Aquaculture, the farming of aquatic animals and plants, is an important component of global food production, which supplies a nutritious protein source for millions of people. Interest in improving the sustainability of aquaculture has led to the development of aquaponics in which fish production is combined with plant production to create zero-discharge systems. A need for more fundamental science and engineering research on marine aquaculture and growing interest in production of halophytes motivated this novel research on marine aquaponics. One objective was to evaluate the growth and nutrient removal capacity of halophytes in marine aquaponics. Bench-scale studies were conducted to determine the best methodology to grow the halophytes sea purslane (Sesuvium portulacastrum) and saltwort (Batis maritima). The results indicated these species were important for nitrogen removal and function well under varying conditions of flow rate, species, or plant density. A prototype commercial-scale marine aquaponic system was evaluated through regular collection of water quality and plant growth data over a 9 month period. The system had a total volume of 50 m3 and contained: a swirl separator, uplfow media filter, a moving bed bioreactor, 61.4 m2 of hydroponic growing area, and a sand filter. Water quality parameters measured included: total ammonia nitrogen (TAN), nitrite (NO2-), nitrate (NO3-), total nitrogen (TN), total phosphorus (TP), chemical oxygen demand (COD), total suspended solids (TSS), and volatile suspended solids (VSS). TAN and nitrite concentrations in the fish tank effluent ranged from 0.04 to 2.42 mg/L TAN and 0.07 to 14.7 mg/L NO2--N, respectively. Nitrate concentrations increased to a maximum of 120 ± 5.7 mg/L NO3--N during the first 119 days of operation. To provide greater control over nitrate concentrations, the sand filter was converted into a downflow submerged packed bed biofilter. This reduced concentrations to a mean of 27.5 ± 13.7 mg/L NO3--N during the last 3 months. Dried plant samples were analyzed for nitrogen and phosphorus content. Nutrient uptake by plants ranged from 0.06 to 0.87 g N/m2/d and 0.01 to 0.14 g P/m2/d. It was estimated 0.55 kg/m2 of plant biomass could be harvested every 28 days. Red drum (Sciaenops ocellatus) were initially stocked at an average weight of 0.047 kg and grew to a harvestable size of 0.91 kg in approximately 12 months. A mass balance indicated that plants contributed to less than 10% of nitrogen and phosphorus removal and passive denitrification was the dominant nitrogen removal process. The second objective was to evaluate the environmental impact of aquaponics through life cycle assessment (LCA). LCAs were completed on freshwater aquaponic systems at commercial- and residential-scales. The system expansion method was used address co-production of 1 ton live-weight fish, recovered solids, plants, and water treatment. The results indicated that aquaponics contributed to significant water savings; however, aquaponics is subject to trade-offs from high energy use and the addition of industrial fish feeds. The methodology developed for freshwater aquaponics was applied to the prototype commercial-scale marine aquaponic system and was compared with two alternative scenarios of maximized plant production and a denitrification reactor with no plant production. The results indicated that a system with a denitrification reactor had the lowest environmental impact. Alternatively in the system with maximized plant production, the use of renewable energy sources would reduce the environmental impact and would contribute to greater water savings, while realizing the economic benefits of dual products. This is the first study to complete an in-depth evaluation of a commercial-scale marine aquaponic system and to evaluate aquaponics using LCA while accounting for the potential environmental offsets of multiple co-products.

Anaerobic digestion (AD) has been shown to be an effective technique for energy recovery and stabilization of livestock wastes, municipal sludges and industrial wastewaters. However, further treatment is required to remove nitrogen from AD effluents to avoid detriments to surface and ground waters. The high free ammonia (FA) concentrations present in AD effluents can inhibit nitrification processes in conventional biological nitrogen removal (BNR) systems. The overall goal of this research was to develop a process for removal of nitrogen from AD swine waste (ADSW) effluent. The proposed solution was to incorporate particulate chabazite, which has a high cation exchange capacity, into a sequencing batch reactor (SBR) to adsorb ammonium and therefore ease nitrification inhibition. The process developed is called a chabazite-SBR. Three research questions were used to guide this research. First question (Chapter 3): How does chabazite pretreatment with groundwater (GW) affect the kinetics and cation exchange capacity during ammonium (NH4+) uptake? Kinetics and isotherm batch tests were performed with GW pretreated chabazite. In addition, sodium chloride (NaCl), and deionized water (DI) pretreated chabazite was included for comparison because these are typically used pretreatment methods. The Ion Exchange (IX) isotherm model was used to calculate the cation exchange capacity and the pseudo-first and film diffusion kinetics models were applied to quantify the effect of the pretreatment on the reaction rate. Results showed that the exchange capacity was slightly higher for GW pretreated chabazite compared with the other common pretreatment strategies; however, the enhancement was not significantly different. The kinetics of NH4+ uptake during the first four hours of contact was significantly improved by GW pretreatment when compared with other common pretreatment strategies. This was caused by an enhancement in film diffusion mechanisms. The findings of this first part of the research were important because it was shown that NaCl pretreatment is not needed to improve the kinetics and cation exchange capacity of chabazite. Second question (Chapter 4): How does addition of chabazite to ADSW centrate affect nitrification rates? Nitrification batch test with varying NH4+ concentrations were performed to identify the inhibitory NH4+ concentration. Additional nitrification batch tests treating real and synthetic waste with initial NH4+ concentration of 1,000 mg-N L-1 with added zeolite were performed. For the mixed liquor tested in this study, NH4+ concentrations must be maintained below 200 mg-N L-1 to relieve nitrification inhibition. Treatment of ADSW centrate requires a chabazite dose of 150 g L-1 to ease FA inhibition of nitrification. The rate of nitrification increased, by approximately a factor of 3, when chabazite was added to a batch reactor treating high NH4+ strength wastewater. However, Na+ release from the chabazite also plays a role in nitrification inhibition. The findings of this part of the research showed the potential for using chabazite for overcoming FA inhibition of nitrification during treatment of high NH4+ strength wastewater. Third question (Chapter 5): How effective is the chabazite-SBR in removing total nitrogen concentrations from ADSW centrate? A chabazite-SBR was operated for 40 weeks (cycles) to study the TN removal efficiency with varying carbon source. The efficiency of IX was also monitored over time. The chabazite-SBR process achieved stable TN removal from ADSW centrate during the 40 weeks of operation. Simultaneous nitrification-denitrification reduced chemical input requirements. Addition of an external organic carbon source at a rate of 3.2 g-COD g-N-1 resulted in maximum TN removal. An overall TN removal efficiency of 84% was achieved, with specific nitrification and denitrification rates of 0.43 and 1.49 mg-N g-VSS-1 hr-1, respectively. The IX stage of the chabazite-SBR was able to reduce FA concentrations to below the inhibitory level for nitrification inhibition over 40 chabazite-SBR cycles with no loss in IX efficiency over time and no fresh zeolite added to the reactor.

This research evaluates two different Biological Nitrogen Removal (BNR) systems for enhanced nitrogen removal in decentralized wastewater treatment. The first study evaluated the performance of Hybrid Adsorption and Biological Treatment Systems (HABiTS) at the pilot scale with and without stage 1 effluent recirculation. HABiTS is a system developed at the bench scale in our laboratory and was designed for enhanced BNR under transient loading conditions. It consists of two stages; an ion exchange (IX) onto clinoptilolite media coupled with biological nitrification in the aerobic nitrification stage 1 and a Tire-Sulfur Adsorption Denitrification (T-SHAD) system in the anoxic denitrification stage 2. The T-SHAD process incorporates NO3- adsorption onto tire chips and Sulfur Oxidizing Denitrification (SOD) using elemental sulfur as the electron donor for NO3- reduction. Previous bench scale studies evaluated HABiTS performance under transient loadings and found significantly higher removal of nitrogen with the incorporation of adsorptive media in stage 1 and 2 compared with controls (80% compared to 73%) under transient loading conditions. In this study, we hypothesize that a HABiTS system with effluent recirculation in nitrification stage 1 may enhance nitrogen removal performance compared to that without recirculation. The following were the expected advantages of Stage 1 effluent recirculation for enhanced nitrogen removal: 1) Pre-denitrification driven by the mixture of nitrified effluent from stage 1 with high concentrations of biochemical oxygen demand (BOD) septic tank effluent. 2) Moisture maintenance in stage 1 for enhanced biofilm growth. 3) Increased mass transfer of substrates to the biofilm in stage 1. 4) Decreased ratio of BOD to Total Kjeldahl Nitrogen (TKN) in the influent of stage 1. Two side-by-side systems were run with the same media composition and fed by the same septic tank. One had a nitrification stage 1 effluent recirculation component (R-system), which operated at a 7:1 stage 1 effluent recirculation ratio for the first 49 days of the study and at 3:1 beginning on day 50 and one was operated under forward flow only conditions (FF-system). The R system removed a higher percentage of TIN (35.4%) in nitrification stage 1 compared to FF (28.8%) and had an overall TIN removal efficiency of 88.8% compared to 54.6% in FF system. As complete denitrification was observed in stage 2 throughout the study, overall removal was dependent on nitrification efficiency, and R-1 had a significantly higher NH4+ removal (87%) compared to FF-1 (70%). Alkalinity concentrations remained constant from stage 1 to stage 2, indicating that some heterotrophic denitrification was occurring along with SOD, as high amounts of sCOD leached from the tire chips in the beginning of the study, reaching sCOD concentrations of 120-160 mg L-1 then decreasing after day 10 of operation of stage 2. Sulfate concentrations from stage 2 for each side were low until the last 10 days of the study, with an average of 16.43 ± 11.36 mg L-1 SO42--S from R-2 and an average of 16.80 ± 7.98 SO42--S for FF-2 for the duration of the study, however at the end of the study when forward flow rates increased, SO42--S concentrations increased to 32 mg L-1 for R-2 and 40 mg L-1 for FF-2. Similar performance was observed in the FF system as the bench scale reactor tests. The second part of the research focused on the findings from a study of a Particulate Pyrite Autotrophic Denitrification (PPAD) process that uses pyrite as the electron donor and nitrate as the terminal electron acceptor in upflow packed bed bioreactors. The advantages of using pyrite as an electron donor for denitrification include less sulfate production and lower alkalinity requirements compared with SOD. The low alkalinity consumption of the PPAD process led to comparison of PPAD performance with and without oyster shell addition. Two columns were operated side-by-side, one packed with pyrite and sand only (P+S), while another one was packed with pyrite, sand and oyster shell (P+S+OS). Sand was used as a nonreactive biofilm carrier in the columns. My contribution to this research was to carry out Scanning Electron Microscopy-Energy-Dispersive X-Ray Spectroscopy (SEM-EDS) analysis to support the hypothesis that oyster shell contributes to nitrogen removal because it has a high capacity for biofilm attachment. SEM analysis showed that oyster shell has a rough surface, supported by its high specific surface area, and that there was more biofilm attached to oyster shell than pyrite or sand in the influent to the column. EDS results showed a decrease in atomic percentages for pyrite sulfur in the effluent of both columns (59.91% ± 0.10% to 53.94% ± 0.37% in P+S+OS column and to 57.61% ± 4.21% in P+S column). This finding indicated that sulfur was oxidized more than iron and/or the accumulation of iron species on the pyrite surface and supports the coupling of NO3- reduction with pyrite oxidation.

Denitrification removes large amounts of reactive nitrogen (N) from ecosystems via reduction of nitrate to dinitrogen gas. In aquatic ecosystems, the influences of terrestrial and aquatic sources of organic matter (OM) on denitrification are potentially complex. Terrestrially-derived OM is often less labile than autochthonous OM; it may inhibit denitrification directly via biochemical mechanisms; and it may indirectly inhibit denitrification by reducing light availability to—and thus OM exudation by—aquatic primary producers. Using a natural dissolved OM gradient among rivers of northern Florida, I investigated these mechanisms using laboratory denitrification assays subjected to factorial amendments of NO3- and dextrose, humic acid dosing, and cross-incubations of sediments and water. Results indicated that C-limitation increased with DOC concentrations, consistent with the indirect inhibition hypothesis. Blackwater neither depressed nor stimulated denitrification rates, indicating that this DOC neither directly inhibits nor acts as a usable OM source for denitrifiers.

<p>Variations in stable isotope abundances of nitrogen (δ¹⁵N) and oxygen (δ¹⁸O) of nitrate are a useful tool for determining sources of nitrate as well as understanding the transformations of nitrogen within soil (Chapter 2). Various sources of nitrate are known to display distinctive isotopic compositions, while nitrogen transformation processes fractionate both N and O isotopes and can reveal the reaction pathways of nitrogen compounds. However, to fully understand the δ¹⁵N and δ¹⁸O values of nitrate sources, we must understand the chemistry and the isotopic fractionations that occur during inorganic and biochemical reactions. Among all N cycle processes, nitrification and denitrification displayed some of the largest and most variable isotope enrichment factors, ranging from -35 to 0‰ for nitrification, and -40 to -5‰ for denitrification. In this dissertation, I will first characterize the isotopic enrichment factors of ¹⁵N during nitrification and denitrification in a Midwestern agricultural soil, two important microbial processes in the soil nitrogen cycle. Nitrification incubations found that a large enrichment factor of -25.5‰ occurs during nitrification NH₄⁺ è NO₃^-, which agrees well with previous studies (Chapter 3). Additionally, oxygen isotopic exchange that occurs between nitrite and water during nitrification was also quantified and found that 82% of oxygen in NO₃^- are derived from H₂O, much greater than the 66% predicted by the biochemical steps of nitrification. The isotopic enrichment that occurs during denitrification was assessed by measuring the change in δ¹⁵N as the reactant NO₃^- was reduced to N₂ gas (Chapter 4). The incubations and kinetic models showed that denitrification can causes large isotopic enrichment in the δ¹⁵N of remaining NO₃^-. The enrichment factor for NO₂^- è gaseous N was -9.1‰, while the enrichment factors for NO₃^- è NO₂^- were between -17 to -10‰, both of which were within the range of values report in literature. The results demonstrated that nitrification and denitrification caused large isotope fractionation and can alter the presumed δ¹⁵N and δ¹⁸O values of nitrate sources, potentially leading to incorrect apportionment of nitrate sources.</p> <p>The results of the denitrification incubation experiments were applied to a field study, where the measured enrichment factor was utilized to quantify loss of N by field-scale denitrification (Chapter 5). Field-based estimates of total denitrification have long been a challenge and only limited success has been found using N mass balance, N₂O gas flux, or isotope labeling techniques. Here, the flux of nitrate and chloride from tile drain discharge from a small field was determined by measuring both dissolved ions (ion chromatography) and monitoring water discharge. The δ¹⁵N and δ¹⁸O of tile nitrate was also measured at a high temporal resolution. Fluxes of all N inputs, which included N wet and dry deposition, fertilizer application, and soil mineralization were determined. The d¹⁵N and d¹⁸O values of these nitrate sources was also determined. Using this data, I first detected shifts in δ¹⁵N and δ¹⁸O values in the tile drain nitrate, which indicated variable amounts of denitrification. Next, a Rayleigh distillation model was used to determine the fraction of NO₃^- loss by field scale denitrification. This natural abundance isotope method was able to account for the spatial and temporal variability of denitrification by integrating it across the field scale. Overall, I found only 3.3% of applied N was denitrified. Furthermore, this study emphasized the importance of complementary information (e.g. soil moisture, soil temperature, precipitation, isotopic composition of H₂O, etc.), and the evidence it can provide to nitrogen inputs and processes within the soil.</p>

No description available.

Explosives used in the mining industry release nitrate into the environment, causing concerns for the water quality in local river-systems. One way of reducing the nitrate loading into the environment is through a woodchip bioreactor. Water is passed through the bioreactor, where denitrifying microbial communities use the organic carbon from the substrate for energy, together with the nitrate. The efficiency of the denitrification process depends on various factors, including the type of carbon source selected and the temperature. To determine a suitable organic substrate to use in colder environments, column experiments were conducted, comparing different woodchip types. Three columns contained woodchips from pine, spruce and birch. In the fourth column, barley wheat was mixed with pine woodchips. An influent solution was pumped into the columns contained 50 mg/L nitrate-nitrogen. The effluent water was sampled and analysed twice per week for nitrate, nitrite and ammonium concentrations. The pH and alkalinity were analysed weekly to determine that denitrification was taking place. Three column conditions were tested. During the initial period, the columns were kept in 21 °C with a hydraulic residence time (HRT) of 6.3 days. In the following period, the columns were refrigerated at a temperature of 5°C. During the final period, the HRT was lowered to 3.2 days. After a 106-day runtime, it could be concluded that pine woodchips were the most effective substrate for denitrification in 5 °C temperature. The column with pine woodchips removed nitrate efficiently and produced the least amount of by-products and released DOC with a short HRT. The pine woodchips and barley straw column had high nitrite accumulation, and the nitrate removal rate in the birch and spruce woodchip columns was low in 5 °C conditions. / Sprängmedel som används inom gruvindustrin släpper ut nitrat i miljön, vilket kan leda till problem med vattenkvaliteten i lokala vattensystem. Ett sätt att reducera mängden nitrat som släpps ut är genom en bioreaktor med träflis. Vatten passeras genom bioreaktorn, där denitrifierande microbakteriella grupper använder det organiska kolet från substratet för energi, tillsammans med nitratet. Effektiviteten av den denitrifierande processen beror på flertalet faktorer, däribland vilken sorts kolkälla som valts ut och vilken temperatur bioreaktorn håller. För att identifiera ett bra organiskt substrat att använda i kallt klimat genomfördes ett kolumnexperiment som jämförde olika sorters träflis. Tre kolonner innehöll träflis från tall, gran och björk. I en fjärde kolonn blandades kornhalm med träflis från tall. En lösning med koncentrationen 50 mg/L kväve i form av nitrat pumpades in i kolonnerna. Utloppsvattnet från de fyra kolonnerna analyserades två gånger per vecka för koncentration av nitrat, nitrit och ammonium. pH och alkalinitet analyserades varje vecka för att se att denitrifikation skedde. Tre olika förutsättningar testades i kolonnerna. I den första perioden hölls kolonnerna i 21 °C med en hydraulisk uppehållstid på 6,3 dagar. I den följande perioden kyldes kolonnerna till 5 °C. I den sista perioden sänktes uppehållstiden till 3,2 dagar. Efter 106 dagar gick det att fastställa att tall-träflisen var det mest effektiva substratet för denitrifikation i 5 °C. Kolonnen med träflis från tall sänkte nitrathalten i vattnet och producerade minst biprodukter, samt frigjorde organiskt kol även vid kort uppehållstid. Kolonnen med tallflis och kornhalm ackumulerade mycket nitrit, och kolonnerna med träflis från björk och gran hade låga nivåer av nitrat-rening när temperaturen sänktes till 5 °C.

This thesis concerns with control calculation of steam boiler. The work is divided into several parts. In the individual parts are executed stechiometry calculations, the enthalpy of flue gas and power of the heat exchange surfaces. Based on the results it is proposed location of the SCR.

abstract: The potential of using bio-geo-chemical processes for applications in geotechnical engineering has been widely explored in order to overcome the limitation of traditional ground improvement techniques. Biomineralization via urea hydrolysis, referred to as Microbial or Enzymatic Induced Carbonate Precipitation (MICP/EICP), has been shown to increase soil strength by stimulating precipitation of calcium carbonate minerals, bonding soil particles and filling the pores. Microbial Induced Desaturation and Precipitation (MIDP) via denitrification has also been studied for its potential to stabilize soils through mineral precipitation, but also through production of biogas, which can mitigate earthquake induced liquefaction by desaturation of the soil. Empirical relationships have been established, which relate the amount of products of these biochemical processes to the engineering properties of treated soils. However, these engineering properties may vary significantly depending on the biomineral and biogas formation mechanism and distribution patterns at pore-scale. This research focused on the pore-scale characterization of biomineral and biogas formations in porous media. The pore-scale characteristics of calcium carbonate precipitation via EICP and biogenic gas formation via MIDP were explored by visual observation in a transparent porous media using a microfluidic chip. For this purpose, an imaging system was designed and image processing algorithms were developed to analyze the experimental images and detect the nucleation and growth of precipitated minerals and formation and migration mechanisms of gas bubbles within the microfluidic chip. Statistical analysis was performed based on the processed images to assess the evolution of biomineral size distribution, the number of precipitated minerals and the porosity reduction in time. The resulting images from the biomineralization study were used in a numerical simulation to investigate the relation between the mineral distribution, porosity-permeability relationships and process efficiency. By comparing biogenic gas production with abiotic gas production experiments, it was found that the gas formation significantly affects the gas distribution and resulting degree of saturation. The experimental results and image analysis provide insight in the kinetics of the precipitation and gas formation processes and their resulting distribution and related engineering properties. / Dissertation/Thesis / Doctoral Dissertation Civil, Environmental and Sustainable Engineering 2019

In der vorliegenden Arbeit werden Ergebnisse von Untersuchungen zur Denitrifikation in Grundwasserleitern vorgestellt. Dabei werden drei pleistozäne norddeutsche Grundwasser-leiter betrachtet. Grundlage der Untersuchungen im Labor bilden Sedimentproben, die aus Bohrungen mit einer maximalen Teufe von 60 m u GOK, gewonnen wurden. Der Gehalt an organischem Kohlenstoff und Sulfidschwefel erlaubt den Ablauf einer chemo-organotrophen und chemo-lithotrophen Denitrifikation. Die Laborversuche zeigen eine maximale Nitratelimi-nation von 0,2 mg∙kg-1∙d-1 N, hauptsächlich infolge chemo-lithotropher Denitrification. Für einige Sedimentproben wurde eine Sorption von Nitrat mit maximal 0,85 mg∙kg-1N nachge-wiesen. Im Feld wurde der Ablauf einer Denitrifikation anhand von N2- und Ar-Messungen nachgewiesen. Die Größenordnung der Denitrifikation im Aquifer wurde außerdem mit Ein-bohrloch-Tracerversuchen (Push&amp;amp;Pull-Tests) bestimmt. Diese Tracerversuche wurden in Teufen durchgeführt, aus denen Sedimentproben für Laboruntersuchungen gewonnen wor-den waren. Die Labor- und Tracerversuche lieferten vergleichbare Ergebnisse. Weiterhin wird ein Weg gezeigt, wie Punktinformationen zum N-Umsatz mittels stochastischer Simula-tion in die Fläche übertragen werden und somit in numerische Transportmodelle eingebun-den werden können. / This thesis shows results from investigations about denitrification, a possibility is shown in aquifers. The investigation areas are three pleistocene aquifers in northern Germany. The studies in laboratory are based on samples of drillings until a depth of 60 m. The content of organic carbon and sulphides allows both chemo-organotrophic and chem-lithotrophic deni-trification. The maximum of nitrate, that was eliminated, mainly by chemo-lithotrophic denitri-fication, was 0.2 mg N per kg sediment and day. In some samples a sorption of nitrate was detected at a maximum of 0.85 mg N per kg sediment. Denitrification in situ was detected by measurements of the gases N2 and Ar at some measurement wells. Denitrification in situ was also quantified by push&amp;amp;pull-tests (single-well-tracer tests). Push&amp;amp;pull-tests as well as labo-ratory studies were carried out with sediment samples of respective measurement-wells. Similar results were found for push&amp;amp;pull tests and batchtests. Further, a possibility is shown how point-data concerning nitrate-metabolism can be transferred into two dimensions by sto-chastic simulation. Thus one can implement point-data into numerical transport-models.