VIETNAM NATIONAL UNIVERSITY, HANOI VIETNAM JAPAN UNIVERSITY VU THI THOM STUDY ON POTENTIAL PLANTS FOR USE IN CONSTRUCTED WETLAND TO STRENGTHEN PHOSPHORUS TREATMENT PERFORMANCE FROM SW
Trang 1VIETNAM NATIONAL UNIVERSITY, HANOI
VIETNAM JAPAN UNIVERSITY
VU THI THOM
STUDY ON POTENTIAL PLANTS FOR USE IN CONSTRUCTED WETLAND TO STRENGTHEN PHOSPHORUS TREATMENT PERFORMANCE
FROM SWINE WASTEWATER
MASTER'S THESIS
Trang 2VIETNAM NATIONAL UNIVERSITY, HANOI
VIETNAM JAPAN UNIVERSITY
VU THI THOM
STUDY ON POTENTIAL PLANTS FOR USE IN CONSTRUCTED WETLAND TO STRENGTHEN PHOSPHORUS TREATMENT PERFORMANCE
FROM SWINE WASTEWATER
MAJOR: ENVIRONMENTAL ENGINEERING
CODE: PILOT SUPERVISORS
DR NGUYEN THI AN HANG ASSOC PROF DR SATO KEISUKE
DR NGUYEN THI HOANG HA
Trang 3ACKNOWLEDGMENTS
First of all, I would like to express the sincere gratitude to my principal supervisor, Dr Nguyen Thi An Hang at VNU Vietnam Japan University, for accepting me as her master student and continuous teaching and supporting me in the process of doing experiments as well as writing essays and making presentations She always encourages and is willing to help me when I have difficulties She is always beside me to teach me how to work effectively This helps me grow up in both personal and professional aspects A special thanks also
go to Assoc Prof Dr Sato Keisuke for his recommendations to my research He provided me with the best conditions for implementing my experiments during my internship in Japan He is wholeheartedly devoted to his students I would like to express my deepest thanks to Dr Nguyen Thi Hoang Ha She gave me valuable supports in developing research methods, and enthusiastically guided me to fullfil
my thesis I always feel grateful to her for accompanying me for such a long time
The second, I would like to send my sciencere thanks to Prof Dr Jun Nakajima for supporting not only me but also all of memerbers in my class during Master course He cares for us like his children And he is our respected father
The third, I am grateful to Ms Nguyen Thi Xuyen, the project staff, for always supporting me in conducting experiments as well as analyzing environmental parameters
This research is funded by Vietnam National Foundation for Science and Technology Development (NAFOSTED) under grant number 105.99-2018.13,
2018 Asean Research Center (ARC) research grant of Vietnam National University, Hanoi (VNU), and Japan International Cooperation Agency (JICA) research grant for the academic year of 2018-2019
My heartfelt thanks and gratitudes to my family for their unconditional helps with plant sampling, the love and encouragement
Hanoi, June 9th, 2019
Vu Thi Thom
Trang 4TABLE OF CONTENTS
ACKNOWLEDGMENTS i
LIST OF TABLES ii
LIST OF FIGURES iii
LIST OF ABBREVIATIONS v
INTRODUCTION vi
CHAPTER 1: LITERATURE REVIEW 1
1.1 Overview of the situation of pig husbandry in Vietnam 1
1.1.1 Current status and development orientation of pig breeding 1
1.1.2 Environmental pollution due to swine wastewater 2
1.1.3 Technologies for the treatment of swine wastewater 4
1.2 Phosphorous pollution and treatment technologies 5
1.2.1 Phosphorus pollution and its consequences 5
1.2.2 Phosphorus treatment technologies 6
1.3 Constructed wetland for wastewater treatment 7
1.3.1 Definition and classification of CWs 7
1.3.2 Influential factors and treatment performance 9
1.4 Removal phosphorus by plants in the CWs 12
1.4.1 Classification of plants used in CWs 12
1.4.2 Removal P mechanisms by plants 14
CHAPTER 2: MATERIALS AND RESEARCH METHODOLOGY 18
2.1 Research object, scale, and scope 18
2.1.1 Research object 18
2.1.2 Research scale & scope 18
2.2 Materials, chemicals and equipment 19
2.2.1 Materials 19
2.2.2 Experimental design 20
2.2.3 Plant sample preparation and P analysis 25
Trang 52.2.4 Analysis of other water quality parameters 26
2.3 Data calculation 27
2.4 Data statistical analysis 28
CHAPTER 3: RESULTS AND DISCUSSION 29
3.1 Screening potential plants for use in the CWs 29
3.1.1 Selection of potential plants based on their P content and biomass growth 29
3.1.2 Selection of CWs plants based on other growth characteristics 33
3.2 Factors influencing the growth and uptake of p of Cymbopogon citratus and Ubon paspalum 35
3.2.1 Effect of initial P concentration 35
3.2.2 Effect of pH 42
3.2.3 Effect of plant age 45
3.2.4 Effect of plant density 49
3.2.5 Effect of water level 52
3.3 Applicability of the selected plants in the constructed wetland 54
CHAPTER 4: CONCLUSION AND RECOMMENDATION 57
4.1 Conclusion 57
4.2 Recommendations 57
REFERENCE 58
APPENDIX 62
Trang 6LIST OF TABLES
Table 1.1 Annual growth rate of culture sector (%) 1
Table 1.2 Composition and characteristics of swine wastewater 3
Table 1.3 Methods for handing and using liquids at systems 4
Table 1.4 3 main parameters of swine wastewater after biogas treatment 5
Table 1.5 P removal by Constructed Wetland 11
Table 1.6 Plant species are used to treat swine wastewater 13
Table 1.7 P removal efficiency by plants in CW (Jesus et al., 2017) 15
Table 2.1 The list of investigated plants 19
Table 2.2 Methods for examination of water quality parameters 27
Table 3.1 The P content in plants use for phytoremediation or CWs 31
Table 3.2 The P removal potential of the studied plants 33
Table 3.3 Growth characteristics of potential plants 34
Table 3.4 The P removal efficiency by different plant species 39
Table 3.5 Biomass growth rate of Ubon paspalum at different plant ages 48
Table 3.6 Effect plant density on the biomass growth rate of Ubon paspalum 51
Trang 7LIST OF FIGURES
Figure 1.1 Eutrophication: cause and effect 5
Figure 1.2 P removal in CWs 9
Figure 2.1 Scheme of horizontal constructed wetland 23
(at the start of experiment) 23
Figure 2.2 The structure of filter media in CWs and adsorption units 24
Figure 2.3 Plant sample preparation and analysis 25
Figure 2.4 Images of apparatus used in this study 26
Figure 3.1 The P content and its distribution in the studied plants 29
Figure 3.2 Images of the investigated plants in this study 34
Figure 3.3 Effect of initial P concentration on the removal efficiency of Cymbopogon citratus 37
Figure 3.4 Effect of initial P concentration on the removal efficiency of Ubon paspalum 37
Figure 3.5 P concentration left in solution plant with Ubon paspalum 38
Figure 3.6 P concentration left in solution planted with Cymbopogon citratus 38
Figure 3.7 Effect of intial P concentration on P removal rate of Ubon paspalum 40
Figure 3.8 Effect of intial P concentration on P removal rate of Cymbopogon citratus 40
Figure 3.9 Ubon paspalum died at the highest P concentration 41
Figure 3.10 Cymbopogon citratus could adapt with a wide range of initial P concentration 41
Figure 3.11 Normal growth of Cymbopogon citratus at all pH values 42
Figure 3.12 The death of Ubon paspalum at pH values of 9&11 43
Figure 3.13 Speciation of P in solution at various pH conditions 43
Figure 3.14 Effect of pH on P removal efficiency of Ubon paspalum and Cymbopogon citratus 44
Figure 3.15 Effect of pH on P removal rate of Ubon paspalum and Cymbopogon citratus 45
Trang 8Figure 3.16 Effect of plant age on P removal efficiency and P removal rate of Ubon
paspalum (hydroponic experiment) 47
Figure 3.17 The effect of plant age on the growth of root system 47
Figure 3.18 Effect of plant age on the biomass growth of Ubon paspalum 48
(experiment with garden soil) 48
Figure 3.19 Effect of plant density on P removal rate of the investigated plants 50
Figure 3.20 Effect of plant density on the P removal efficiency of the investigated plants 50
Figure 3.21 The root growth of Ubon paspalum at different plant densities 52
Figure 3.22 Effect of Ph on P removal rate of plants 53
Figure 3.23 Effect of water level on root growth of Ubon paspalum 54
Figure 3.24 The change of phosphorus in the effluent over the time 54
Figure 3.25 P removal efficiency and Ph after treatment of HFCWs 55
Figure 3.26 The plants growth well after 2 weeks of system operation 56
Trang 9LIST OF ABBREVIATIONS
COD Chemical oxygen demand
CW Constructed Wetland BOD Biological oxygen demand EBPR Enhanced biological phosphorus removal EPA Environmental Protection Agency
HF Horizontal flow HLR Hydraulic loading rate HRT Hydraulic retention time SSF Subsurface water flow
SF Surface flow
TN Total nitrogen
TP Total phosphorus TSS Total suspended solids
VF Vertical flow WHC White hard clam
Trang 10INTRODUCTION
Background
In Vietnam, in recent years, pig breeding industry has developed rapidly Since most of pig farms have not designed and operated appropriately, wastewater from pig farms cause serious environmental pollution, which poses a high risk to public health and surrounding ecosystems Therefore, the proper treatment of swine wastewater is urgent and necessary At present, swine wastewater in Vietnam is normally treated
by biogas technology However, the concentration of pollutants in the effluent is still high, exceeding national discharge standards (QCVN 01-79: 2011/BNNPTNT) Thus, further processing after biogas treatment of swine wastewater is mandatory Constructed wetlands (CWs) is a promising technology, which possesses many advantages, such as cost-effective, green technology (Wu et al., 2015; Yang et al, 2018;), low land, energy, and less-operational requirements (Wu et al., 2015); simple construction and operation (Bunce et al., 2018) However, the wide application of CWs is limited by intensive land requirement, long-term unsustainability (Bunce et al., 2018) Especially, although CWs can achieve high removal efficiency with TSS, COD, BOD, it is demonstrated to be inefficient in nutrient elimination It is well-known that the treatment performance of phosphorus by CWs is low and unstable Hence, the enhancement of phosphorus removal by CW is of great significance Since phosphorus is eliminated by CWs mainly via substrate adsorption, plant uptake, microbial degradation, selection and application of potential plants in CWs plays an important role
Plant-based treatment technology is known as phytoremediation, which receives the great interests of scientists in the world So far, a numerous number of studies on successful phytoremediation of wastewater polluted by phosphorus The most common types of plant species for nutrient removal are Typha latifolia, Cyperus papyrus, Phragmite australiis (Almuktar et al., 2018) TP removal efficiency of
Trang 11Phragmites communis, Typha orientatlis and Sparganium stoloniferum was 72.67%, 73.39%, 71.54%, respectively (Liu et al., 2012) TP was considerably eliminated by Persicaria hydropiper, representing 97.63% (Zheng et al., 2013) However, these are wildlife grass type with no or less economic value There is still lack of information about potential plants with high economic value for phytoremediation and CWs to treat P- rich water and wastewater Also, very few studies on factors influencing the growth and utapke of phosphorus by plants
The objectives of this study comprise (1) to search for potential plants for phosphorus decontamination from wastewater, (2) to investigate five factors
influencing the growth and phosphorus removal efficiency of Ubon paspalum and
Cymbopogon citratus, (3) to evaluate the applicapability of selected plant (Ubon paspalum) in the constructed wetlands for treatment of synthetic swine wastewater
Thesis’ outline
The thesis has been completed by 5 chapters The main contents of each chapter are provided as below
Introduction: Introduce the research content, identify research issues, tasks,
purposes, research scope
Chapter 1: Literature review - Providing information on the characteristics of
P factor, the negative impact of P on the environment, technological solutions implemented to eliminate P, the removal efficiency of Contructed Wetland, roles and mechanisms P removal of plants
Chapter 2: Materials and methods - Describe potential plant selection
methods, methods of analyzing P content in plants and water, methods of setting up experiments to study absorption capacity of plants under the influencing factors
Chapter 3: Results - Focus on describing the results of plant uptake rates and
assess the role of plants in the P removal in CWs
Trang 12Chapter 4: Discussion and recommendation - Summarizes major findings of
this study Additionally, the unique contributions of this study to the field of phosphorus removal by plants are provided Provide limitations and for future research direction
Appendices – provides some pictures in research activities
Trang 13CHAPTER 1: LITERATURE REVIEW
1.1 Overview of the situation of pig husbandry in Vietnam
1.1.1 Current status and development orientation of pig breeding
According to FAO, Asia will become the region, which produces and consumes livestock products the most Like other countries in the region, Vietnam needs to maintain high growth level to meet the demand of domestic consumption and export In recent years, the livestock industry in Vietnam has developed rapidly The annual growth rate of livestock in the period of 2006-2010 was 8.5%
Table 1.1 Annual growth rate of culture sector (%)
Source: Vietnam Agricultural Economics Institute, 2009
Recently, there is a trend to develop centralized animal husbandry As a result, the number of large-scale farms is increasing By 2006, Vietnam has 17,721 farms throughout the country, of which there is 7,415 pig farms, accounting for 42.18% The number of pig farms has increased from 3,293 to 14,481 in the period of 2011-
2016
Among Asian countries, Vietnam has to suffer from high pressure of land use The fast population growth and urbanization have resulted in a reduction of agricultural land In order to ensure food security, Vietnam has no choice but
Trang 14implementation of intensive animal husbandry Of which, pig raising plays an important role According to Decision No 10/2008/QĐ-TTg dated on 16 January
2008 by the Prime Minister on the approval of livestock development strategy to
2020, the proportion of livestock in the agriculture will increase from 32% (2010) to 38% (2015) and reach 42% (2020)
1.1.2 Environmental pollution due to swine wastewater
a Characteristics of swine wastewater
The swine wastewater can pose a high risk to the environment, due to high content of organic matter, TSS, N, P, and pathogen According to the report to assess the current status of the environment by Institute for Animal Husbandry (2006), in centralized pig farms in Ha Noi, Ninh Binh, Nam Dinh, Quang Nam, Binh Duong, Dong Nai, the swine wastewater is characterized as follows:
- Organic matter accounts for 70-80%, including cellulose, protein, acid amine, lipid, hydrate carbon, …
- Inorganic matter represents 20-30%, including, salts (chloride, sulfate, etc.)
- Nutrients (N and P): The swine wastewater usually contains high levels of N and
P (e.g TN 200-350 mg/ L of which N-NH4 accounts for 80-90%, TP 60-100 mg/ L)
- Pathogens: Swine wastewater may contain microorganisms, virus, eggs of parasites, etc
Trang 15Table 1.2 Composition and characteristics of swine wastewater
No Parameters Unit Value Category A, QCVN
Source: Xuyen Viet Environment Company
b Swine wastewater management
In recent years, the pig breeding industry has developed rapidly However, most of them have been developed spontaneously and have not met the technical standards for breeding facilities Therefore, breeding productivity is usually low and the surrounding environment is seriously polluted The wastewater from pig farms includes urine, wastewater from pig bathing and facilities cleaning A majority of pig farms discharge directly the wastewater into surrounding water bodies, causing unpleasant smells (H2S and NH3) especially in the hot and sunny days The ineffective management of swine wastewater is due to huge amount of wastewater is generated, which cannot be used all for arable lands in surrounding areas It is estimated that the need of clean water for cleaning breeding facilities, pig bathing, pig drinking is 30-50 L/ pig head/ day The bad smell, hindering its transport for long distances for purposes of agriculture and aquaculture development
Trang 16Table 1.3 Methods for handing and using liquids at systems
Discharge into environment
m3 2.22 ±2.23 4.91±2.95 3.98 ±5.75 3.50±5.40
1.1.3 Technologies for the treatment of swine wastewater
Numerous technologies have been used for treatment of swine wastewater, which can be divided into (1) Mechanical treatment method, (2) Physio-chemical treatment method, and (3) Biological treatment method Of which, biological treatment method is mainly used after mechanical and physio-chemical treatment
Biological treatment methods comprise both aerobic and anaerobic treatment The anaerobic treatment processes include biogas, anaerobic tank, anaerobic biological trickling filtration, upflow anaerobic slug blanket (UASB), expanded granular sludge bed (EGSB) The commonly used aerobic processes are aerotank, aerobic biological filtration, biological lagoon, algae, aquatic plants In order to cut down the price of pig breeding, farm owners in Vietnam tend to simply apply biogas instead of combining various technologies The commonly used treatment train is: Swine wastewater => Biogas tank => Lagoon => Environment Consequently, the effluent after biogas treatment is heavily polluted, and far above the discharge standard (QCVN 40:2011/BTNMT)
Trang 17Table 1.4 3 main parameters of swine wastewater after biogas treatment
1.2 Phosphorous pollution and treatment technologies
1.2.1 Phosphorus pollution and its consequences
Phosphorous is an element essential for plant growth It is actively involved in main functions of plants, such as photosynthesis, energy conveyance, activation of protein, control of metabolic processes, etc (Vo et al., 2017) However, the excessive level of phosphorus may cause the eutrophication in natural water bodies
Figure 1.1 Eutrophication: cause and effect
This results in many water quality issues, including deterioration of water quality and algal bloom Degradation of algal reduces O2 but increase CO2 in water, thus influencing the life of aquatic organisms The lack of oxygen leads anaerobic decomposition of organic matter, producing foul smell (H2S, NH3, CH4) (Thongtha
et al., 2014) Phosphorus in water and wastewater may come from natural or artificial
Trang 18activities Natural activities include earthquake, soil erosion, etc Human activities can release phosphorus into aquatic medium, such as agriculture, wastewater, storm water, etc The contribution of domestic sewage, agriculture and industry to the global phosphorous load is 54, 38, and 8% respectively The phosphorus load from agriculture in USA increased by 27%, from 579,000 to 734,000 tons in 2010
1.2.2 Phosphorus treatment technologies
Phosphorus decontamination from wastewater can be done via physical, chemical or biological methods Physical methods include membrane, magnetic separation, adsorption, ion exchange etc Chemical processes are precipitation, crystallization
Biological methods comprise EBPR, phytoremediation, constructed wetlands, etc Each method has both advantages and limitations Typically, the chemical precipitation is widely used for phosphorus treatment, because it is flexible, easy to install, high P removal, less space requirement However, its application is limited due to high chemical demand, chemical sludge generation, effluent neutralization requirement, difficult to identify optimal dosing conditions, low bioavailability of end-products, unsuitable for wastewater with low P levels Another method for phosphorus removal is adsorption This method is favored because of simple operation, less chemicals use, no sludge formation, suitability for P-poor wastewater Nevertheless, limitations of this method are high cost, disposal problems after use, etc In a study conducted by Gustafsson et al (2008) using naturally occurring materials, the phosphorus removal efficiency reached 95% In another study, Seo et
al (2013) reported that phosphorus could be removed up to 90% In recent years, phosphorus removal using enhanced biological methods has received great interests
of scientists in the world, due to the dominant advantages of modest cost, minimal sludge formation or ability to remove phosphorus to very low levels According to Smith et al (2014) Sun et al (2013), 88% of phosphorus was removed from wastewater by membrane bioreactor integrated into a continuous flow EBPR Besides
to advantages, this method has some constraints, including external carbon source
Trang 19requirement, complex configuration and operating regimes, more energy and space requirement (Nguyen et al., 2015) The utilization of biological process is not only limited to EBPR but also using algal or aquatic plants Sukacova et al (2015) stated that fixed growth algal bioreactor could eliminate up to 97% phosphorus in wastewater The ability of macrophyte in phosphorus decontamination from wastewater will be discussed thoroughly in other section of thesis
1.3 Constructed wetland for wastewater treatment
1.3.1 Definition and classification of CWs
a Definition
Artificial wetlands are human wetland areas designed to treat wastewater The system of artificial wetlands has low operating and maintenance costs, low energy consumption, does not require high operational and environmentally friendly techniques (Viet et al., 2019)
Components of CWs include substrate, plant, microorganism, animal (earthworm), water (Davis, 1985) The biomass of plants in the system can be used
as animal feed, as a fiber material or as an organic fertilizer However, the land area for construction of artificial wetlands is relatively large, which is an obstacle to the selection of this treatment method, so artificial wetlands are suitable for crowded areas with wide and unfocused land area
b Advantages and limitations
CWs are inexpensive (building, maintenance), simple operation, tolerant to various flow, habitat of many submerged species, wild animals; improve the surroundings, get the community's approval (Davis, 1995)
CWs need to be a large land area, effectively processing inconsistently affected external environmental conditions such as rainfall, droughts, seasons, sensitive to toxic chemicals (Davis, 1995)
c Classification
Trang 20There are many ways to classify CWs which are based on water level, direction
of water (Vymazal, 2008) Based on CWs water levels are classified into categories: Surface flow CWs, Subsurface flow CWs (VF-CWs, HF-CWs), Hybrid / integrated / combined CWs The water level in the
SF system is higher than the substrate surface while it is equal to or lower than the substrate surface in the SSF system (Davis, 1995)
Based on the flow direction of water, SSF is divided into 2 types of horizontal flow (HF) and vertical flow (VF) Water in HFCWs flooded the substrate in the system before exiting through water level control While water in the VFCWs system drains with the intermittent application of water to the system (Stefanakis et al 2014)
d Mechanisms of CWs for P removal
Numerous studies shown that the phosphorus in constructed wetlands is removed mainly by absorption of plants, accumulation of microorganisms, absorption and precipitation of matrix (Lu, 2006) Firstly, the inorganic phosphorus is synthesized ATP, DNA and RNAetc.by uptake and assimilation of plants, and removed from the system through the plants harvested Secondly, phosphorus is necessary to microbial, phosphorus bacteria converted poorly soluble organic phosphorus and phosphorus to dissolved inorganic phosphorus which is conducive to absorption by plants Finally, phosphorusis removed by adsorption of media or ion exchange, the iron, aluminum, calcium compounds will affect the adsorption capacity
of the media, and PAOs excess polyphosphate phosphorus also has a certain role to removal phosphorus Since the constructed wetland have a special aerobic and anaerobic conditions, PAOs can be adsorbed an excess of phosphorus in the aerobic state, and released excess phosphorus in anaerobic conditions, some of phosphorus will spread with the water transport, other will adsorption by the medium, because of the release of phosphorus, adsorption by media in favor of phosphorus in the local where concentration of phosphorus is higher
Trang 21Figure 1.2 P removal in CWs (Hristina Bodin, 2013)
The most important way to remove phosphorus is adsorption and precipitation
of matrix in constructed wetland system, there is less effect for plant adsorption of organic phosphorus, but the absorption of plant is given priority to remove inorganic phosphorus, which may be related to the large plants, like reed plants, need for inorganic phosphorus with a longterm growth.( LI jianbo, 2008) considered that: the adsorption by plants is a major way when at a low concentration of phosphorus, and the absorption by plants appear to be negligible when at a higher concentrations However, the adsorption of medium is limited, that is the absorption effect will be reduced after reaching saturation (Qin and Chen, 2016)
1.3.2 Influential factors and treatment performance
a Influence factors
Substrates (medium)
The substrate is the critical design parameter in CWs and SSF CWs in particular, because it can provide a suitable growing medium for plant and also allow successful movement of wastewater (Kadlec and Wallace, 2009) Moreover, substrate sorption may play the most important role in absorbing various pollutants such as phosphorus (Ju et al., 2014) Selection of suitable substrates to use in CWs for industrial wastewater treatment is an important issue The selection of substrates is determined
in terms of the hydraulic permeability and the capacity of absorbing pollutants Poor
Trang 22hydraulic conductivity would result in clogging of systems, severely decreasing the effectiveness of the system, and low adsorption by substrates could also affect the long-term removal performance of CWs (Wang et al., 2010) Many studies also suggest that substrates such as sand, gravel, and rock are the poor candidate for long-term phosphorus storage, but by contrast, artificial and industrial products with high hydraulic
HRT (Hydraulic retention time)
HRT determines the average contact time of microbial communities with pollutants (Lee et al., 2009) Furthermore, the effect of HRT may differ between CWs depending on the dominant plant species and temperature, as those factors can affect the hydraulic efficiency of wetlands
HLR (Hydrologic loading rate)
HLR is defined as following formular:
𝑞 = 𝑄/𝐴100Where q is defined as the volume per time per unit area (cm day -1); A is the wetland surface area (m2), Q is the flow rate (m3 day-1) Avila et al (2014) also studied the feasibility of hybrid CW systems used for removing emerging organic contaminants, and demonstrated that the removal efficiency for most compounds decreased as the HLR increased (Yan and Xu, 2014; Huang et al., 2000)
Feeding mode
The influent feeding mode is another crucial design factor that can affect the performance of a wetland system (Zhang et al., 2012) Wetlands can be fed in continuous, batch, and intermittent modes These modes affect the oxidation and reduction conditions as well as the oxygen to be transferred and diffused in the system resulting in treatment efficiency modification
Trang 23b P removal efficiency
Table 1.5 P removal by Constructed Wetland
Types of plants Environments Types of
wastewater
Initial concentration (mgP/L)
Removal (%)
Synthetic strom water 4.51 mg/l
6-36
Typha
Lockport dolomite
Sewage wastewater
189 (mg/m2/d) 18 Queenston
shale
400-700 (mg/m2/d) 17-28 Fonthill
sand
105-331 (mg m−2day−1)
HFWs seem to be more effective in P elimination than VFWs because of the longer flowing distance and treatment time (Lüderitz and Gerlach, 2002)
Trang 241.4 Removal phosphorus by plants in the CWs
1.4.1 Classification of plants used in CWs
a Role of plants in CWs
Plants is one of factors will affect the performance of CWs Plants provide an environment for microorganisms to attach and release oxygen from the root system which affect removal efficiency of plants (Jethwa and Bajpai, 2016) Using green plants to reduce pollutant concentration in soil and water was defined as phytoremediation (“Phyto” meaning plants, “remediation” meaning to restore and clean) (Cunningham et al., 1997)
Phytoremediation is more attractive than other technologies thanks to low maintenance, far-reaching, reducing pollution emissions, dust and by-products, preventing soil erosion, surface water flow, permeability, noise reduction, and increased aesthetics, carbon dioxide absorption, improved soil supply after treatment (Champagne, 2007)
In addition, phytoremediation (phytoremediation) is economically viable According to Champagne (2007), this method is at least 40% cheaper than other on-site processing methods and 90% less than ex situ technologies
b Classification of plants used in CWs
Wetland plants can be categorized under four main classes, namely, emergent plants, floating leave macrophytes, submerged plants, and freely floating macrophytes Wu et al (2014)
Macrophytes frequently used in CW treatments include emergent plants, submerged plants, floating leaved plants and free floating plants Although more than
150 macrophyte species have been used in CWs globally, only a limited number of these plant species are very often planted in CWs in reality Emergent species are
Phragmitesspp (Poaceae), Typha spp (Typhaceae), Scirpus spp.(Cyperaceae), Iris spp (Iridaceae), Juncus spp (Juncaceae) and Eleocharis spp.(Spikerush) The most
Trang 25frequently used submerged plants are Hydrilla verticillata, Ceratophyllum demersum, Vallisneria natans, Myriophyllum verticillatum and Potamogeton crispus The floating leaved plants are mainly Nymphaea tetragona, Nymphoides peltata, Trapa bispinosa and Marsilea quadrifolia The free-floating plants are Eichhornia crassipes, Salvinia natans, Hydrocharis dubia and Lemna minor In addition, Ornamental flowering plants, especially Canna indica (Sandoval et al., 2019)
P.australis is the most common species in Asia and Europe while T latifolia
is the most popular plant used in North America The most used plants in Africa are Cyperus papyrus L., P australis and Typha domingensis, Schoenoplectus tabernaemontani In Central and South Americas, Oceania, Palla was recored the most popular wetland plants Regarding types of the wetland plants used subsurface wetland, the second most common plant is Typha spp which is found in Australia,
East Asia, North America, Africa In addition, P.australis is the most popular species
globally (IWA Specialist Group 2000; Scholz 2006; Vymazal 2014)
Common species used in HFCWs are Scirpus (lacustri, acutus, californicus
and validus) Typha (domingensis, glauca, orientalis, latifolia and angustifolia),
Bulrush and comment reeds Phragmites spp is the most popular (Vymazal, 2011) And most of them are herbaceous plants (Vymazal, 2011; Jethwa and Bajpai, 2016)
Table 1.6 Plant species are used to treat swine wastewater
Species Common name Science name Submerged plant
Hydrilla Hydrilla verticilata
Water milfoil Myriophyllum spicatum
Blyxa Blyxa aubertii
Free floating plants
Water hyacinth Eichhornia crassipes
Rootless duckweed Wolfia arrhiga
Water lettuce Pistia stratiotes
Water fern Salvinia spp
Emergent plant Cattails Typha spp
Trang 261.4.2 Removal P mechanisms by plants
a Removal P mechanisms and P removal efficiency of plants
The roots use energy to get P into the tree through the cell membrane Other changes take place in rhizosphere affecting plant P uptake The roots secrete organic acids (citrate and oxalate) which increase the availability of P availability Amount
of excreted organic acid, mycorrhizal fungi, root-zone microorganisms allow a plant
to uptake P more from soil P is removed from the system by harvesting the plants (Brix 1997; Ma et al 2016)
In fact, the CWs with plants are more effective (Vymazal, 2011; Tanner, 2001) Depending on the stage of the system, plants will contribute to various removal effects For immature CWs, the role of plants in eliminating P will not be clearly shown However, the P removal efficiency of the system can still be enhanced by plants through its indirect impact on the treatment conditions of the system (Tanner, 2001)
In addition, phytoremediation (phytoremediation) is economically viable According to Champagne (2007), this method is at least 40% cheaper than other on-site processing methods and 90% less than ex situ technologies
The removal efficiency of P of Typha latifolia, Canna indica, Phragmites
australisdao is 0.06 -74.87%, 0.43 - 4.17, 0.56 - 36.7%, respectively under different
conditions In the same research conditions, the efficiency of removing P of Cladium
mariscus and Iris pseudacorus is 10% and 18% (Jesus et al., 2017) The treatment
efficiency of the dominant species is 37, 53, 61% for Phragmites, Typha, Scirpus
respectively (Vymazal, 2011)
Trang 27Table 1.7 P removal efficiency by plants in CW (Jesus et al., 2017)
Phragmites australis 36.71 1st year harvested Zheng et al (2015)
Phragmites australis 34.19 1st year
unharvested Zheng et al (2015)
Phragmites australis 32.02 2nd year harvested Zheng et al (2015)
Phragmites australis 35.93 2nd year
unharvested Zheng et al (2015)
VSSF
Typha latifolia 35.53 Tang et al (2008)
Typha latifolia 42.54 Tang et al (2008)
Typha latifolia 74.87 Tang et al (2008)
Typha orientalis 14.31 Tang et al (2008)
Phragmites australis 10.76
Scirpus validus 32.27
Iris pseudacorus 34.17 High nutrient
Iris sibirica 13.19 Medium nutrient
Iris sibirica 13.19 Low nutrient
Iris sibirica 13.19
Phragmites Australis 22
Sara G
Abdelhakeem , Samir A Aboulroos
HSSF
Canna indica 0.7 Cui et al (2015)
Canna indica 0.43 Cui et al (2015)
Phragmites australis 0.56 Meng et al (2014)
Arundo donax 0.36 Meng et al (2014)
Typha latifolia 0.06 Meng et al (2014)
SSF
Arachis duranensis 10.4 Van et al (2015)
Cyperus alternifolius 29.8 Van et al (2015) Philodendron
Phalaris arundinacea 45.9 Lower input
Březinová and Vymazal (2015)
Phalaris arundinacea 3.1 Higher input
Březinová and Vymazal (2015)
b Plant selection criteria
Factors affecting the removal efficiency of plants include differences in
Trang 28species, growth conditions, root surface area, oxidizing supply capacity, type of waste water and rate of loading, ability to withstand, absorb pollutants, be resistant to flooding, huge biomass (Jesus et al., 2017)
Fast growth
The rapid growth of plants corresponded with high level of P Therefore, they uptake a significant amounts of nutrient during the period of their growth Harvesting their above parts is the way to remove nutrients from wastewater (Vymazal, 2007)
Tolerant to continuous flooding
Beside the requirement of wetland plants with huge biomass and well developed root system, the tolerance ability to flood affects the nutrient removal efficiency by plants (Almuktar, 2018)
Tolerant to contaminant
Plants can be affected by environment stresses because many pollutants are present in CWs The concentration of influences in wastewater is too high to exceed the capacity of plants which reduces the growth and survival of plants (Surrency, 1993) In addition, high levels of pollutants directly affect the ecosystem of CWs causing inhibition of plant growth, even causing the disappearences of plants (Wu et al., 2015)
The high concentration of pollutants in water resulting in disadvantage of both treatment efficiency and plant survival Plant tolerance to the high concentration of pollutants is another important factor which is considered when selecting them for CWs (Almuktar, 2018)
Ability to accumulate contaminant
Wetlands plants are recognized as an important factor affecting water quality
in CWs Absorption capacity of pollutants of plants contributes to CWs removal efficiency (Wu et al., 2015)
Most common plants used in CWs are weedy plants, which do not bring
Trang 29economic value This study was conducted to find out whether the plants are both economically valuable and treat environmental pollution
Trang 30CHAPTER 2: MATERIALS AND RESEARCH METHODOLOGY
2.1 Research object, scale, and scope
2.1.1 Research objects
In this research, experiments to investigate influential factors on P removal by selected plants and those with CWs were conducted with synthetic wastewater The experiments to search for potential plants were carried out with soil
This study investigated 05 types of plants, including Colocasia gigantean,
Piper lolot, Sauropus androgynous, Cymbopogon citratu, and Ubon paspalum
2.1.2 Research scale & scope
The experiments to evaluate influential factors and those with CWs were implemented at lab-scale The former was done at the laboratory of Master’s Program
in Environmental Engineering (MEE), VNU Vietnam Japan University (VJU), whereas the latter was located on the roof of a residential building in Yen Hoa, Cau Giay, Hanoi
Concerning wastewater quality, this study focused on the removal of ortho phosphate (P-PO43-) of investigated plants Besides, other environmental parameters, such as TSS, pH, BOD5, COD, TN, N-NH4+, TP, P-PO43- were measured to evaluate the composition of real swine wastewater
In relation to plants, in the experiment to screen plants, the attention was paid
to the content of phosphorus in the whole plant as well as in different parts of plants
In experiments to explore influential factors, phosphorus removal rate was used as main indicator
Trang 312.2 Materials, chemicals and equipment
2.2.1 Materials
a Plants
The investigated plant Ubon paspalum was collected in a home garden in Dong Phong commune, Tien Hai district, Thai Binh province whereas Colocasia gigantean, Piper lolot, Sauropus androgynous, and Cymbopogon citrate were gathered in Quang
Bi commune, Chuong My district, Hanoi City Depending on the purpose of experiments, the plants of different ages were utilized
Table 2.1 The list of investigated plants
Common name Science name Picture Location
Lemongrass Cymbopogon citratus
Quang Bi commune, Thinh Da hamlet, Chuong
My district, Hanoi cityPiper lolot Piper sarmentosum
Giant elephant Colocasia gigantea
Trang 32Star gooseberry Sauropus androgynus
Ubon paspalum Ubon paspalum
Dong Phong commune, Tien Hai Distric, Thai Binh province
b Synthetic wastewater
Synthetic wastewater was prepared accordingly the composition and characteristics the real swine wastewater collected from a pig farm, which was located in Luong Xa village, Nam Dien commune, Chuong My district, Ha Noi
c Chemicals
KH2PO4, NH4Cl used in this study were of analytical grade and purchased from ESQ Co., Ltd (Ba Dinh, Hanoi)
2.2.2 Experimental design
a Screening potential plants
This experiment was to search for plants, which have potential for used in phytoremediation or CWs to eliminate phosphorus All investigated plants were grown in the soil They were harvested for determination of phosphorus content at the mature age In this experiment, phosphorus content and biomass growth rate were used for comparison purpose
b Investigating influential factors
All experiments were implemented with simulated swine wastewater First, the stock phosphorus solution (1000 mg P/L) was prepared by dissolving 4.39 g KH2PO4 into 1L of distilled water Then, the P stock solution was diluted 20 times to prepare
Trang 33P working solution (50 mg P/ L) After that, the certain amount of NH4Cl was added
to make the nutrient solution A (50 mg P/ L and 500 mg N/ L) Finally, the A solution was diluted four times to get the background nutrient solution B (12.5 mg P/ L and
125 mg N/ L) The experiments to investigate influential factors were carried out by varying the influential factors while using the same background nutrient solution (except the experiment to investigate effect of initial P concentration)
Effect of initial phosphorus concentration: This experiment was designed to investigate how the plant can grow and uptake phosphorus in the solutions of different phosphorus concentrations This experiment was conducted with synthetic wastewater, which simulated 100%, 50 and 25% of real swine wastewater (P-PO4 50 mg/L, N-NH4-500 mg/L), in term of P and N This experiment included 3 turns, each turn lasted for 9 days, when the phosphorus in the solution was almost removed Cymbopogon citrate and 1.5-month Ubon paspalum were utilized for comparison 45
g of each plant was cultivated in a beaker containing 200 mL of nutrient solution The water sampling was done at the beginning of the experiment and after every 2 days for determination of phosphorus concentration First, the water volume was measured Next, tape water was added for compensation of vaporization After that,
7 mL of water was sampled for P analysis
Effect of pH: This experiment was to evaluate the influence of pH on phosphorus uptake and growth of two plants, namely Cymbopogon citrate and Ubon paspalum It was conducted with aqueous solutions of different pH values (3, 5, 7, 9, and 11) The pH value of the background nutrient solution was adjusted using H2SO4 and NaOH of various concentrations to ensure that the change in volume of the solution was negligible 2-week Cymbopogon citrate and 3-month Ubon paspalum were utilized The plant (60 g) was placed into a beaker containing 200 mL of the background nutrient solution This experiment comprised 7 turns (2 days/ turn) At the start of experiment and after every 2 days, water sample of 7 mL was collected for P concentration and pH analysis Before sampling, the water volume left in the beaker was measured The status of plant was also recorded
Trang 34Effect of plant age: The purpose of this test was to identify at which growth period, the plant is most efficient in phosphorus removal from wastewater This experiment was implemented with the background nutrient solution Ubon paspalum
of 3 kinds of age (1, 1.5, and 3 months) and Cymbopogon citrate of 2 kinds of age (baby and mature) were used This experiment lasted for 7 turns (2 days/ turn) The water sampling was implemented the same as that for experiment to investigate the effect of pH
Effect of plant density: The experiment was to determine the best plant density for plant growth and phosphorus accumulation This experiment was carried out in both soil and auqeous solutions For hydroponic experiments, three kinds of plant density, such as 1, 3, and 5 plant(s)/ beaker were applied The water sampling was done in a similar procedure to that of experiments for pH and plant age For soil experiment, it was conducted only with Ubon paspalum with 3 types of plant density (1, 3, and 5 plants/ trough) The soil was fertilized 3 times/ week, 2 months after planting, the Ubon paspalum was harvested for determination of both P content and biomass growth
Effect of water level: This experiment was to evaluate the ability of plant to adapt with different water levels It was done with 3 kinds of water levels (2, 5, and
8 cm) The water sampling frequency was the same as that of the experiment on pH, plant age, and density
c Trial application of the selected plant in CWs
CWs experiment setting up: The experiment was designed to include 4 treatment systems in parallel In the systems 1&3, the horizontal flow constructed wetland was followed by the adsorption unit The wastewater was stored in a big sink, then pumped into the CWs using 4 peristaltic pump (HV-77200-50, Masterflex Cole-Parmer, USA) To ensure that the effluent quality meets the requirement of discharge standard, after going through CWs, the wastewater was pumped into adsorption unit The systems 2&4 did not include adsorption units and used as the control systems
Trang 35Figure 2.1 Scheme of horizontal constructed wetland
(at the start of experiment) Dimension and filter materials: The four CWs tanks were made of stainless steel, in rectangle shape and have the same dimension (L x W x H = 68.5 cm x 33
cm x 42 cm The efficient volume of each tank was 0.095 m3
The filter media including sand, WHC, yellow sand, and gravel were arranged into 3 layers with descending particle size from bottom to top of the tank The bottom layer, which was made of 5-10 mm gravel, had the height of 1.5 cm The upper layer, which was made of 0.25-0.5 mm sand, had the length of 13 cm For the treatment systems 1&2, the middle layer, which was 27.5 cm in height, was made of 2 particle sizes (1.4 -2.0 mm and 2.0 - 4.0 mm) For the systems 3&4, the filter material in the middle layer was made of yellow sand 0.5-0.85 mm rather than WHC
Trang 36Tank 1+ Tank 2 Tank 3+ Tank 4 Adsorption unit
Figure 2.2 The structure of filter media in CWs and adsorption units
Plants
The plant used in the CWs experiment was Ubon paspalum This plant was
selected because of high biomass, fast growth, deep roots, good tolerance to flooding, high uptake of nutrient, high economic value To the best of our knowledge, this is the first time this plant has been used in CWs for phosphorous decontamination
The plant was grown in soil of a home garden It was cut off leaves to mitigate the water evaporation The stem with the height of 25 cm was put into a bucket of tap water for 1 week in the cool place with daylight When the new leaves reached the height of 10 cm, the water in the bucket was replaced by the background nutrient solution and kept for another 1 week for adaptation After that, the plants were transferred into CWs It took around 2 weeks for CWs plants to stabilize and grow well
Wastewater characteristics
This experiment used the background nutrient solution, which simulated 25% real swine wastewater in terms of P and N contents (12.5 mg P/ L, and 125 mg N/ L) Every two days, waster sampling was implemented at the inlet and the outlet of all four CWs and after two adsorption units for P and pH measurement
Operational parameters
Trang 37The treatment systems were operated with hydraulic loading rate (HLR) of 0.032 and 0.027 m3/m2/d for the treatment systems 1&2 and the treatment system 3&4, respectively The hydraulic retention time (HRT) of the CWs, adsorption unit 1 and adsorption unit 3 was 5.4, 0.16 and 0.19 d, respectively The HRT of the hybrid treatment system 1 (CW1 + adsorption unit 1) and the hybrid treatment system 2 (CW3 + adsorption unit 2) was 5.5 and 5.59 d, respectively
2.2.3 Plant sample preparation and P analysis
Figure 2.3 Plant sample preparation and analysis
Plant sample preparation: First, plant samples were well rinsed with double distilled water, dried in the room with the air conditioner (27 0C and high fan speed) for 15 min Next, the plant was cut into different parts (stem, leaves, and roots) and then measured the fresh weight Then, the cut plants were placed in the Thermo Scientific oven at 70 0C for 48 h, and cooled down to the room temperature After that, the dried plant samples were measured to determine the dry weight The dried samples were ground into powder using the plant crusher and coffee grinder The powdered plants were kept in a tight glass bottle for P analysis
Plant sample digestion: The plant samples were digested according to Vietnam Standard TCVN 8551:2010 using heating digester (DK6) Accordingly, 0.5 g of the plant sample was mixed with 10 mL of the mixture of HClO4: HNO3 (1: 2 in volume), kept overnight and then digested in DK6 for 5 h at different temperatures
P analysis: The wastewater and plant samples (after digestion) were measured
to identify the concentration of phosphorus according to Method 365.3 of EPA, using UV-VIS S2150 Spectrophotometer