2.9 mg/gsorbent respectively for Pb⁺², Cd⁺², and Ni⁺² in the case of the multimetal system (0.3 L/h, 8 g of sorbent, and 10 mg/L influent solution). EDX analysis carried out on the sorbent surface showed that the wt % ratios between the sorbed metals were similar to the ratios between the column overall capacities. Inter-diffusion of the ions in the Nernst stationary liquid film around the particle was identified as the step which controls the kinetics of the process. Exhausted wastes were successively recycled in cement mortars together with another aggregate as exhausted porous glass in order to obtain a lightweight composite with good consistency and interesting mechanical resistances.
... A large number of chemicals are today released in water [1][2][3], land [4,5], or air [6,7], with severe impacts on the environment and consequently on human health. Environmental remediation is based on the removal of these contaminants from air [8,9], soil [10,11], sediment, groundwater, and surface water [12][13][14][15] which are carried out with specific technological approaches. ...
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A porous waste glass (RWPG = recycled waste porous glass) was used in wastewater treatments for the removal of lead ions from single, binary, and ternary metal solutions (with cadmium and nickel ions). Experiments were performed in columns (30 cm3, 10 g) filled with 0.5–1 mm beads till complete glass exhaustion (breakthrough). In the case of single and binary solutions, the columns were percolated at 0.2 Lh−1 (2 mg Me+2 L−1); in the case of ternary solutions, the columns were percolated at 0.15–0.4 Lh−1 (2 mg Me2+ L−1) and with 2–5 mg Me2+ L−1 influent concentration (0.2 Lh−1). Lead ions were removed mainly by ion exchange and also by adsorption. From a kinetic point of view, the rate controlling step of the process was the interdiffusion of the lead ions in the Nernst stationary liquid film around the sorbent. The uptake of the metals and the glass selectivity were confirmed by Energy Dispersive X-ray spectroscopy (EDX) analysis. After lead retention process, glass beads were reused as lightweight aggregates for thermal insulating and environmental safe mortars.
... These promising results may be effective in light of the specific applications of these cellulosic lightweight materials in the field of sustainable constructions [85]. In fact, these composites may be adopted for indoor non-structural applications (passive constructions design, more efficient in terms of thermal insulation, and energy saving), also in consideration of the advantages related to the reuse of a waste from agriculture, which may suggest further employment in the environmental engineering of these or other natural materials from contaminated ecosystems after sorption of organic and inorganic pollutants [86,87]. ...
Article
In the present research, an environmentally sustainable material as wheat straw deriving from Apulia region, Southern Italy, was added to cement mortars and characterized by thermal, acoustic, mechanical, and microstructural measurements. The straw and the matrix composition were not modified and the mixture preparation did not require complex manufacturing or expensive procedures. The aim was to obtain a lightweight product for indoor applications using a renewable material from the agro-food industry and adopting a safe and cheap process. The samples with high straw content showed very low thermal conductivities exceeding 0.16 W/mK and good acoustic absorptions in the 500–1000 Hz range. The results were strongly dependent on the porosity of the composites, ascribed to the straw features and to the voids at the cellulose fibers/cement matrix interface. Moreover, preliminary observations of the material stability (microstructural analysis) demonstrated that the conglomerate components did not show detectable effects of degradation.
... Vymazal [39] classified them on the basis of the industrial processes: petrochemical and chemical industries; pulp and paper, textile and tannery industries; abattoir and meat processing effluents; food processing; wineries and distilleries. Treatment of contaminated waters from the petrochemical industry is aimed at removal of various hydrocarbons including diesel range organics, BTEX [17,45,46]. One of the most extensive horizontal flow (HF) CWs in Europe (total area of 49,000 m 2 ) was built at the Air Products chemical works at Billingham, Teeside, United Kingdom [47]. ...
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Constructed wetlands (CWs) are affordable and reliable green technologies for the treatment of various types of wastewater. Compared to conventional treatment systems, CWs offer an environmental-friendly approach, are low cost, have fewer operational and maintenance requirements, and have a high potential for being applied in developing countries; particularly in small rural communities. However, the sustainable management and successful application of these systems remain a challenge. Therefore, after briefly giving basic information on wetlands and summarizing the classification and use of current CWs, this study aims to provide sustainable solutions for the performance and applications of CWs. To accomplish this objective, design and management parameters of CWs, including macrophyte species, media types, water level, hydraulic retention time (HRT), and hydraulic loading rate (HLR), are discussed. The current study collects and presents results of more than 120 case studies from around the world. This work provides a tool for researchers and decision-makers for using CWs to treat wastewater in a particular area. This study presents an aid for informed analysis, decision-making, and communication.
... Consequently, besides proposing a sustainable wastewater treatment, the reuse of exhausted, expanded perlite to increase the insulating properties of cement is in accordance with circular economy principles [37] and with the recent trend towards sustainable water treatments [38][39][40]. ...
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This paper deals with the possibility of using perlite as a lead ion sorbent from industrial wastewater. Dynamic (laboratory column) operations were carried-out using beads, which were percolated by metals in a 2–10 mg·L−1 concentration range. To this purpose, lead ion solutions were eluted in columns loaded with different amounts of sorbent (2–4 g) within a 1–2 mm bead size range, at 0.15–0.4 L·h−1 flow-rates. Tests were performed to complete sorbent exhaustion (column breakthrough). The highest retention was obtained at 0.3 L·h−1, with 4 g of perlite and 10 mg·L−1 of influent, lead ion concentration. Film diffusion control was the kinetic step of the process in the Nerst stationary film at the solid/liquid interface. At the end of the sorption, perlite beads were used as lightweight aggregates in the construction field (i.e., for the preparation of cement mortars). Specifically, conglomerates showing different weights and consequently different thermal insulating and mechanical properties were obtained, with potential applications in plaster or panels.
... Constructed wetlands were introduced to the UK in the mid-1980s after the UK WRc (Water Researchcouncil)visitedKickuth,Seidel'sstudentwhowasanearlyadvocate of the technology (Boon, 1986). Later, the WRc and UK Water Services Associated established the Reed Bed Treatment System Coordinating Group, which combined the results of the initial technology trials carried out by water utilities with the plan of accelerating development Murphy and Cooper, 2010;Knowles, 2012). Severn Trent, a member of UK Water Services Associated, confirmed that HSSF CWs have an ability to treat domestic wastewater effluent for communities of <2000 people as a tertiary treatment and as a secondary treatment for communities of <50 people (Green and Upton, 1993). ...
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Wetlands have long played a significant role as natural purification systems. Textile industry processes are among the most environmentally unsustainable industrial processes, because they produce coloured effluents in large quantities polluting water. The aim of this study is to assess the performance of VFCWs to treat two different azo textile dyes with and without artificial wastewater for long periods of time through different operation modes such as contact and resting times, and loading rates, which has rarely been considered in previous research works. The corresponding key objectives are (a) to assess the role of gravel (as a control wetland) and plants on dye reduction and other pollutants; (b) to determine the influence of two groups of dyes (acid (AB113) and basic (BR46)), each dye having a different molecular weight and chemical structure, at two different concentrations (7 mg/l and 215 mg/l); (c) to evaluate the impact of the mixture of both dyes on the performance of vertical-flow constructed wetlands in terms of dye reduction with/without artificial wastewater; (d) to determine the annual and seasonal reduction; and (e) to assess the influence of operational parameters such as contact time (48h and 84h), resting time and mass loading rate on dye reduction and other pollutants for a long period. The first phase dealt with treating the two azo textile dyes only during the period between 1 June 2015 and 31 May 2016, while the second phase dealt with artificial wastewater containing the two azo textile dyes during the period between 1 June 2016 and 31 May 2017. According to the first phase, for the low concentration of BR46, there was no significant (p≥0.05) difference between the wetlands in terms of dye reductions. However, for chemical oxygen demand (COD), the reduction percentages were 50%, 59% and 67% for the control and for the wetlands with short and long contact times, respectively. All reductions were statistically significant (p<0.05). For the high concentration of BR46, the reduction percentages for the dyes were 94% and 82%, and for COD, they were 89% and 74% for the long and short contact times, correspondingly. A good reduction was noted for total suspended solids for long and short contact times. For the low concentration of AB113, the percentage reductions for the dye were 71%, 68% and 80%, and for COD, they were 5%, 7% and 16% for the control, and the short and long contact times, respectively. For the high concentration of AB113, the percentage reductions for the dye were 72% and 73%, and for COD, they were 54% and 55% for the 48 h and 96 h contact times in this order. Regarding ortho-phosphate-phosphorous for the low concentrations of BR46 and AB113, the reduction percentages for wetlands, which have high contact times, were significantly (p<0.05) better than those of the control wetlands, as well as wetlands, which have low contact times. In the case of high concentration regarding BR46, the reduction percentages of wetlands with low loading rates were significantly (p<0.05) better than wetlands with high loading rates, while for AB113, the reduction percentages of wetlands with high loading rate were significantly (p<0.05) better than those for wetlands with low loading rates. In the case of ammonia-nitrogen for the high concentration of dyes, there were no significant (p≥0.05) differences between wetlands. Regarding nitrate-nitrogen reduction for low and high concentration of BR46 and AB113, the reduction percentages for wetlands with long contact times were better than those for wetlands having short contact times. In the case of phase two, the presence of plants had no effect on the dye and COD reductions. For the low concentration of BR46, the percentage reductions for the dye were 92%, 89% and 91%, and for COD, they were 69%, 82% and 70% for the control, and the short and long contact times, respectively. All reductions were statistically significant (p<0.05). For the high concentration of BR46, the reduction percentages for the dyes were 73% and 33%, and for COD, they were 56% and 39% for the long and short contact times, respectively. For the low concentration of AB113, the percentage reductions for the dye were 85%, 77% and 82%, and for COD, they were 76%, 81% and 62% for the control, and the short and long contact times in this order. For the high concentration of AB113, the percentage reductions for the dye were 44% and 54%, and for COD, they were 40% and 56% for the 48 h and 96 h contact times, correspondingly. Regarding ortho-phosphate-phosphorous for the low concentrations in the case of AB113 and BR46 and the mixture of both dyes, the reduction percentage in wetlands with high contact time was significantly (p<0.05) better than those of the control wetlands and wetlands with low contact time. For the high concentration of BR46, AB113 and the mixture of both of them, wetlands with high resting and contact times had lower ortho-phosphate-phosphorous effluent concentrations when compared with wetlands with low resting and contact times. Regarding ammonia-nitrogen reduction percentages for low concentrations of BR46 and AB113 and the mixture of both dyes, wetlands with high resting times had better reduction percentages (p<0.05) when compared with the control wetlands as well as wetlands with low resting times. In the case of high concentrations for BR46, AB113 and the mixture of both of them, wetlands with low loading rates had a better reduction percentage when compared with wetlands with a high loading rate. Regarding nitrate-nitrogen reductions for low and high concentrations of BR46, AB113 and the mixture of both of them, the reduction percentages for all wetlands were in the range from 75 to 100%. Regarding aromatic amine compound reductions, wetlands with long contact times showed significant (p<0.05) differences when compared with the control and wetlands with short contact times for the low concentrations of BR46 and AB113. For the high concentration of BR46 and AB113, wetlands with low loading rates showed a significant difference (p<0.05) when compared with wetlands with a high loading rate. The researcher recommended that using HPLC combined with FTIR to investigate the reduction in aromatic amines and working on modelling of the results should help the designer in improving the construction of wetlands on an industrial scale.
... Trichloromethane e (1) (Keefe et al., 2004) Dichloromethane e (1) (Keefe et al., 2004) 1,2-dichloroethane e (2) (Kassenga et al., 2004;Kassenga and Pardue, 2006) Pentachlorobenzene e (1) (Matamoros et al., 2007b) Benzene e (25) (Braeckevelt et al., 2007;Brovelli et al., 2011;Chen et al., 2012b;Chen et al., 2014b;De Biase et al., 2011;Eke and Scholz, 2008;Fester, 2013;Ho et al., 2012;Mothes et al., 2010;Ranieri et al., 2013;Ranieri et al., 2014;Ranieri et al., 2015;Reiche et al., 2010;San Miguel et al., 2013;Schurig et al., 2015;Seeger et al., 2013;Seeger et al., 2011;Tang et al., 2009a (1) (Peters et al., 2001) a Dieldrin e (1) (Peters et al., 2001) No studies were found for the other 17 organic PSs (some are classes of substances) defined in Directive 2013/39/EU, namely: trichlorobenzenes, chloroalkanes, dioxin and dioxin-like compounds (polychlorinated biphenyls and polychlorinated dibenzofurans), anthracene, polycyclic aromatic hydrocarbons (indeno(1,2,3-cd)pyrene, benzo(k) fluoranthene, benzo(g,h,i)perylene, benzo(k)fluoranthene, benzo(b)fluoranthene, benzo(a)pyrene), hexabromocyclododecanes (g-hexabromocyclododecane, b-hexabromocyclododecane, a-hexabromocyclododecane, 1,2,5,6,9,10-hexabromocyclododecane, 1,3,5,7,9,11-hexabromocyclododecane), brominated diphenylethers (heptabromodiphenylether, hexabromodiphenylether, pentabromodiphenylether, tetrabromodiphenylether), bifenox, aclonifen, quinoxyfen, cypermethrin, terbutryn, cybutryne, dichlorvos, hexachlorobutadiene, hexachlorocyclohexane, heptachlor and its epoxide, dicofol. a No studies were either found for 6 of the other substances with EQS defined in Directive 2013/39/EU, namely: trichloro-ethylene, tetrachloro-ethylene, carbon tetrachloride, endrin, isodrin and aldrin. ...
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The presence of organic pollutants in the aquatic environment, usually found at trace concentrations (i.e., between ng L⁻¹ and μg L⁻¹ or even lower, known as micropollutants), has been highlighted in recent decades as a worldwide environmental concern due to their difficult elimination by conventional water and wastewater treatment processes. The relevant information on constructed wetlands (CWs) and their application for the removal of a specific group of pollutants, 41 organic priority substances/classes of substances (PSs) and 8 certain other substances with environmental quality standards (EQS) listed in Directive 2013/39/EU as well as 17 contaminants of emerging concern (CECs) of the Watch List of Decision 2015/495/EU, is herein reviewed. Studies were found for 24 PSs and 2 other substances with EQS: octylphenol, nonylphenol, perfluorooctane sulfonic acid, di(2-ethylhexyl)phthalate, trichloromethane, dichloromethane, 1,2-dichloroethane, pentachlorobenzene, benzene, polychlorinated dibenzo-p-dioxins, naphthalene, fluoranthene, trifluralin, alachlor, isoproturon, diuron, tributyltin compounds, simazine, atrazine, chlorpyrifos (chlorpyrifos-ethyl), chlorfenvinphos, hexachlorobenzene, pentachlorophenol, endosulfan, dichlorodiphenyltrichloroethane (or DDT) and dieldrin. A few reports were also published for 8 CECs: imidacloprid, erythromycin, clarithromycin, azithromycin, diclofenac, estrone, 17-beta-estradiol and 17-alpha-ethinylestradiol. No references were found for the other 17 PSs, 6 certain other substances with EQS and 9 CECs listed in EU legislation.
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A comparison between model and experimental pilot-scale horizontal subsurface flow constructed wetland (HSFCW) located in Lecce (Apulia, South Italy) has been reported in the paper. The experiments were carried out in three constructed wetlands each with a planted area equal to 15 m(2) and with water depth of 0.6 m. Tracer tests were conducted by single-shot injection of a dissolution of KBr into the inlet tubes of the beds. The objective of the study was to compare hydraulic performances in a pilot experiences and to evaluate the suitability of two-dimensional method for describing the hydraulic behaviour of the HSFCW. At the beginning of the experience and after 24 months the results show the variation of the hydraulic conductivity and a good correlation between model and physical data by modifying input parameters as a consequence of the clogging.
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Constructed wetlands are a natural alternative to technical methods of wastewater treatment. They can remove Benzene, Toluene, Ethylbenzene, Xylenes (BTEX), and metals from wastewater, which are commonly encountered pollutants. In this paper, an experimental pilot-scale Horizontal Subsurface Flow Constructed Wetland (HSFCW) located in Lecce (Apulia, South Italy) has been reported. The experiments were carried out in three constructed wetlands. Two of them were planted with two different species of macrophytes and the third was used as a control. The objectives of this study are to compare hydraulic behavior of the CWs with the trend of the model by varying the hydraulic conditions, to evaluate the effect of the clogging and then to assess the efficiency of the different species of macrophytes in removing BTEX and metals. At the beginning of the experience and after 24 months, the results show a good correlation in the hydraulic behavior between model and physical data by modifying input parameters as a consequence of the clogging. The BTEX removal planted fields is higher than the unplanted one, while the three HSFCWs have a similar capacity in removing Cr, Fe, and Pb.
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The paper presents the results of an experimental process designed for the treatment of the sewage generated by a rural community located in the north-east of Brazil. The process consists of a preliminary mechanical treatment adopting coarse screens and grit traps, followed by a biological treatment in a UASB reactor and a sub-surface horizontal flow phytodepuration step. The use of a UASB reactor equipped with a top cover, as well as of the phytodepuration process employing a porous medium, showed to present important health advantages. In particular, there were no significant odor emissions and there was no evidence of the proliferation of insects and other disease vectors. The plant achieved the following mean abatement efficiencies: 92.9% for BOD5, 79.2% for COD and 94% for Suspended Solids. With regard to fecal indicators average efficiencies of 98.8% for fecal coliforms and 97.9% for fecal enterococci were achieved. The UASB reactor showed an important role in achieving this result. The research was also aimed at evaluating the optimal operating conditions for the UASB reactor in terms of hydraulic load and organic volumetric loading. The achieved results hence indicated that the process may be highly effective for small rural communities in tropical and sub-tropical areas.
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The aim of this research was to assess the treatment efficiencies for gully pot liquor of experimental vertical-flow constructed wetland filters containing Phragmites australis (Cav.) Trin. ex Steud. (common reed) and filter media of different adsorption capacities. Six out of 12 filters received inflow water spiked with metals. For 2 years, hydrated nickel and copper nitrate were added to sieved gully pot liquor to simulate contaminated primary treated storm runoff. For those six constructed wetland filters receiving heavy metals, an obvious breakthrough of dissolved nickel was recorded after road salting during the first winter. However, a breakthrough of nickel was not observed, since the inflow pH was raised to eight after the first year of operation. High pH facilitated the formation of particulate metal compounds such as nickel hydroxide. During the second year, reduction efficiencies of heavy metal, 5-days at 20 degrees C N-Allylthiourea biochemical oxygen demand (BOD) and suspended solids (SS) improved considerably. Concentrations of BOD were frequently < 20 mg/L. However, concentrations for SS were frequently > 30 mg/L. These are the two international thresholds for secondary wastewater treatment. The BOD removal increased over time due to biomass maturation, and the increase of pH. An analysis of the findings with case-based reasoning can be found in the corresponding follow-up paper (Part B).
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Benzene, toluene, ethylbenzene, and xylenes (BTEX) are commonly encountered pollutants. The focus of the present work is on the removal of BTEX using pilot-scale constructed wetlands (CWs). Experiment carried out in three similar pilot-scale horizontal sub-surface flow constructed wetlands with an area of 35 m2 (each), two of which were planted with different macrophytes (Phragmites australis and Typha latifolia), while an unplanted one was used as control. A number of hydraulic tests were carried out using lithium bromide as tracer, to assess the hydraulic residence time. Residence time distributions for the two CWs indicated that the Typha field was characterized by a void volume fraction (porosity) of 0.16 and exhibited more ideal plug flow behavior (Pe = 29.7) compared with the Phragmites field (Pe = 26.7), which had similar porosity. The measured hydraulic residence times in the planted fields were 35.8, 36.7, and 34.1 h for Typha, Phragmites, and unplanted respectively, at wastewater flow rates equal to 1 m3/d. The observed percentage removal for BTEX ranged between 46 and 55%. The average removal in the Phragmites field was 5% higher than the Typha field and 23% higher than the unplanted field. BTEX removal was primarily attributed to volatilization; however, biodegradation also played a significant role.
Article
Background Two pilot scale horizontal subsurface flow constructed wetlands (HSFCWs), with a planted area of 15 m2 each, were constructed in Puglia, Italy, and planted with hydrophytes (Phragmites australis and Typha latifolia), while a similar field of equal size was used as a control. The primary aim of the present work was to assess the removal of three heavy metals from waste water, in relation to the evapotranspiration, using HSFCWs. ResultsResidence time distributions in both planted HSFCWs indicated that the Typha field had porosity of 0.16 and exhibited more ideal plug flow behavior (Pe = 29.7), compared with the Phragmites field (Pe = 26.7), which had similar porosity. The measured hydraulic residence times in the planted fields were 35.8 and 36.7 h, for Typha and Phragmites, respectively, at waste water flow rates of 1 m3 d−1 (corresponding to hydraulic loading rate of 66.7 mm d−1). Heavy metals concentrations at the inlet were 2 mg/L, for each heavy metal, while at the outlet of the fields were Cr = 0.23 mg L−1, Pb = 0.21 mg L−1 and Fe = 0.18 mg L−1 in the Phragmites field, and the removal rates were 87, 88 and 92% of Cr, Pb and Fe, respectively. The Typha field showed a similar behavior with concentrations equal to Cr = 0.19 mg L−1, Pb = 0.23 mg L−1 and Fe = 0.16 mg L−1 and removal percentages of 90, 87, and 95% of Cr, Pb and Fe, respectively. The control field showed metal removals slightly lower (86, 78 and 88% for Cr, Pb and Fe, respectively). ConclusionsHSFCWs are appropriate for removing heavy metals from waste water. Evapotranspiration may significantly reduce the amount of discharged flow and may influence the removal rate of heavy metals. © 2013 Society of Chemical Industry
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The longitudinal mixing of fluids in flow can sometimes be characterized by a single parameter D, the “longitudinal dispersion coefficient.” which is analogous to and has the same units as the coefficient of molecular diffusion. The results of a study of this model show that a dimensionless parameter, the Peclet number can be used as the similarity criterion for longitudinal mixing. Also, it is pointed out that the obvious and direct method of calculating the mean velocity of flow, by injecting a tracer into the fluid stream at one point and measuring its maximum concentration at a given point downstream, may in some cases lead to an appreciable error, even in situations where the diffusion-type model is applicable. Methods are shown for evaluating D from experimental measurements, examples are worked out and conditions for applicability of the model are discussed.RésuméEn écoulement des fluides, le mélange dans le sens longitudinal peut être caractérisé par un paramètre unique D : “coefficient de dispersion longitudinal” analogue au coefficient de diffusion moléculaire et exprimé avec les mêmes unités. Les résultats d'une étude de ce type montre que le nombre sans dimension de Perclet peut être utilisé comme critère de similitude pour les mélanges “longitudinaux.” De même les auteurs signalent que la méthode classique et directe pour la mesure de la vitesse d'écoulement d'un fluide par introduction d'un traceur et mesure de sa concentration maximum en un point donné, peut en certain cas donner des erreurs appréciables, même dans les cas où le type de diffusion modèle peut être appliqué. Ils indiquent des méthodes pour calculer D à partir de mesures expérimentales, donnent des exemples avec les conditions d'utilisation.
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Contaminated ground water from a former coke plant site was purified in a free water surface (FWS) constructed wetland plant during a 3-mo short-term experiment. The pilot plant (total surface area 27 m²) was filled with a 1 m thick lava-gravel substrate planted with cattail (Typha spp.) and bulrush (Scirpus lacustrls). Major contaminants were low to moderate concentrations of polycyclic aromatic hydrocarbons, BTEX, nitrate, and nitrite. The wetland was dosed at hydraulic loading rates of q{sub A} = 4.8 and 9.6 cm d⁻¹ with a hydraulic residence time (HRT) of 13.7 and 6.8 d. The surface removal rates of PAH were between 98.8 and 1914 mg m⁻² d⁻¹. Efficiency was always
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This paper presents a simple method for evaluating the degree of clogging of subsurface flow constructed wetlands based on saturated hydraulic conductivity measurements. The method was applied to two full-scale wetlands located inside the wastewater treatment plants of two small villages (2000 PE) in the province of Lleida, Catalonia, Spain. In addition, to gain an insight into the mechanisms that lead to clogging, other measurements and analyses were carried out including the quantification of accumulated solids and belowground plant biomass. X-ray diffraction analyses were carried out to evaluate the mineral composition of accumulated sludge and granular medium. Hydraulic conductivity measurements and samples for solids analyses were taken along two transects that spanned the length of each wetland. Patterns for hydraulic conductivity were the same in both wetlands: very low values from the inlet zone to the middle (