Relevant bibliographies by topics / Effluent Treatment Plant Sludge

Contents

  1. Journal articles
  2. Dissertations / Theses
  3. Books
  4. Book chapters
  5. Conference papers
  6. Reports

Academic literature on the topic 'Effluent Treatment Plant Sludge'

Author: Grafiati
Published: 4 June 2021
Last updated: 6 September 2023

Create a spot-on reference in APA, MLA, Chicago, Harvard, and other styles

Select a source type:

Consult the lists of relevant articles, books, theses, conference reports, and other scholarly sources on the topic 'Effluent Treatment Plant Sludge.'

Next to every source in the list of references, there is an 'Add to bibliography' button. Press on it, and we will generate automatically the bibliographic reference to the chosen work in the citation style you need: APA, MLA, Harvard, Chicago, Vancouver, etc.

You can also download the full text of the academic publication as pdf and read online its abstract whenever available in the metadata.

Journal articles on the topic "Effluent Treatment Plant Sludge"

1

T, Raghunathan. "A Study on Geopolymer with Dyeing Industry Effluent Treatment Plant Sludge." International Journal of Trend in Scientific Research and Development Volume-3, Issue-1 (December 31, 2018): 950–53. http://dx.doi.org/10.31142/ijtsrd19165.

Full text
APA, Harvard, Vancouver, ISO, and other styles
2

Sivard, Å., T. Ericsson, and B. Larsson. "Strategy for nutrient control in modern effluent treatment plants." Water Science and Technology 55, no. 6 (March 1, 2007): 157–63. http://dx.doi.org/10.2166/wst.2007.224.

Full text
Abstract:
The fate of nutrients in the modern effluent treatment plant depends on several factors, for example type of treatment plant, availability of nutrients in the specific effluent, dosing of nutrients and sludge age/production. New technologies with the aim to increase the efficiency and stability of the conventional activated sludge process have strongly affected the possibilities to control discharge of nutrients in pulp and paper effluents. A paradox is that a reduction of organic material may often lead to an increase of nutrient discharges. It is of the utmost importance that the operators have good knowledge of the factors affecting nutrient uptake and release in order to minimise nutrient discharge and obtain optimal plant performance. Dosing of nitrogen and phosphorus is one key factor in the sensitive balance in most pulp and paper effluent treatment plants. Correct dosing is crucial as high or low doses might lead not only to increased discharge of nutrients but also to severe operational problems with poor sludge quality, which in turn affects the plant performance for longer periods.
APA, Harvard, Vancouver, ISO, and other styles
3

Sima, Laura C., Julien Schaeffer, Jean-Claude Le Saux, Sylvain Parnaudeau, Menachem Elimelech, and Françoise S. Le Guyader. "Calicivirus Removal in a Membrane Bioreactor Wastewater Treatment Plant." Applied and Environmental Microbiology 77, no. 15 (June 10, 2011): 5170–77. http://dx.doi.org/10.1128/aem.00583-11.

Full text
Abstract:
ABSTRACTTo evaluate membrane bioreactor wastewater treatment virus removal, a study was conducted in southwest France. Samples collected from plant influent, an aeration basin, membrane effluent, solid sludge, and effluent biweekly from October 2009 to June 2010 were analyzed for calicivirus (norovirus and sapovirus) by real-time reverse transcription-PCR (RT-PCR) using extraction controls to perform quantification. Adenovirus andEscherichia colialso were analyzed to compare removal efficiencies. In the influent, sapovirus was always present, while the norovirus concentration varied temporally, with the highest concentration being detected from February to May. All three human norovirus genogroups (GI, GII, and GIV) were detected in effluent, but GIV was never detected in effluent; GI and GII were detected in 50% of the samples but at low concentrations. In the effluent, sapovirus was identified only once. An adenovirus titer showing temporal variation in influent samples was identified only twice in effluent.E. coliwas always below the limit of detection in the effluent. Overall, the removal of calicivirus varied from 3.3 to greater than 6.8 log units, with no difference between the two main genogroups. Our results also demonstrated that the viruses are blocked by the membrane in the treatment plant and are removed from the plant as solid sludge.
APA, Harvard, Vancouver, ISO, and other styles
4

van Kempen, R., C. C. R. ten Have, S. C. F. Meijer, J. W. Mulder, J. O. J. Duin, C. A. Uijterlinde, and M. C. M. van Loosdrecht. "SHARON process evaluated for improved wastewater treatment plant nitrogen effluent quality." Water Science and Technology 52, no. 4 (August 1, 2005): 55–62. http://dx.doi.org/10.2166/wst.2005.0087.

Full text
Abstract:
New stricter nitrogen effluent standards and increasing influent loads require existing wastewater treatment plans (WWTPs) to extend or optimize. At WWTPs with limited aeration capacity, limited denitrification capacity or shortage of aerobic sludge age, implementation of SHARON to improve nitrogen effluent quality can be a solution. SHARON is a compact, sustainable and cost-effective biological process for treatment of nitrogen-rich rejection waters. At WWTP Rotterdam-Dokhaven and WWTP Utrecht a SHARON has been in operation for several years. For both WWTPs the effect of SHARON on the nitrogen effluent quality has been evaluated. WWTP Rotterdam-Dokhaven has limited aeration capacity. By implementation of SHARON, the ammonia load of the effluent was reduced by 50%. WWTP Utrecht had limited denitrification capacity. The implementation of SHARON improved the effluent nitrate load by 40%. The overall TN removal efficiency increased from 65% to over 75% and strict nitrogen effluents standards (TN = 10 mg N/l) could be reached. Through modelling and supported by full scale practice it has been shown that by implementation of SHARON in combination with enhanced influent pre-treatment, the aerobic sludge age can be extended to maintain total nitrogen removal at lower temperatures.
APA, Harvard, Vancouver, ISO, and other styles
5

Lumley, D. J., P. Balmér, and J. Adamsson. "Investigations of Secondary Settling at a Large Treatment Plant." Water Science and Technology 20, no. 4-5 (April 1, 1988): 133–42. http://dx.doi.org/10.2166/wst.1988.0161.

Full text
Abstract:
The sedimentation phase of the activated sludge process has a large influence on the effluent quality of secondary wastewater treatment plants. Increasingly stringent effluent guidelines emphasize the need to improve the performance of secondary settlers. Full scale studies of rectangular settlers, at a secondary treatment plant with an average flow of 4 m3/s, were made. The non-settleable fraction of the effluent suspended solids defines an upper limit to settler efficiency. Polymer can be used to enhance settling when dealing with peak flow situations. The mass of solids in the settler, needed to calculate a mass balance of the activated sludge process, can be estimated by a simple model based on the sludge blanket depth and the average concentration of the sludge blanket at a central location in a settler. On-line instruments are useful for monitoring rapid and periodic changes in the state of the activated sludge process.
APA, Harvard, Vancouver, ISO, and other styles
6

Assis, Tatiane Martins de, Aruani Letícia da Silva Tomoto, Ana Paula Trevisan Lied, Luiz Felipe Gomes Ferreira, Julia Elizabeth Martins, Dagoberto Yukio Okada, Nicolas Roche, and Simone Damasceno Gomes. "Kinetic of nitrogen consumption by Anammox process in membrane biofilm reactors operated in sequential batch." Ciência e Natura 44 (April 20, 2022): e20. http://dx.doi.org/10.5902/2179460x68843.

Full text
Abstract:
Biological nitrogen removal via Anammox is an advantageous technology in the nitrogen treatment effluents with a low Carbon/Nitrogen ratio, a process that makes this route interesting for the most different types of industries, agribusinesses, and urban effluent treatment plants. Achieving robust Anammox biomass for use in full-scale plants is still a challenge that motivates studies of biomass enrichment and the search for kinetic parameters of substrate consumption rate that help optimize the conduction of reactors. According to the previously mentioned, this work aimed to carry out the kinetic study of nitrogen consumption by the Anammox process in a membrane aerated biofilm reactors operated in sequential batches (MABR-BS). 6 MABR-BS reactors were used, each one of them inoculated with a specific Anammox sludge, obtained from the enrichment of anaerobic and aerobic sludges coming from 3 different sludge sources, namely, a municipal wastewater treatment plant, a landfill leachate treatment plant, and a swine slaughterhouse effluent treatment plant. For the kinetic study, 6 reactors were used, made in glass flasks with a total volume of 1L, with a useful volume of 500 mL, with the 300:200mL ratio between synthetic effluent (with 100mgN-NH4+.L-1) and sludge from the sources: R1 - anaerobic sludge from a UASB reactor for urban sewage treatment; R2 - mixed sludge from a UASB reactor, consisting of waste sludge and supernatant scum; R3 - anaerobic sludge from landfill leachate treatment; R4 - mixed sludge consisting of aerobic and anaerobic sludge from landfill leachate treatment plant; R5 - anaerobic sludge from the swine slaughter effluent treatment plant and R6 - aerobic and anaerobic sludge from the swine slaughter effluent treatment plant. The experimental apparatus had 3 aerators coupled to 3 flowmeters with an air flow regulated at 1.0 L.min-1; 30 cm of silicone membrane in a curved shape with one of the inlets connected to the aerator and flowmeter, the other outlet was immersed in a 75 cm water column, exerting negative pressure on the air inside the tubular silicone membrane, forcing the air to exit through the microporosity of the membrane. Aeration was intermittent, with an interval of 0.16 h between each minute of aeration, the reactors were shaken in a water bath at 30 rpm and temperature of 32°C. The kinetic test had a duration of 24 hours with sampling every 2.5 hours. The nitrogen removal efficiencies (%) determined in the kinetic test were 61.36 (R1); 61.01(R2); 59.03 (R3); 56.70 (R4); 62.77 (R5) and 64.40 (R6). Regarding pH, all reactors had an initial pH above 8.0 and a final pH close to neutral. The specific nitrogen removal rates (in mgN.gVSS-1h-1), were on average 29.43 (R1); 33.50 (R2); 33.62 (R3); 33.42 (R4); 28.90 (R5) and 30.34 (R6). The best performance in the kinetic assay was obtained in the R1 reactor, obtaining a specific activity of maximum nitrogen removal of 57.61 mgN.gVSS-1h-1 and molar generation of residual nitrate with a stoichiometric coefficient of 0.018 mol.
APA, Harvard, Vancouver, ISO, and other styles
7

Bennie, D. T., C. A. Sullivan, H. B. Lee, and R. J. Maguire. "Alkylphenol Polyethoxylate Metabolites in Canadian Sewage Treatment Plant Waste Streams." Water Quality Research Journal 33, no. 2 (May 1, 1998): 231–52. http://dx.doi.org/10.2166/wqrj.1998.013.

Full text
Abstract:
Abstract Nonylphenol polyethoxylates and their refractory metabolites, including nonylphenol, are on the second Priority Substances List (PSL2) to determine if they are "toxic" as defined under the Canadian Environmental Protection Act. This study addresses the need for data on their occurrence in raw sewage, final effluents and sludge in Canada. Samples of raw sewage, final effluent and sludge were collected from 16 wastewater treatment plants across Canada in 1995 and 1996. These samples were analyzed for 4-nonylphenol (4-NP), nonylphenol ethoxylate (NP1EO), nonylphenol diethoxylate (NP2EO) and 4-4-tert-octylphenol (4-t-OP). Measurable quantities of these chemicals were found in almost all raw sewage and sludge samples. In the raw sewage, concentrations ranged from <0.005 to 21 μg/L for 4-t-OP, from 0.69 to 155 μg/L for 4-NP, from 2.9 to 43 μg/L for NP1EO and from 0.26 to 24 μg/L for NP2EO. Sludge concentrations (based on dry weight) ranged from <0.010 to 20 μg/g, from 8.4 to 850 μg/g, from 3.9 to 437 μg/g and from 1.5 to 297 μg/g for 4-t-OP, 4-NP, NP1EO and NP2EO, respectively. Of the final effluent samples, 60% contained detectable amounts of 4-t-OP and concentrations ranged from <0.005 to 0.37 μg/L. Almost all of the final effluent samples had detectable levels of 4-NP, NP1EO and NP2EO. The 4-NP concentrations varied from <0.020 to 13 μg/L, NP1EO was found in the range of 0.072 to 26 μg/L and NP2EO was found in the range of 0.099 to 21 μg/L.
APA, Harvard, Vancouver, ISO, and other styles
8

Hvala, Nadja, Darko Vrečko, and Cirila Bordon. "Plant-wide modelling for assessment and optimization of upgraded full-scale wastewater treatment plant performance." Water Practice and Technology 13, no. 3 (September 1, 2018): 566–82. http://dx.doi.org/10.2166/wpt.2018.070.

Full text
Abstract:
Abstract This paper presents the design of a plant-wide CNP (carbon-nitrogen-phosphorus) simulation model of a full-scale wastewater treatment plant, which will be upgraded for tertiary treatment to achieve compliance with effluent total nitrogen (TN) and total phosphorus (TP) limit values. The plant-wide model of the existing plant was first designed and extensively validated under long-term dynamic operation. The most crucial step was a precise characterization of input wastewater that was performed by extending the plant performance indicators both to a water line and sludge line and systematically estimating identifiable wastewater characterization parameters from plant-wide performance indicators, i.e. effluent concentrations, biogas and sludge production, and sludge composition. The thus constructed simulation model with standard activated sludge model (ASM2d) and anaerobic digestion model (MantisAD) overpredicted ortho-P and ammonia-N on the sludge line, indicating a need to integrate state-of-the-art physico-chemical minerals precipitation models to simulate plant-wide interactions more precisely. The upgraded plant with multimode anaerobic/anoxic/oxic configuration shows limited denitrification potential. Therefore, additional reject water treatment was evaluated to improve effluent TN and TP performance.
APA, Harvard, Vancouver, ISO, and other styles
9

Möbius, C. H., I. Demel, and R. Huster. "Performance Increase of Papermill Waste Water Treatment Plants by a High-Capacity Trickling Filter Inserted as First Biological Stage." Water Science and Technology 22, no. 7-8 (July 1, 1990): 217–23. http://dx.doi.org/10.2166/wst.1990.0248.

Full text
Abstract:
In many cases, it will be advisable to enhance operational safety and increase degradation performance of existing activated sludge plants by inserting a high-capacity trickling filter with plastic media. Easily degradable carbohydrates are largely decomposed in the trickling filter at low energy requirements. This allows the subsequent activated sludge stage to be set to reduced BOD sludge load levels which are required for efficient COD elimination, because the volume load has been reduced and a higher biomass concentration can be obtained at a lower sludge volume index. In the light of several years' pilot testing of numerous different effluents, and of knowledge derived from observations of several industrial plants in the paper sector, precise rating directives can now be given for plants of this type. It has proven advantageous to discharge the trickling filter effluent directly into the activated sludge plant without intermediate clarification. The effluent temperature, which frequently exceeds 35°C, is reduced by up to 10°C in the trickling filter. This improves the conditions prevailing in the activated sludge plant, thus permitting limit values for the discharge of effluents into surface waters to be adhered to.
APA, Harvard, Vancouver, ISO, and other styles
10

Defrain, M., and F. Schmidt. "Solids Concentrations in a Treatment Plant Effluent." Water Science and Technology 26, no. 9-11 (November 1, 1992): 2543–46. http://dx.doi.org/10.2166/wst.1992.0783.

Full text
Abstract:
In the calculations customarily used to dimension nitrification and denitrification plants in the Federal Republic of Germany, solids in the influent of the biological stage represent a significant output variable. Numerous modified methods based on nationally and internationally standardized analysis procedures are available to determine solids concentrations in waste-water. Tests showed that different values are measured depending on the method of analysis employed. Harmonization of the analysis procedure is advisable to ensure comparable conditions for the calculation of activated sludge tank volumes. The solids reaching a treatment plant originate from two main sources. Filterable materials are passed to the treatment plant via the preceding sewerage network with its industrial and commercial users, but are also carried by process water from sludge treatment. The influence of process water on wastewater composition is illustrated by reference to the Wuppertal-Buchenhofen treatment plant.
APA, Harvard, Vancouver, ISO, and other styles
More sources

Dissertations / Theses on the topic "Effluent Treatment Plant Sludge"

1

Russo, Stephen Leonard. "Anaerobic treatment of a paper plant effluent." Master's thesis, University of Cape Town, 1987. http://hdl.handle.net/11427/21988.

Full text
Abstract:
The objective of this study was to investigate the anaerobic biological treatment of an organic-bearing wastewater from a particular paper manufacturing process at laboratory scale. The process produces paper by re-pulping waste paper. Effluent from the process has a Chemical Oxygen Demand (COD) concentration of approximately 4500 mg/l with a sulphate content of approximately 300 mg SO₄²⁻/l. The upflow anaerobic sludge bed (UASB) reactor was selected for the study. Important information derived from the laboratory treatability study was: (l) the extent of COD removal possible; (2) the effluent quality; (3) the maximum COD leading rate (kgCOD/m³ reactor/day) which can be achieved while maintaining reasonable COD removal, and the influence on loading rate of temperature: (4) the nature of the sludge produced in the reactor with particular reference to the extent of pelletisation: and (5) the effect of reactor effluent recycling on alkalinity requirements.
APA, Harvard, Vancouver, ISO, and other styles
2

Jiwani, Ashifa. "Influence of plant operating conditions on the dewaterability of surplus activated sludge." Thesis, Imperial College London, 1996. http://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.243950.

Full text
APA, Harvard, Vancouver, ISO, and other styles
3

Pereira, Sofia Filipe. "Modelling of a wastewater treatment plant using GPS-X." Master's thesis, Faculdade de Ciências e Tecnologia, 2014. http://hdl.handle.net/10362/13621.

Full text
Abstract:
Dissertation to obtain the degree of Master in Chemical and Biochemical Engineering
The work present in this thesis was conducted in Portucel Soporcel mill, in the industrial complex of Setúbal, and had as main objective the modelling of the treatment process of the effluents from this industry, using for this purpose the software GPS-X. This program has a clear-cut graphical interface and uses a specialized translator that converts the graphical process into material balance equations, based on dynamic models. These models allow, besides the kinetic descripton of the treatment process carried out at the WWTP, to simulate new scenarios towards the study of critical parameters for the process as well as optimization and control of the WWTP. The effluent that arrives to Portucel’s WWTP, from the pulp and paper mills of the complex, is particularly rich on fibers (solids), lignin, chlorinated and sulphur compounds, resin acids, phenols and starch. It has a brown colour due to the presence of lignin and has a high oxygen chemical demand (about 1,095 g O2/m3). The WWTP uses the activated sludge process with extended aeration. This method allows an efficient removal of organics at the same time as it minimizes the sludge production. For the modelling of the process it was necessary to collect historical data related to the WWTP’s performance over the last 3 years. This data was used as input values for the influent characterisation and as output values to achieve the treated effluent characterisation. Since the first simulation did not lead to the desired output results, it was necessary to proceed to the model calibration, by means of a more detailed study concerning the nutrient and organic fractions of the influent. Once the model was calibrated, a study of the urea flowrate was conducted. The urea is added to the influent, before the beginning of the biological oxidation, as a way to satisfy the nitrogen requirements along the treatment process. However, this flowrate was never submitted to a study that evaluated, in a higher detail, the effective requirements of this nutrient. Thus, some simulations were done using the software, by decreasing successively the value of the urea flowrate and the results obtained were analyzed. Furthermore, these simulations were validated in the WWTP itself, at Portucel, through the decrease of the urea flowrate to half the normal value. Both the simulations and Portucel’s results showed that, actually, the addition of urea is not necessary because it does not affect the treatment process in a significant way, namely in terms of the removal of chemical oxygen demand. The simulations have also showed that the concentration of nitrogen in the final effluent diminishes significantly with the reduction of the urea flowrate, which could be advantageous in an environmental point of view.
APA, Harvard, Vancouver, ISO, and other styles
4

Hariyadi, Hari Rom. "Microbiological treatment of prochloraz process effluent." Thesis, University of Strathclyde, 2000. http://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.366913.

Full text
APA, Harvard, Vancouver, ISO, and other styles
5

Schrader, Guillo Alexander. "Direct nanofiltration of wastewater treatment plant effluent." Enschede : University of Twente [Host], 2006. http://doc.utwente.nl/55981.

Full text
APA, Harvard, Vancouver, ISO, and other styles
6

Stocks, Christopher. "The reprocessing of brewery sludge to produce a useful compost." Thesis, University of Birmingham, 2000. http://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.368288.

Full text
APA, Harvard, Vancouver, ISO, and other styles
7

Stear, Robert Martin. "Effects of salinity on the settling properties of activated sludge." Thesis, University of Nottingham, 1998. http://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.243497.

Full text
APA, Harvard, Vancouver, ISO, and other styles
8

Savage, Matthew John. "Integrated Treatment Processes For Primary Wool Scouring Effluent." Thesis, University of Canterbury. Chemical and Process Engineering, 2003. http://hdl.handle.net/10092/1125.

Full text
Abstract:
The increasing cost of effluent treatment in the wool scouring industry is rapidly becoming a determining factor in the viability of existing scouring operations and new installations alike. This thesis details the development of an integrated effluent treatment process capable of treating the worst polluted effluent from a wool scour "heavy flow-down", to the point where it can either be economically discharged to local trade waste sewer, or directly discharged to river or ocean outfall with minimal environmental impact. The existing proprietary chemical flocculation process, Sirolan CF™, was improved by the addition of a bio-flocculation stage and turbidity monitoring and control, and the product from this process fed to an aerobic biological treatment system based upon the traditional activated sludge process. The biological treatment process was found to remove up to 98% of the BOD5 loading from the pre-treated liquor with a hydraulic residence time of at least 50 hours being required in the aerobic digestion vessels. A residual biorefractory COD of approximately 3,600mg/L was identified which could not be removed by biological treatment. When operating continuously, the biological process was observed to metabolically neutralise the pH 3.0 - 4.5 feed from the chemical flocculation system to pH > 7.0 without the need for supplemental addition of neutralising agents such as sodium hydroxide. This in itself provides a significant economic incentive for implementation of the process. Kinetic analysis of the biological process carried out under controlled laboratory conditions using a Bioflo 3000 continuous fermentor showed that the bio-chemical process followed substrate inhibition kinetics. An appropriate kinetic model was identified to represent the behaviour of the substrate degradation system, and modified by inclusion of a pseudo toxic concentration to account for the effect of pH inhibition upon the biological growth rate. The process was verified both at pilot plant scale and at demonstration plant scale at an operational wool scour. The demonstration plant was of sufficient size to handle the full heavy effluent flow-down from a small wool scour. At the time of publishing three full-scale effluent treatment systems based on this research had been sold to both domestic and international clients of ADM Group Ltd. who funded the research.
APA, Harvard, Vancouver, ISO, and other styles
9

Edwards, Justin Kenneth. "Reed bed systems for the treatment of wastewaters and for sludge dewatering." Thesis, University of Birmingham, 1999. http://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.343453.

Full text
APA, Harvard, Vancouver, ISO, and other styles
10

Brown, Jonathan Jed 1964. "Halophytes for the treatment of saline aquaculture effluent." Diss., The University of Arizona, 1998. http://hdl.handle.net/10150/282715.

Full text
Abstract:
The discharge of untreated aquaculture effluent can pollute receiving water bodies. I tested the feasibility of using salt-tolerant plants (halophytes) with potential as forage and oilseed crops, as biofilters to treat saline aquaculture effluent. Plants were grown in draining lysimeters in greenhouses and irrigated with effluent salinized with NaCl. Irrigation water came from a recirculating tilapia culture system. I measured yield potential, water use and capacity for nitrogen and phosphorus uptake. In Experiment 1, Suaeda esteroa, Salicornia bigelovii and Atriplex barclayana (Chenopodiaceae) were grown in sand in 0.02 m³ lysimeters. Plants were irrigated with effluent of 0.5 ppt, 10 ppt and 35 ppt salinity, to meet evapotranspiration demand and to allow 30% of the applied water to leach past the plant root zone. Despite the high leaching fraction and short residence time of water in the pots, the plant-soil system removed 98% and 94% of the applied total and inorganic nitrogen, respectively, and 99% and 97% of the applied total and soluble reactive phosphorus respectively. For all species, salt inhibited (P ≤ 0.05) the growth rate, nutrient removal, and volume of water the plants could process. The salt marsh species S. esteroa and S. bigelovii performed better than the desert saltbush, A. barclayana, at 35 ppt. In Experiment 2, Suaeda esteroa, was grown in lysimeters containing approximately 0.8 m³ sandy loam soil and irrigated three times per week with 31 ppt NaCl effluent. I used five irrigation treatments, ranging in volume from 50 to 250% of the potential evaporation rate. Plant biomass and water consumption increased significantly (P ≤ 0.05) with increasing irrigation volume. Nitrate concentrations in water draining from the lysimeters decreased during the experiment, and were significantly lower in the high-volume treatments than in the low-volume treatments. Phosphorus concentrations in the leachate water increased during the experiment as a function of increasing irrigation volume. Irrigating halophyte crops with aquaculture wastewater of seawater-salinity may be a viable strategy for disposal of effluent.
APA, Harvard, Vancouver, ISO, and other styles
More sources

Books on the topic "Effluent Treatment Plant Sludge"

1

Berndt, Marian P. Sources and distribution of nitrate in ground water at a farmed field irrigated with sewage treatment-plant effluent, Tallahassee, Florida. Tallahassee, Fla: Dept. of the Interior, U.S. Geological Survey, 1990.

Find full text
APA, Harvard, Vancouver, ISO, and other styles
2

Tarmohamed, Yasmin. Ontario municipal sewage treatment plants mass balance project: Report-- metals. [S.l.]: MISA Advisory Committee, 1990.

Find full text
APA, Harvard, Vancouver, ISO, and other styles
3

Ioannidis, K. I. A computer program to estimate the heavy metals concentrations and partitioning in treated sludge and effluent of municipal sewage treatment plants. Manchester: UMIST, 1993.

Find full text
APA, Harvard, Vancouver, ISO, and other styles
4

Srinivas, C. TBP production plant effluent treatment process. Mumbai: Bhabha Atomic Research Centre, 2004.

Find full text
APA, Harvard, Vancouver, ISO, and other styles
5

Gray, T. W. Effluent treatment plant for Britoil's Nigg Terminal. London: Institute of Petroleum, 1985.

Find full text
APA, Harvard, Vancouver, ISO, and other styles
6

Hood, Gwendolyn D. Dewatering of waste effluent from a tile manufacturing plant. Washington, D.C. (2401 E St., N.W., MS #9800, Washington 20241-0001): U.S. Dept. of the Interior, Bureau of Mines, 1991.

Find full text
APA, Harvard, Vancouver, ISO, and other styles
7

Hood, Gwendolyn D. Dewatering of waste effluent from a tile manufacturing plant. Washington, DC: U.S. Dept. of the Interior, Bureau of Mines, 1991.

Find full text
APA, Harvard, Vancouver, ISO, and other styles
8

India. Ministry of Environment and Forests. and National Environmental Engineering Research Institute., eds. Common effluent treatment plant: State-of-the-art. Nagpur, India: National Environmental Engineering Research Institute, 1992.

Find full text
APA, Harvard, Vancouver, ISO, and other styles
9

Federation, Water Environment. Wastewater treatment plant design. Alexandria, VA: Water Environment Federation, 2003.

Find full text
APA, Harvard, Vancouver, ISO, and other styles
10

Higgs, Thomas W. AMD treatment plant sludge: Chemical stability and disposal considerations. S.l: s.n, 1990.

Find full text
APA, Harvard, Vancouver, ISO, and other styles
More sources

Book chapters on the topic "Effluent Treatment Plant Sludge"

1

Patil, Uday Singh, S. P. Raut, and Mangesh V. Madurwar. "Development of Sustainable Brick Using Textile Effluent Treatment Plant Sludge." In Recent Trends in Construction Technology and Management, 185–99. Singapore: Springer Nature Singapore, 2022. http://dx.doi.org/10.1007/978-981-19-2145-2_15.

Full text
APA, Harvard, Vancouver, ISO, and other styles
2

Ashok Kumar, V. T., P. T. Ravichandran, and P. R. Kannan Rajkumar. "Use of Textile Effluent Treatment Plant Sludge as Sustainable Material in Brick Manufacturing." In Advances in Intelligent Systems and Computing, 283–91. Singapore: Springer Singapore, 2018. http://dx.doi.org/10.1007/978-981-13-2182-5_27.

Full text
APA, Harvard, Vancouver, ISO, and other styles
3

Rai, Ashita, and M. H. Fulekar. "Wastewater Treatment: Common Effluent Treatment Plant—Case Study." In Bioremediation Technology, 267–84. Boca Raton : CRC Press, [2020]: CRC Press, 2020. http://dx.doi.org/10.1201/9780429296031-14.

Full text
APA, Harvard, Vancouver, ISO, and other styles
4

Siddiqui, Mohd Imran, Izharul Haq Farooqi, Hasan Rameez, and Farrukh Basheer. "Enhanced Biogas Production from Treatment Plant Sludges." In Management of Wastewater and Sludge, 233–56. Boca Raton: CRC Press, 2023. http://dx.doi.org/10.1201/9781003202431-13.

Full text
APA, Harvard, Vancouver, ISO, and other styles
5

Kobe, Jiei, Mohamad Danial Shafiq, Rosnani Alkarimiah, Abu Zahrim Yaser, Hafiza Shukor, and Muaz Mohd Zaini Makhtar. "Overview of Sludge in Waste Treatment Plant." In Microbial Fuel Cell (MFC) Applications for Sludge Valorization, 1–22. Singapore: Springer Nature Singapore, 2023. http://dx.doi.org/10.1007/978-981-99-1083-0_1.

Full text
APA, Harvard, Vancouver, ISO, and other styles
6

Subhawong, S. "Effluent Treatment at the Pasminco Clarksville Zinc Plant." In Lead-Zinc 2000, 865–78. Hoboken, NJ, USA: John Wiley & Sons, Inc., 2013. http://dx.doi.org/10.1002/9781118805558.ch59.

Full text
APA, Harvard, Vancouver, ISO, and other styles
7

Liebminger, Lorenzo Antonio, Sriman Narayanan, and Josef Lahnsteiner. "Pengerang PETRONAS Refinery Effluent Treatment Plant, Case Study Malaysia." In Handbook of Water and Used Water Purification, 1–18. Cham: Springer International Publishing, 2023. http://dx.doi.org/10.1007/978-3-319-66382-1_175-1.

Full text
APA, Harvard, Vancouver, ISO, and other styles
8

Patel, Nital, Jayesh Ruparelia, and Jayesh Barve. "Soft Sensor for TSS in Effluent of Primary Clarifier of Industrial Effluent Treatment Plant." In Smart Technologies for Energy, Environment and Sustainable Development, 455–63. Singapore: Springer Singapore, 2019. http://dx.doi.org/10.1007/978-981-13-6148-7_45.

Full text
APA, Harvard, Vancouver, ISO, and other styles
9

Okeke, Nonso Evaristus, Charles Oluwaseun Adetunji, Wilson Nwankwo, Kingsley Eghonghon Ukhurebor, Ayodeji Samuel Makinde, and Deepak G. Panpatte. "A Critical Review of Microbial Transport in Effluent Waste and Sewage Sludge Treatment." In Microbial Rejuvenation of Polluted Environment, 217–38. Singapore: Springer Singapore, 2021. http://dx.doi.org/10.1007/978-981-15-7459-7_10.

Full text
APA, Harvard, Vancouver, ISO, and other styles
10

Flower, P. R. A. "Case Study: Faure Water Treatment Plant Potable Water Treatment and Sludge Handling." In Chemical Water and Wastewater Treatment V, 399–412. Berlin, Heidelberg: Springer Berlin Heidelberg, 1998. http://dx.doi.org/10.1007/978-3-642-72279-0_32.

Full text
APA, Harvard, Vancouver, ISO, and other styles

Conference papers on the topic "Effluent Treatment Plant Sludge"

1

Koralewska, Ralf. "SYNCOM-Plus: An Optimized Residue Treatment Process." In 17th Annual North American Waste-to-Energy Conference. ASMEDC, 2009. http://dx.doi.org/10.1115/nawtec17-2375.

Full text
Abstract:
In a large-scale pilot plant, studies on wet-mechanical treatment of bottom ash using the SYNCOM-Plus process were carried out by MARTIN GmbH in the SYNCOM waste-to-energy plant in Arnoldstein, Austria (approx. 11000 kg/h waste throughput). Granulate of > 2 mm and fine fraction of < 5 mm were produced by dry screening, washing and wet screening. Additionally, sludge was separated from the wash water. The fine fraction and sludge as well as the boiler ash were recirculated into the furnace. In conclusion, the SYNCOM-Plus process meets all requirements which need to be complied with in an optimized and effluent-free commercial residue treatment process for the recovery of industrial products. This paper documents successful continuous operation of the SYNCOM-Plus process in direct connection with bottom ash discharge as well as the effects on combustion, flue gas composition and residue qualities.
APA, Harvard, Vancouver, ISO, and other styles
2

Ashby, Jim, and Tony Sobkowicz. "Field Testing Improves Citrus Plant Biological Treatment." In ASME 2002 Citrus Engineering Conference. American Society of Mechanical Engineers, 2002. http://dx.doi.org/10.1115/cec2002-4804.

Full text
Abstract:
Wastewater from citrus processing contains high levels of sugars, suspended solids, and caustic cleaning agents. Biological treatment is the only economical process for removing and neutralizing all of these contaminants, and the activated sludge process is the workhorse of the biological treatment stable. The biological treatment system must produce a treated effluent of the highest quality, regardless of the wild variation in flow and composition of the influent. Problems in the treatment process can almost always be traced to either a wastewater loading that is higher than the system can tolerate, or a failure to maintain and operate the treatment system to realize its treatment potential. A thorough review of the operational and loading characteristics of the system will determine whether excessive loading or inadequate treatment system is responsible for the system failure. When the problem has been identified, it can be resolved in one of three ways: □ A new treatment system of greater capacity can be installed to replace the inadequate system. □ The wastewater loading, hydraulic and organic, can be reduced through changes in fruit processing practices. □ Changes in the existing treatment system (equipment or operational) can be identified to increase its capacity. Paper published with permission.
APA, Harvard, Vancouver, ISO, and other styles
3

Aadhil, M. F. H. M., K. K. D. I. K. Gunaratne, A. M. U. Dananjina, and S. A. S. Perera. "Conversion of textile industry Effluent Treatment Plant sludge into a valuable organic fertilizer using Delta-D technology." In 2017 Moratuwa Engineering Research Conference (MERCon). IEEE, 2017. http://dx.doi.org/10.1109/mercon.2017.7980449.

Full text
APA, Harvard, Vancouver, ISO, and other styles
4

Sanchez, Edgar N., Jean-F. Beteau, Gilberto Vera, and Catherine Cadet. "Fuzzy supervisory control and substrate addition to improve effluent quality in an activated sludge wastewater treatment plant." In 2003 European Control Conference (ECC). IEEE, 2003. http://dx.doi.org/10.23919/ecc.2003.7085329.

Full text
APA, Harvard, Vancouver, ISO, and other styles
5

Flouret, Julie, Yves Barré, Hervé Muhr, and Edouard Plasari. "Design and Implementation of an Intensified Coprecipitation Reactor for the Treatment of Liquid Radioactive Wastes." In ASME 2013 15th International Conference on Environmental Remediation and Radioactive Waste Management. American Society of Mechanical Engineers, 2013. http://dx.doi.org/10.1115/icem2013-96033.

Full text
Abstract:
The coprecipitation is a robust and inexpensive process for the treatment of important volumes of low and intermediate radioactive level liquid wastes. Its major inconvenient is the huge volume of sludge generated. The purpose of this work is to optimize the industrial coprecipitation continuous process by achieving the following objectives: - maximize the decontamination efficiency; - minimize the volume of sludge generated by the process; - reduce the treatment cost decreasing the installation volume. An innovative reactor with an infinite recycling ratio was therefore designed. It is a multifunctional reactor composed of two zones: a perfectly mixed precipitation zone and a classifier to perform liquid-solid separation. The experiments are focused on the coprecipitation of strontium by barium sulphate. The effluent containing sulphate ions and the barium nitrate solution are injected in the reaction zone where strontium and barium coprecipitate as sulphates. The produced solid phase is returned into the reaction zone by the classifier and goes out slowly from the reactor bottom with a residence time much higher than the liquid phase. This creates both a high concentration of solid phase in the reaction zone and a high efficiency of decontamination. The experimental conditions simulate the industrial effluents. The total treatment flow rate is 17 L/h, with an effluent flow rate of 16 L/h and a reactive flow rate of 1 L/h, hence a mean residence time of 10 minutes. In these experimental conditions, the molar ratio sulphate/barium after mixing corresponds to 4.9. These conditions are used in the reprocessing plant of La Hague. The decontamination factor reached in these experimental conditions is excellent: DF = 1500. The decontamination factor obtained with the classical continuous process is only equal to 60. Different process parameters are studied in order to optimize the reactor/classifier: residence time, barium nitrate flow rate and racking flow rate. The decrease of barium nitrate flow rate reduces the volume of sludge generated by the process keeping a high efficiency of strontium decontamination: DF = 400. An excess of sulphate is necessary to perform an efficient decontamination, but the molar ratio sulphate/barium can be reduced to 3 instead of 4.9 used industrially. The reactor/classifier also represents an efficient device for the coprecipitation process intensification. Indeed, it can sensibly reduce the final installation size while treating important volume of effluents. This innovative reactor optimizes both the decontamination efficiency of radioactive liquid wastes and the reduction of sludge volume. A reduction of sulphate ions in the discharge is also possible, which is environmentally friendly.
APA, Harvard, Vancouver, ISO, and other styles
6

Burin, Eduardo, Fabiana de Marqui Mantovan, Leandro Rogel Silva, Cristian Giliard Zapalai, Erick Cardoso Costa, Fabio Antonio Xavier, and Edson Bazzo. "Analysis of corrosion and fouling development in a biomass steam generator burning sludge from a slaughterhouse effluent treatment plant." In 19th Brazilian Congress of Thermal Sciences and Engineering. ABCM, 2022. http://dx.doi.org/10.26678/abcm.encit2022.cit22-0280.

Full text
APA, Harvard, Vancouver, ISO, and other styles
7

Ribeiro, A., J. Araújo, A. Mota, R. Campos, C. Vilarinho, and J. Carvalho. "Decontamination of Heavy Metals From Municipal Sewage Sludge (MSS) by Electrokinetic Remediation." In ASME 2019 International Mechanical Engineering Congress and Exposition. American Society of Mechanical Engineers, 2019. http://dx.doi.org/10.1115/imece2019-11221.

Full text
Abstract:
Abstract A large quantity of sludges resulting from the treatment of MWWTP (Municipal Wastewater Treatment Plant) effluent is generated annually following the increase of population density and acceleration of urbanization. Sludge production in Europe has been predicted by around 12 million tons in 2020. As a solid waste, appropriate disposal of Municipal Sewage Sludge (MSS) has been taken seriously due to its larger volume and toxic substances such as heavy metals. Electrokinetic remediation has more advantages in heavy metals uptake compared to other technologies, due to the ability to treat soils in-situ and to remove heavy metals from soils. In this work, it was studied the remediation of MSS by the electrokinetic remediation coupled with activated carbon (AC) as a permeable reactive barrier (PRB). It was applied an electric current of 3 V cm−1 and it was used an AC/sludge ratio of 30 g kg−1 of contaminated sludge for the preparation of the PRB. In each trial, the evolution of cadmium (Cd), lead (Pb), copper (Cu), chromium (Cr), nickel (Ni) and zinc (Zn) removal from the sludge were evaluated. Results proved that this process is perfectly suited for the removal of chromium, nickel and zinc metals from the sludge. At the end of the operation time, it was achieved a maximum removal rate of 56% for chromium, 73% for nickel and 99% for zinc, with initial concentrations of 2790 mg kg−1, 2840 mg kg−1, and 94200 mg kg−1, respectively. Based on these results, it was proved the technical viability of the proposed technology (electrokinetic with AC as a permeable reactive barrier) to treat municipal sewage sludges.
APA, Harvard, Vancouver, ISO, and other styles
8

Li-juan, Wang, and Chen Chao-bo. "Support Vector Machine Applying in the Prediction of Effluent Quality of Sewage Treatment Plant with Cyclic Activated Sludge System Process." In 2008 IEEE International Symposium on Knowledge Acquisition and Modeling Workshop (KAM 2008 Workshop). IEEE, 2008. http://dx.doi.org/10.1109/kamw.2008.4810572.

Full text
APA, Harvard, Vancouver, ISO, and other styles
9

Rajamani, Sengoda Gounder, and Arnold Mulder. "Ecological Friendly Production Process and Waste Treatment for Circular Economy in Leather Tanning Industries." In The 9th International Conference on Advanced Materials and Systems. INCDTP - Leather and Footwear Research Institute (ICPI), Bucharest, Romania, 2022. http://dx.doi.org/10.24264/icams-2022.iv.11.

Full text
Abstract:
Ecological friendly processes with recovery of salt, chemicals and water for reuse in the tanning process as well as from liquid and solid waste are necessary for the promotion of circular economy.Recent developments in cleaner production and treatment process by reducing volume of effluent and pollution discharges, recovery of quality salt in the segregated streams such as saline soak liquor, spent chrome liquor and adoption of advanced aerobic oxidation process in the treatment system resulted in the recovery of purified salt, quality chromium and water for reuse. The achievements of innovative cleaner production and effluent treatment for promotion of circular economy are: Reduction in water usage in soaking process from 6000-8000 liters to less than 3000 liters/ ton of hides, Separate treatment of saline streams and recovery of quality salt, chromium in the form of cake / powder and Replacement of physiochemical treatment into biological treatment reduction in chemical usage and sludge generation by more than 60%. Viable cleaner production and sustainable treatment technologies had been engineered and are being implemented in many major leather clusters and Common Effluent Treatment Plants.
APA, Harvard, Vancouver, ISO, and other styles
10

Santin, Ignacio, Ramon Vilanova, Marian Barbu, and Carles Pedret. "Manipulating the sludge flow to increase methane production and to reduce effluent pollution in wastewater treatment plants." In 2016 24th Mediterranean Conference on Control and Automation (MED). IEEE, 2016. http://dx.doi.org/10.1109/med.2016.7535996.

Full text
APA, Harvard, Vancouver, ISO, and other styles

Reports on the topic "Effluent Treatment Plant Sludge"

1

LUECK, K. J. Waste Treatment Plant Liquid Effluent Treatability Evaluation. Office of Scientific and Technical Information (OSTI), June 2001. http://dx.doi.org/10.2172/807138.

Full text
APA, Harvard, Vancouver, ISO, and other styles
2

LUECK, K. J. WASTE TREATMENT PLANT (WTP) LIQUID EFFLUENT TREATABILITY EVALUATION. Office of Scientific and Technical Information (OSTI), October 2004. http://dx.doi.org/10.2172/834437.

Full text
APA, Harvard, Vancouver, ISO, and other styles
3

Flaherty, Julia, Ernest Antonio, Carolyn AM Burns, Richard Daniel, and Jennifer Yao. Hanford Waste Treatment Plant Effluent Management Facility Stack Effluent Monitoring Sampling Probe Location Qualification Evaluation. Office of Scientific and Technical Information (OSTI), April 2022. http://dx.doi.org/10.2172/1880068.

Full text
APA, Harvard, Vancouver, ISO, and other styles
4

Wempner, P. J., and J. K. Prazniak. Evaluation of iron in the steam plant wastewater treatment facility effluent. Office of Scientific and Technical Information (OSTI), December 1994. http://dx.doi.org/10.2172/137444.

Full text
APA, Harvard, Vancouver, ISO, and other styles
5

Kim, Byung J., and Richard Shanley. Development of a Wastewater Treatment Plant (WWTP) Sludge (Biosolids) Management Strategy. Fort Belvoir, VA: Defense Technical Information Center, July 1997. http://dx.doi.org/10.21236/ada329279.

Full text
APA, Harvard, Vancouver, ISO, and other styles
6

RUTHERFORD WW, GEUTHER WJ, STRANKMAN MR, CONRAD EA, RHOADARMER DD, BLACK DM, and POTTMEYER JA. SLUDGE TREATMENT PROJECT PHASE 1 SLUDGE STORAGE OPTIONS ASSESSMENT OF T PLANT VERSUS ALTERNATE STORAGE FACILITY. Office of Scientific and Technical Information (OSTI), April 2009. http://dx.doi.org/10.2172/952592.

Full text
APA, Harvard, Vancouver, ISO, and other styles
7

MacDonald, James D., Aharon Abeliovich, Manuel C. Lagunas-Solar, David Faiman, and John Kabshima. Treatment of Irrigation Effluent Water to Reduce Nitrogenous Contaminants and Plant Pathogens. United States Department of Agriculture, July 1993. http://dx.doi.org/10.32747/1993.7568092.bard.

Full text
Abstract:
The contamination of surface and subterranean drinking water supplies with nitrogen-laden agricultural wastewater is a problem of increasing concern in the U.S. and Israel. Through this research, we found that bacteria could utilize common organic wastes (e.g. paper, straw, cotton) as carbon sources under anaerobic conditions, and reduce nitrate concentrations in wastewater to safe levels. Two species of bacteria, Cellulomonas uda and a Comamonas sp., were required for dentitrification. Celulomonas uda degraded cellulose and reduced nitrate to nitrite. In addition, it excreted soluble organic carbon needed as a food source by the Comamonas sp. for completion of denitrification. We also found that recirculated irrigation water contains substantial amounts of fungal inoculum, and that irrigating healthy plants with such water leads to significant levels of root infection. Water can be disinfected with UV, but our experiments showed that Hg-vapor lamps do not possess sufficient energy to kill spores in wastewater containing dissolved organics. Excimer lasers and Xenon flashlamps do possess the needed power levels, but only the laser had a high enough repetition rate to reliably treat large volumes of water. Ozone was highly efficacious, but it's use as a water treatment is probably best suited to moderate or low volume irrigation systems. This research provides critical data needed for the design of effective water denitrification and/or pathogen disinfection systems for different growing operations.
APA, Harvard, Vancouver, ISO, and other styles
8

Hastings, R. L. Idaho Chemical Processing Plant Liquid Effluent Treatment and Disposal Facility hot test report. Office of Scientific and Technical Information (OSTI), September 1993. http://dx.doi.org/10.2172/10136140.

Full text
APA, Harvard, Vancouver, ISO, and other styles
9

Flaherty, Julia, and Ernest Antonio. Hanford Waste Treatment Plant LAB Facility Stack Effluent Monitoring - Sampling Probe Location Qualification Evaluation. Office of Scientific and Technical Information (OSTI), July 2021. http://dx.doi.org/10.2172/1814642.

Full text
APA, Harvard, Vancouver, ISO, and other styles
10

Flaherty, Julia, and Ernest Antonio. Hanford Waste Treatment Plant LAB Facility Stack Effluent Monitoring - Sampling Probe Location Qualification Evaluation. Office of Scientific and Technical Information (OSTI), February 2022. http://dx.doi.org/10.2172/1872735.

Full text
APA, Harvard, Vancouver, ISO, and other styles
You might also be interested in the extended bibliographies on the topic 'Effluent Treatment Plant Sludge' for particular source types:
Journal articles Dissertations / Theses Books
We offer discounts on all premium plans for authors whose works are included in thematic literature selections. Contact us to get a unique promo code!

To the bibliography