Gotowe bibliografie tematyczne / Sewage – Purification – Nitrogen removal

Gotowa bibliografia na temat „Sewage – Purification – Nitrogen removal”

Autor: Grafiati
Data publikacji: 4 czerwca 2021
Data aktualizacji: 31 stycznia 2023

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Artykuły w czasopismach na temat "Sewage – Purification – Nitrogen removal"

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Kalenik, Marek. "Badania modelowe skuteczności oczyszczania ścieków w piasku średnim z warstwą wspomagającą z hydro-antracytu". Przegląd Naukowy Inżynieria i Kształtowanie Środowiska 28, nr 2 (10.07.2019): 257–67. http://dx.doi.org/10.22630/pniks.2019.28.2.24.

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The model investigations of sewage purification were carried out in a medium sand bed with an assisting hydro-anthracite layer with thickness of 0.10 and 0.20 m. It has been observed that the effectiveness of sewage purification related to basic qualitative parameters (total suspended solids – TSS, BOD5, COD, total nitrogen, total phosphorus) is in accordance with the Polish standards on sewage disposal into grounds and surface water. It has been stated that the medium sand soil bed with the 0.20-meter thick assisting hydro-anthracite layer shows higher effectiveness of sewage purification than the 0.10 m thick assisting layer. This application in the medium sand soil bed increased the removal efficiency regarding TSS by 3.1%, total nitrogen by 29.4%, ammonia nitrogen by 1.2% and total phosphorus by 23.0%, and reduction efficiency regarding BOD5 by 1.5% and COD by 11.3% with relation to the 0.10-meter thick assisting hydro-anthracite layer (all percentages – in average). The investigations confirm that the hydro-anthracite with the granulation of 1.8–2.5 mm can be used to assist in removal of nitrogen and phosphorus compounds from sewages
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Ma, Chao, Hui Ding, Yi Chao Sun i Xiao Wen Deng. "Removal of Nutrients from Saline Waste Sewage with Different Vertical-Flow Constructed Wetland Substrates". Advanced Materials Research 356-360 (październik 2011): 1189–94. http://dx.doi.org/10.4028/www.scientific.net/amr.356-360.1189.

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In order to find the best substrates of constructed wetlands for saline waste sewage treatment, Bio-ceramic, quartz sand, zeolite and medical stone were used as filtering media for saline sewage treatment with proper proportion microbe, isolated from the sewage of the Wuqing sewage treatment plant. In this paper, the purification of the vertical-flow constructed wetlands (VFCWs) with different substrates was studied, and the component of the nitrogen in the influent and effluent was analyzed. The concentrations of chemical oxygen demand (COD), ammonia (NH4+-N), total phosphorus (TP), total nitrogen (TN) and the salinity of the influent during the experimental period were 150mg•L-1, 36 mg•L-1, 8mg•L-1, 36mg•L-1and 1.6%. Under the condition that the hydraulic loading rate was 0.25m•d-1, the average removal efficiency of COD, TP and TN were obtained about 68.81%, 32.01% and 20.72 %, respectively with Bio-ceramic; 61.92%, 31.75% and 34.33%, respectively with quartz sands; 69.47%, 35.44% and 55.28% , respectively with zeolite; and 64.77%, 32.63% and 34.72%, respectively with medical stone. This result proves that comprehensive purification of the system with zeolite is the best.
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Xing, Chuanjie, Xiangxi Xu, Zhenghe Xu, Rongzhen Wang i Lirong Xu. "Study on the Decontamination Effect of Biochar-Constructed Wetland under Different Hydraulic Conditions". Water 13, nr 7 (25.03.2021): 893. http://dx.doi.org/10.3390/w13070893.

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To explore the purification effect of biochar-constructed wetlands on rural domestic sewage, six types of biochar-constructed wetlands were constructed for experiments. Under different hydraulic conditions, the removal effects of each biochar-constructed wetland on chemical oxygen demand, ammonia nitrogen, total nitrogen, and total phosphorus in sewage were analyzed. The results showed that the removal rates of the four types of pollutants in each biochar-constructed wetland first increased and then decreased with the increase in hydraulic retention time, and the optimal hydraulic retention time range was 36–48 h. The highest removal rates of chemical oxygen demand, ammonia nitrogen, total nitrogen, and total phosphorus in the wetland were 97.34 ± 0.84%, 95.44 ± 1.29%, 98.95 ± 0.52%, and 97.78 ± 0.91%, respectively. The chemical oxygen demand (COD) removal rate of each biochar-constructed wetland increased first, then decreased with the increase in hydraulic load, and the optimal hydraulic load was 10 cm/d. The removal efficiency of ammonia nitrogen, total nitrogen, and total phosphorus of each biochar-constructed wetland gradually weakened with the increase in hydraulic load, and the optimal hydraulic load range was between 5 and 10 cm/d. Under these conditions, the highest removal rates of chemical oxygen demand, ammonia nitrogen, total nitrogen, and total phosphorus in the wetland were 92.15 ± 2.39%, 98.32 ± 0.48%, 96.69 ± 1.26%, and 92.62 ± 2.92%, respectively. Coconut shell and shell-constructed wetlands with the highest proportion of biochar in the matrix have the best removal effect on pollutants under different hydraulic conditions, and the wastewater purification effect is stronger, indicating that the addition of biochar is helpful for the removal of pollutants in constructed wetlands.
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Zhang, Dong Xia, Qi Liu i Yong Ming Zhang. "Treating Effect of Potassium Ferrate to Aquaculture Recirculating Water". Advanced Materials Research 1004-1005 (sierpień 2014): 1005–7. http://dx.doi.org/10.4028/www.scientific.net/amr.1004-1005.1005.

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Aquaculture waste water was a major sewage resource, and recirculating aquaculture is an important mode of aquaculture development. Potassium ferrate is a novel sewage treatment agent and the use of potassium ferrate as a aquaculture recirculating water purification agents had a very important significance in the theoretical and practical application. When the amount of potassium ferrate is 8mg / L, the removal rate of the total number of colonies is 98.8%, the removal rate of COD is 92.16%, 98.78%, and sulfide is 98.42%. For the total amount of ammonia and nitrite also has a certain effect, when the amount of potassium ferrate is 12mg / L, the nitrite removal rate was 44.61%, total ammonia nitrogen removal rate was 23.61%.
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Shui, Yong Hong, Jian Li, Xil Ning Feng, Xue Jun Jiang, Qiao Qiao Li i Ai She Shui. "Nitrogen Removal along Vertical direction by Plant Biological Membrane System". Advanced Materials Research 955-959 (czerwiec 2014): 2463–68. http://dx.doi.org/10.4028/www.scientific.net/amr.955-959.2463.

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Based on the equipment of integrated constructed wetlands (ICWs) with independent intellectual property rights. Plant biological membrane system (PBMS) was constructed to purify nitrogen of sanitary sewage. PBMS includes palm silk, non-woven and floating plant (Trifolium repens L.). Total nitrogen (TN), ammonia nitrogen (NH3-N) was investigated to evaluate the effects of the layered purification and resistance to the outside impact. The results showed that layered purification occurred along the flowing vertical direction. The average removal rate of TN, NH3-N and total dissolved solids was 65.6%, 60.7% and 38.7%, respectively. The TN and NH3-N removal load of the lower, middle and upper layer were 1.0, 0.8, 0.7g/ (m2.d) and 0.8, 0.8, 0.3g/ (m2.d), respectively. The higher concentration of inflow the stronger resists impact load capability. The TN and NH3-N average removal load of the lower, middle and upper layer were 4.1, 1.88, 1.57 times and 3.13, 1.25, 1 time than those of the stable phase, respectively.
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Tsytlishvili, Kateryna. "Experimental Investigations of Removal of Phosphorus Compounds from Wastewater under Biological Purification". Key Engineering Materials 925 (11.07.2022): 159–67. http://dx.doi.org/10.4028/p-p0fnoc.

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Today, most surface waters of Ukraine are eutrophied due to the entry into water bodies of a significant amount of nutrients – compounds of carbon, nitrogen and phosphorus. Nitrogen and phosphorus enter water bodies with wastewater, sewage from agricultural lands and livestock farms, as well as with precipitation, due to the decomposition of water biomass, aquatic vegetation and zoocenoses. In the presence of free carbon dioxide (the concentration of which depends on bicarbonate alkalinity and water pH) and at certain rates of biochemical oxygen utilization (BOD) 7.2 g of nitrogen and 1 g of phosphorus produce 115 g of algae, which decomposition then consumes 115 g of oxygen [1].
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Zhou, Weijian, Wenzhong Liang, Yining Ding, Yutao Lei, Zhihua Pang i Zhipeng Zhuang. "Engineering Example of Compact Type Sewage Treatment Plant". E3S Web of Conferences 145 (2020): 02052. http://dx.doi.org/10.1051/e3sconf/202014502052.

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Considering the land shortage features of a given district in Hangzhou city, the High-sludge sedimentation tank + denitrification filtering tank + nitrification filtering tank + cloth media filtering tank process is adopted for purification treatment. When the system (with the treatment scale of 15,000m3/d) runs for 60 days, the average removal rate of COD and ammoniacal nitrogen are 86% and 96% respectively and the effluent quality reach the quasi grade IV standard.
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Shamanskyi, Sergii, Sergii Boichenko, Viktoria Khrutba, Olena Barabash, Iryna Shkilniuk, Anna Yakovlieva, Petro Topilnyckyi i Lesia Pavliukh. "Improving the photobioreactor operation efficiency in the technological scheme of wastewater treatment". Eastern-European Journal of Enterprise Technologies 6, nr 10 (114) (29.12.2021): 6–15. http://dx.doi.org/10.15587/1729-4061.2021.248746.

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Conventional process schemes of municipal sewage water treatment, advantages, and disadvantages of the methods applied when removing biogenic elements were considered. It was shown that the existing shortcomings cause additional explicit costs and difficulties when disposing of the resulting waste. Low efficiency of the removal processes themselves causing residual concentrations of biogenic elements in the treated sewage water was also shown. A process scheme for treating municipal sewage water was proposed. It includes the use of a photobioreactor of a proposed design for the removal of biogenic elements due to the metabolism of microalgae. It was experimentally shown that the use of Euglena gracilis strain for removal of phosphates in initial concentrations of 4, 7, and 14 mg/dm3 from sewage water is the most efficient way. It makes it possible to reduce these concentrations to residual 0…0.55 mg/dm3 in four days. A 3.75…5.58 times increment of microalgae biomass during this period was also shown. A mathematical model was constructed for calculating the time of staying the sewage water and microalgae mixture in a photobioreactor to achieve the required degree of removal of biogenic elements. Based on the proposed model and experimental studies, the required time of staying in the rector working area was calculated. It was shown that with the use of Euglena gracilis strain but without removal of biogenic elements at previous purification stages (process schemes including only mechanical purification), the time of mixture staying in the working zone was 37.81 hrs. With partial removal of biogenic elements at the stage of biological treatment (0.55 mg/dm3 total nitrogen, 0.91 mg/dm3 ammonium nitrogen, 0.44 mg/dm3 phosphates), this time was reduced to 26.66 hrs. It was found that the use of Euglena gracilis strain instead of Chlorella vulgaris (FC-16) in the removal of phosphates results in a 2-time increase in the process efficiency and a 50 % decrease in time of mixture staying in the working zone. Recommendations for calculating geometric parameters of photobioreactors of the proposed design were given for use in the process schemes
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Andersson, C., M. Tendaj i M. Rothman. "Filtration at Bromma Sewage Treatment Plant". Water Science and Technology 25, nr 4-5 (1.02.1992): 59–66. http://dx.doi.org/10.2166/wst.1992.0481.

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The requirements for purification of the sewage will be more stringent in Sweden. For the three plants in Stockholm - Henriksdal, Bromma and Loudden the proposed limit concentrations for BOD7, total phosphorus and total nitrogen are 10, 0.3 and 15 respectively. A limit value of 0.3 mg/l of phosphorus in the effluent will require a filtration stage. In this paper results are presented from filter tests at Bromma sewage treatment plant. The tests were carried out during almost two years and included operation of different types of sand dual-media downflow filters and an upflow filter. The filters were tested with respect to sludge accumulation capacity, suspended solids removal and phosphorus removal at different operation conditions including chemical precipitation in the filters.
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Yan, Min, Jian Zhang, Xiaoguo Wang i Xin Lu. "Performance of a Tower-Shaped Integrated Ecological Purification Device for Pollutants Removal from Domestic Sewage in Rural Areas". International Journal of Environmental Research and Public Health 19, nr 24 (18.12.2022): 17014. http://dx.doi.org/10.3390/ijerph192417014.

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With the continuous development of China’s modern economy and agricultural society, the discharge of rural sewage has been recognized as a major threat to the safety of the rural ecological environment. This study discussed the purification efficiency of a tower-shaped integrated ecological purification device (TIEPD)—consisting of a measuring tank, detention tank and three-stage purification unit—towards various common pollutants in rural areas during operation and tested the stability and efficiency of the TIEPD under different rural life events (fair activity days and nonfair activity days) and different precipitation intensities (light rain, moderate rain and heavy rain). The results showed that the average removal efficiencies of the TIEPD towards chemical oxygen demand, ammonia nitrogen, total nitrogen and total phosphorus were 69%, 67%, 54% and 73%, respectively. The average effluent concentration of each pollutant can meet the standard of the discharge of pollutants in China. The system exhibited good stability in removing pollutants and good ecological and economic benefits. This study provides the treatment of domestic sewage in the upper reaches of the Yangtze River and in mountainous areas of China and strengthens the prevention and control of rural nonpoint source pollution.
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Rozprawy doktorskie na temat "Sewage – Purification – Nitrogen removal"

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Mao, Yanping, i 毛艷萍. "Biological removal of phosphorus and nitrogen from wastewater : new insights from metagenomic and metatranscriptomic approaches". Thesis, The University of Hong Kong (Pokfulam, Hong Kong), 2014. http://hdl.handle.net/10722/206323.

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Yan, Qingmei, i 嚴慶梅. "Biological nitrogen removal of saline wastewater by ammoniumoxidizers". Thesis, The University of Hong Kong (Pokfulam, Hong Kong), 2009. http://hub.hku.hk/bib/B42182116.

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Chen, Wen, i 陳雯. "A membrane bioreactor(MBR) for an innovative biological nitrogen removal process". Thesis, The University of Hong Kong (Pokfulam, Hong Kong), 2007. http://hub.hku.hk/bib/B39557959.

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楊龍元 i Lung-yuen Christopher Yeong. "Removal of wastewater cod and nitrogen using fibrous packing media". Thesis, The University of Hong Kong (Pokfulam, Hong Kong), 1991. http://hub.hku.hk/bib/B31210636.

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Cao, Keping. "Simultaneous Removal of Carbon and Nitrogen by Using a Single Bioreactor for Land Limited Application". Thesis, Water Resources Research Center, University of Hawaii at Manoa, 1998. http://hdl.handle.net/10125/22230.

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An Entrapped-Mixed-Microbial-Cell (EMMC) process was investigated for its simultaneous removal of carbon and nitrogen in a single bioreactor with the influent COD/N ratio varying from 4 to 15 and influent alkalinity of 140 mg CaCO3/L and 230 mg CaCO3/L. The reactor was operated with alternate schedules of intermittent aeration. Two different sizes of carriers (10 * 10 * 10 mm3 and 20 * 20 * 20 mm3) were studied. The medium carrier (10 * 10 * 10 mm3) system presents higher nitrogen removal and COD removal compared to the large carrier system. The nitrogen removal efficiency is related to the ratio of COD/N in the influent. With the increase of the COD/N ration in the influent, the nitrogen removal efficiency is increased. The average reductions of nitrogen were over 92% and the average reductions of SCOD and BOD5 are over 95% and 97%, respectively, in the medium carrier system. This is operated at the HRT of 12 hours and 0.5 hour aeration and 2 hours of non-aeration, and the COD/N ratio of 15 in the influent. Changing alkalinity from 140 to 230 mg CaCO3/L has no effect in both large and medium carriers for the nitrogen removal efficiency. The pH, oxidation – reduction potential (ORP) and dissolved oxygen (DO) were used to monitor the biological nitrogen removal. It was found that the ORP (range from -100 to 300 mV) can be used to provide better effluent quality measured as total-nitrogen of less than 10 mg/L. Also, the impact of influent COD/N ratio on the effluent quality (measured as Inorg.-nitrogen) for the EMMC process is very important. Compared to other two compact biological wastewater treatment processes, membrane bioreactor (MBR) and moving bed biofilm reactor (MBBR), the EMMC process with the intermittent aeration has higher removal efficiencies of carbon and nitrogen, easier operation, lower O&M cost, lower energy requirement, and more compact. The total cost requirement is less than $3.27 per 1000 gallons (3.785 m 3) of treated settled domestic sewage per day. It is apparent that the EMMC process is technically feasible for the simultaneous removal of carbon and nitrogen under the operation on a schedule of intermittent aeration and suitable to be used for replacement or upgrading of existing treatment plant at land limited area.
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Clayton, John Andrew. "Denitrification kinetics in biological nitrogen and phosphorus removal activated sludge systems". Master's thesis, University of Cape Town, 1989. http://hdl.handle.net/11427/21139.

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In order to size the anoxic reactors in nutrient (N and P) removal activated sludge plants, it is essential to know the denitrification kinetics that are operative in such systems. To date, denitrification kinetics have been accurately defined only for systems that remove N alone; little research has been performed on denitrification in N and P removal plants.
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黃金華 i Kam-wah Wong. "Deritrification in the activated sludge process with controlled anoxicconditions in the aeration tank". Thesis, The University of Hong Kong (Pokfulam, Hong Kong), 1987. http://hub.hku.hk/bib/B31208423.

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Hijazi, Amal. "Nitrogen and phosphorus transformations in fixed-film biofilters subjected to aeration/no-aeration cycles". Thesis, Queensland University of Technology, 1998. https://eprints.qut.edu.au/36070/6/36070_Digitised_Thesis.pdf.

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Despite recent developments in fixed-film combined biological nutrients removal (BNR) technology; fixed-film systems (i.e., biofilters), are still at the early stages of development and their application has been limited to a few laboratory-scale experiments. Achieving enhanced biological phosphorus removal in fixed-film systems requires exposing the micro-organisms and the waste stream to alternating anaerobic/aerobic or anaerobic/anoxic conditions in cycles. The concept of cycle duration (CD) as a process control parameter is unique to fixed-film BNR systems, has not been previously investigated, and can be used to optimise the performance of such systems. The CD refers to the elapsed time before the biomass is re-exposed to the same environmental conditions in cycles. Fixed-film systems offer many advantages over suspended growth systems such as reduced operating costs, simplicity of operation, absence of sludge recycling problems, and compactness. The control of nutrient discharges to water bodies, improves water quality, fish production, and allow water reuse. The main objective of this study was to develop a fundamental understanding of the effect of CD on the transformations of nutrients in fixed-film biofilter systems subjected to alternating aeration I no-aeration cycles A fixed-film biofilter system consisting of three up-flow biofilters connected in series was developed and tested. The first and third biofilters were operated in a cyclic mode in which the biomass was subjected to aeration/no-aeration cycles. The influent wastewater was simulated aquaculture whose composition was based on actual water quality parameters of aquacuture wastewater from a prawn grow-out facility. The influent contained 8.5 - 9:3 mg!L a111monia-N, 8.5- 8.7 mg/L phosphate-P, and 45- 50 mg!L acetate. Two independent studies were conducted at two biofiltration rates to evaluate and confirm the effect of CD on nutrient transformations in the biofilter system for application in aquaculture: A third study was conducted to enhance denitrification in the system using an external carbon- source at a rate varying from 0-24 ml/min. The CD was varied in the range of0.25- 120 hours for the first two studies and fixed at 12 hours for the third study. This study identified the CD as an important process control parameter that can be used to optimise the performance of full-scale fixed-film systems for BNR which represents a novel contribution in this field of research. The CD resulted in environmental conditions that inhibited or enhanced nutrient transformations. The effect of CD on BNR in fixed-film systems in terms of phosphorus biomass saturation and depletion has been established. Short CDs did not permit the establishment of anaerobic activity in the un-aerated biofilter and, thus, inhibited phosphorus release. Long CDs resulted in extended anaerobic activity and, thus, resulted in active phosphorus release. Long CDs, however, resulted in depleting the biomass phosphorus reservoir in the releasing biofilter and saturating the biomass phosphorus reservoir in the up-taking biofilter in the cycle. This phosphorus biomass saturation/depletion phenomenon imposes a practical limit on how short or long the CD can be. The length of the CD should be somewhere just before saturation or depletion occur and for the system tested, the optimal CD was 12 hours for the biofiltration rates tested. The system achieved limited net phosphorus removal due to the limited sludge wasting and lack of external carbon supply during phosphorus uptake. The phosphorus saturation and depletion reflected the need to extract phosphorus from the phosphorus-rich micro-organisms, for example, through back-washing. The major challenges of achieving phosphorus removal in the system included: (I) overcoming the deterioration in the performance of the system during the transition period following the start of each new cycle; and (2) wasting excess phosphorus-saturated biomass following the aeration cycle. Denitrification occurred in poorly aerated sections of the third biofilter and generally declined as the CD increased and as the time progressed in the individual cycle. Denitrification and phosphorus uptake were supplied by an internal organic carbon source, and the addition of an external carbon source (acetate) to the third biofilter resulted in improved denitrification efficiency in the system from 18.4 without supplemental carbon to 88.7% when the carbon dose reached 24 mL/min The removal of TOC and nitrification improved as the CD increased, as a result of the reduction in the frequency of transition periods between the cycles. A conceptual design of an effective fixed-film BNR biofilter system for the treatment of the influent simulated aquaculture wastewater was proposed based on the findings of the study.
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Guo, Lei. "Optimization of BNR from wastewater using SBR and A²O processes". Thesis, University of Macau, 2011. http://umaclib3.umac.mo/record=b2493027.

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Hanson, Carter Curtis. "Temporal effect on nitrogen removal in a subsurface flow constructed wetland". Virtual Press, 1996. http://liblink.bsu.edu/uhtbin/catkey/1027117.

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A subsurface flow constructed wetland planted with the common reed (Phragmites australis) and softstem bulrush (Scirpus validus) was built in East Central Indiana. The objective of this study was to determine if temperature had an effect on nitrogen (N) removal from the wetland. The research was conducted from the first week of October 3, 1995 to the first week in December 5, 1995 why the wetland froze. Water samples were taken from 5 samplings sites in the system. Each sample was analyzed for organic-N, ammonia, nitrate, and total-N. In the system statistically significant amounts of organic-N, nitrate, and total-N were removed. Ammonia lever reductions, however, were not significant. Organic-N had a mean removal of 37% (8 mg/1) 'Nitrate had a mean removal of 96% (2.3 mg/1). Total-N removal over the sampling period averaged 30% (12 mg/1). The N results were regressed against air and wastewater temperatures. Wastewater temperature was more important because it had a direct impact can the plants and microbes in the system. Warmer temperatures sustained a higher metabolism for the biota in the system. Air temperature had an indirect impact on efficiency of N removal from the wastewater flowing through the wetland. The primary impact .: f the air temperature was on water temperature which then affected the metabolism of or a nc ns in the wetland cell. Greater removal efficiencies were seen during high temperature periods and lower removal efficiencies were noted when the temperatures were low.
Department of Natural Resources and Environmental Management
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Książki na temat "Sewage – Purification – Nitrogen removal"

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Richard, Sedlak, red. Phosphorus and nitrogen removal from municipal wastewater: Principles and practice. Wyd. 2. [Chelsea, Mich.]: Lewis Publishers, 1991.

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Nyhuis, Geert. Beitrag zu den Möglichkeiten der Abwasserbehandlung bei Abwässern mit erhöhten Stickstoffkonzentrationen. Hannover: Institut für Siedlungswasserwirtschaft und Abfalltechnik der Universität Hannover, 1985.

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Risk Reduction Engineering Laboratory (U.S.) i United States. Environmental Protection Agency. Office of Wastewater Enforcement and Compliance., red. Nitrogen control. Lancaster, Pa: Technomic Publishing Company, 1993.

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Gantzer, C. J. Biological degradation of cyanide by nitrogen-fixing cyanobacteria. Cincinnati, OH: U.S. Environmental Protection Agency, Risk Reduction Engineering Laboratory, 1990.

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Zimmo, Omar. Nitrogen transformations and removal mechanisms in algal and duckweed waste stabilisation ponds. Lisse: Balkema, 2003.

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Teichgräber, Burkhard. Zur Nitrifikation von Abwässern mit geringer Säurekapazität. Braunschweig: Institut für Siedlungswasserwirtschaft, Technische Universität Braunschweig, 1988.

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Siedlungswasserwirtschaftliches Kolloquium (61st 1986 Stuttgart, Germany). Verfahren zur Phosphor- und Stickstoffelimination: 61. Siedlungswasserwirtschaftliches Kolloquium. München: R. Oldenbourg, 1986.

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Halling-Sørensen, B. The removal of nitrogen compounds from wastewater. Amsterdam: Elsevier, 1993.

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Waquoit Bay National Estuarine Research Reserve. Nitrogen removal onsite wastewater treatment systems: Technologies and regulatory strategies. Waquoit, Mass: WBNERR, 1992.

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Surmacz-Górska, Joanna. Usuwanie zanieczyszczeń organicznych oraz z odcieków powstających w wysypiskach odpadów komunalnych. Gliwice: Wydawnictwo Politechniki Śląskiej, 2000.

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Części książek na temat "Sewage – Purification – Nitrogen removal"

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Radetic, Bogdanka, i Claudio Lehmann. "Carbon, Nitrogen, and Phosphorous Removal, Basics and Overview of Technical Applications". W Handbook of Water and Used Water Purification, 1–39. Cham: Springer International Publishing, 2018. http://dx.doi.org/10.1007/978-3-319-66382-1_93-1.

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Jin, Bingbing. "Application of Cognitive Environment and Data in Urban Sewage Biological Phosphorus and Nitrogen Removal System". W Lecture Notes on Data Engineering and Communications Technologies, 536–40. Singapore: Springer Singapore, 2021. http://dx.doi.org/10.1007/978-981-16-5854-9_68.

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Ramli, Suzana, Jurina Jaafar i Raja Baharudin Raja Mohamad. "Study on Nitrogen Removal Capability of Selected Regional Sewage Treatment Plants in Klang Valley, Malaysia". W Lecture Notes in Civil Engineering, 1385–96. Singapore: Springer Singapore, 2022. http://dx.doi.org/10.1007/978-981-16-7924-7_91.

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Ergas, S. J., i V. Aponte-Morales. "Biological Nitrogen Removal". W Comprehensive Water Quality and Purification, 123–49. Elsevier, 2014. http://dx.doi.org/10.1016/b978-0-12-382182-9.00047-5.

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Boyer, T. H. "Physical–Chemical Processes for Nitrogen Removal". W Comprehensive Water Quality and Purification, 163–95. Elsevier, 2014. http://dx.doi.org/10.1016/b978-0-12-382182-9.00085-2.

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Kamaruddin, Mohamad, Mohd Yusoff, Hamidi Aziz i Nur Basri. "Removal of COD, Ammoniacal Nitrogen and Colour from Stabilized Landfill Leachate by Anaerobic Organism". W Sewage and Landfill Leachate, 247–67. Apple Academic Press, 2016. http://dx.doi.org/10.1201/b20005-18.

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"Removal of COD, Ammoniacal Nitrogen and Colour from Stabilized Landfill Leachate by Anaerobic Organism". W Sewage and Landfill Leachate, 269–90. Apple Academic Press, 2016. http://dx.doi.org/10.1201/b20005-21.

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Sánchez Guillén, Javier Adrián. "Pollution control of dissolved inorganic nitrogen in urban zones through sewage treatment". W Autotrophic Nitrogen Removal from Low Concentrated Effluents, 1–47. CRC Press, 2017. http://dx.doi.org/10.1201/9781315115955-1.

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Shen, Hengxia. "Research on technical reforms of nitrogen and phosphorus removal process in T Sewage Company: Research on technical reforms of nitrogen and phosphorus removal process in T Sewage Company". W Advances in Energy, Environment and Materials Science, 209–12. CRC Press, 2016. http://dx.doi.org/10.1201/b19635-46.

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"Advanced Wastewater Treatments". W Advanced Design of Wastewater Treatment Plants, 293–331. IGI Global, 2019. http://dx.doi.org/10.4018/978-1-5225-9441-3.ch005.

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Advanced wastewater treatment is the process that reduces the level of impurities in wastewater below that attainable through conventional secondary or biological treatment. It includes the removal of nutrients such as phosphorus and nitrogen and a high percentage of suspended solids. The removal of nitrogen and phosphorus from wastewater has become an emerging worldwide concern because these compounds cause eutrophication in natural water. A post-treatment process is therefore required to remove nitrogen and phosphorus from the effluent. Therefore, the purpose of this chapter is to provide the deeper knowledge of membrane technology, membrane bioreactor, sequential batch reactor, moving bed biofilm reactor, nitrification, denitrification, phosphorus removal from wastewater, carbon adsorption, and provide a design of a sewage treatment plant using moving bed biofilm reactor technology.
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Streszczenia konferencji na temat "Sewage – Purification – Nitrogen removal"

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Lu, Liquan, Liping Qiu, Shoubin Zhang, Jiabin Wang i Kang Xie. "Research Progress of Nitrogen and Phosphorus Removal in Municipal Sewage". W 2015 4th International Conference on Sustainable Energy and Environmental Engineering. Paris, France: Atlantis Press, 2016. http://dx.doi.org/10.2991/icseee-15.2016.85.

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Song, Xiancai, Lejun Zhao, Dongfang Liu i Jianqiang Zhao. "Step-feeding SBR for nitrogen removal from expressway service area sewage". W 11TH ASIAN CONFERENCE ON CHEMICAL SENSORS: (ACCS2015). Author(s), 2017. http://dx.doi.org/10.1063/1.4977293.

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Chen Ai-Xia, Ma Yuan, Liu Xiao-Ru i Chen Jing-Wen. "Effect research of nitrogen removal out of sewage in constructed wetland". W 2011 International Symposium on Water Resource and Environmental Protection (ISWREP). IEEE, 2011. http://dx.doi.org/10.1109/iswrep.2011.5893252.

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Zhou, Gaofeng, Yiqing Liu, Junfeng Zhao, Yongsheng Fu i Yuhua Nie. "The purification of nitrogen by the micro-aeration enhanced ecological floating bed in sewage". W ADVANCES IN ENERGY SCIENCE AND ENVIRONMENT ENGINEERING II: Proceedings of 2nd International Workshop on Advances in Energy Science and Environment Engineering (AESEE 2018). Author(s), 2018. http://dx.doi.org/10.1063/1.5029800.

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Zhang, Shoubin, Maoan Du i Liping Qu. "Modified DAT/IAT Process for Removal of Ammonia Nitrogen from Domestic Sewage". W 2008 2nd International Conference on Bioinformatics and Biomedical Engineering (ICBBE '08). IEEE, 2008. http://dx.doi.org/10.1109/icbbe.2008.1153.

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Yoka, Getu, i Ajay Bharti. "The Potential of Sewage Treatment through Constructed Wetlands in Northeast India: A Critical Review". W International Web Conference in Civil Engineering for a Sustainable Planet. AIJR Publisher, 2021. http://dx.doi.org/10.21467/proceedings.112.30.

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The benefits of economical treatment systems and global demand for introducing sustainable way of environmental management, the Constructed Wetlands (CWs) treatment of domestic sewage is rising rapidly all over the globe. The Total nitrogen in the sewage is the summation of Organic Nitrogen, Nitrate Nitrogen, Nitrite Nitrogen and Ammonium Nitrogen. Ammonification, Matrix Adsorption, Nitrification, Denitrification, Plant Uptake and Ammonia Volatilization are the principle involved for total nitrogen removal in the treatment of sewage using CWs. This paper provides a comprehensive review by comparative analysis of effects of type and nature of flow system, wetland structures, types of Macrophyte, removal mechanisms, Aeration, Step-feeding and other key operational parameters and conditions for the enhance removal of total nitrogen in CWs.
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Zhang, Hao, Guanghua Xu, Zhaoxia Zeng, Youzhi Li, Muqing Qiu i Fuping Zeng. "Nitrogen removal of a Myriophyllum elatinoides purification system for treating piggery wastewater in karst region". W 2016 5th International Conference on Sustainable Energy and Environment Engineering (ICSEEE 2016). Paris, France: Atlantis Press, 2016. http://dx.doi.org/10.2991/icseee-16.2016.123.

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Pio S Lombardo. "Nitrogen Removal for Cluster Residential and Commercial Development, Main Street Village, Mashpee, MA". W Eleventh Individual and Small Community Sewage Systems Conference Proceedings, 20-24 October 2007, Warwick, Rhode Island. St. Joseph, MI: American Society of Agricultural and Biological Engineers, 2007. http://dx.doi.org/10.13031/2013.23981.

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Nara, Matsunori, i Keiji Yoda. "Purification of Sea Pollution by a Bio-Micromachine". W ASME 2009 28th International Conference on Ocean, Offshore and Arctic Engineering. ASMEDC, 2009. http://dx.doi.org/10.1115/omae2009-79240.

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Contamination of sea water is proceeding quickly under the influence of climate changes including global warming. The cause of the expansion of seawater pollution is an elevated water temperature by the climate change and an inflow of the pollution river water. The problem of seawater pollution occurs as a result that planet’s environmental problem and regional environmental problems are combined. The effective method for removing these contaminants from sea water now is not developed. In this research, the method of producing the micromachine which fixed the photocatalyst to the surface of the substance designed so that it might float near a sea surface was built up. And experimental examination was performed about the conditions for removing the organic matter and nutritive salts in the sea using this micromachine. In addition, as a result of performing theoretical examination about a photocatalyst, the titanium dioxide was chosen as a suitable photocatalyst. In the examination about the quality of the material of a micromachine, since an organic polymer substance like styrene foam will be decomposed by the photocatalyst made to adhere to the surface, it decided to use the sphere of metal hollow. Metal took the corrosive protection performance into consideration. Moreover, the form of a metal ball was designed so that photocatalyst efficiency might become high. This metal ball can be collected and re-used after a treatment end. In order to make a photocatalyst bond to a surface of metal, baking by the water solvent method and an alcoholic solvent method was performed. Here, specific treatment conditions required in order to carry out the supported of the photocatalyst to metal certainly were clarified. A phosphate and nitrogen caused eutrophication and the damage by eutrophication is increasing them by in recent years. Then, the experiment about decomposition removal of the phosphate and nitrogen which are the causative agent which pollutes sea water was conducted. According to the evaluation experiment of the performance of a micromachine, the removal ratio of a phosphate was about 30%, and the removal ratio of nitrogen was about 60%. It was shown that the suitable amount of micro-machines per unit volume and the interval between them must be maintained here. As mentioned above, establishment of the manufacture method of a micromachine and the fundamental verification about the performance were able to be performed. However, a conclusion clear about the performance in the depth direction of a micromachine is not obtained, but it is a future subject.
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Ling-Xiao, Gong, Peng Yong-Zhen, Yang Qing, Zhu Ru-Long i Wang Shu-Ying. "Effect of Internal Recycle on Nitrogen Removal in a Novel Anoxic/oxic Integrated Biofilm Reactor Treating Low C/N Ratio Domestic Sewage". W 2013 Third International Conference on Intelligent System Design and Engineering Applications (ISDEA). IEEE, 2013. http://dx.doi.org/10.1109/isdea.2012.153.

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