Relevant bibliographies by topics / Full scale plant

Academic literature on the topic 'Full scale plant'

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Published: 14 March 2023

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Journal articles on the topic "Full scale plant"

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Henket, Frans. "Testing Polymers at Full Plant Scale." Opflow 13, no. 11 (November 1987): 4–5. http://dx.doi.org/10.1002/j.1551-8701.1987.tb00467.x.

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Elnour, Mariam, Nader Meskin, Khlaed M. Khan, Raj Jain, Syed Zaidi, and Hammadur Siddiqui. "Full-Scale Seawater Reverse Osmosis Desalination Plant Simulator." IFAC-PapersOnLine 53, no. 2 (2020): 16561–68. http://dx.doi.org/10.1016/j.ifacol.2020.12.780.

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Eng, A. Pearce C., G. Long, and Lingley Mere. "DAVYHULME WwTW PILOT VERSUS FULL SCALE BAFF PLANT." Proceedings of the Water Environment Federation 2000, no. 13 (January 1, 2000): 130–44. http://dx.doi.org/10.2175/193864700784607730.

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Christensen, Niels Peter, F. Dalhoff, O. Biede, and M. Noer. "Full-scale CCS demo plant at Nordjyllandsværket, Denmark." IOP Conference Series: Earth and Environmental Science 6, no. 17 (February 1, 2009): 172014. http://dx.doi.org/10.1088/1755-1307/6/17/172014.

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Yu, Y. H., and K. S. L. Lo. "A Pilot-Plant Study to Salvage a Full-Scale Treatment Plant." Water Science and Technology 25, no. 1 (January 1, 1992): 93–98. http://dx.doi.org/10.2166/wst.1992.0014.

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Kwei-Shan Wastewater Treatment Plant is the second oldest treatment plant ever designed and operated in Taiwan, to treat the combined industrial wastewater collected from various kinds of factories located in Kwei-Shan Industrial Park. From the beginning the treatment plant has been suffering from influents containing a spectrum of various pollutants harmful to the activated-sludge system of the plant. Extreme pH measurements (1.4-12.0), jumpy organic contents (COD 104-6660 mg/l), high metal concentrations (Cu up to 19 mg/l, Zn up to 37 mg/l), and high grease concentrations (up to 470 mg/l) were unbelievably found in tne plant influents, while a traditional plain primary settling tank was the only shield to protect the aeration basin from damage. In a dilemma like this, a pilot-plant study was undertaken to save the efficiency of the existing biological treatment plant from those various fatal influent constituents. A flow equalization tank and a chemical treatment unit were first built to damp out pH and COD variations, Ca(OH)2 was added to remove the toxic metals as well as part of the grease. The effluent after the above treatment was then neutralized and sent to the downscaled activated sludge system containing one aeration tank and one settling tank. The results indicated that equalization and chemical precipitation by using the existing space of the roughing filter and the sedimentation tank could produce much safer influents to the activated sludge system.
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Stenström, F., and J. la Cour Jansen. "Impact on nitrifiers of full-scale bioaugmentation." Water Science and Technology 76, no. 11 (August 31, 2017): 3079–85. http://dx.doi.org/10.2166/wst.2017.480.

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Abstract Nitrifiers are the slowest growing bacteria used in conventional biological wastewater treatment. Furthermore, their growth rate is seriously hampered by low temperature. As a result, the volume needed for nitrification dominates the volume of the biological reactors at a wastewater treatment plant. As a way of enhancing nitrification and reducing this volume, bioaugmentation can be used. Nitrifiers from a side-stream plant can be inoculated to the mainstream process, which is thereby boosted. The effect of bioaugmentation can be measured in different ways. This full-scale study focuses on the effect of bioaugmentation from a microbial point of view by using 16S rRNA amplicon sequencing. The study reveals how bioaugmentation increases the diversity of nitrifiers in the mainstream process and in the side-stream plant; that the abundance of nitrifiers is increased in the mainstream process; the interaction between nitrifiers from the side-stream plant and mainstream process; and the effect of bioaugmentation on nitrifying genera and species over time. To our knowledge, this detailed microbial information on nitrifying species during a full-scale bioaugmentation study has not been presented before.
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ten Brummeler, E. "Full scale experience with the BIOCEL process." Water Science and Technology 41, no. 3 (February 1, 2000): 299–304. http://dx.doi.org/10.2166/wst.2000.0084.

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The BIOCEL process is a mesophilic dry anaerobic batch digestion system for solid organic wastes. In the BIOCEL process organic solid wastes, such as source separated organic fraction of MSW (biowaste) is converted into enriched compost and biogas. In the process net energy production is achieved by converting the biogas to heat and power with a heat-electric power production unit. In September 1997 the first full scale plant is started-up in Lelystad, The Netherlands. This plant is processing 50,000 tons of biowaste (organic fraction of MSW from source separation) per year. The plant has a net energy production and therefore contributes to prevention of CO2 emissions from fossil fuels. In the BIOCEL-system the several compost fractions are produced with a “wet” separation process. During the wet separation sand and contaminants are removed. An important aspect of compost quality is the absence of several types of pathogens. It appears that anaerobic digestion with the BIOCEL- process results in complete inactivation of several important groups of plant and animal pathogens. The mechanism that causes the inactivation is not yet fully understood, but the relatively high Volatile Fatty Acids concentration during the first two weeks of the digestion process might presumably be the key factor.
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Qamar, Mohd Obaid, Izharul Haq Farooqi, Faris M. Munshi, Abdullah H. Alsabhan, Mohab Amin Kamal, Mohd Amir Khan, and Aisha Saleh Alwadai. "Performance of full-scale slaughterhouse effluent treatment plant (SETP)." Journal of King Saud University - Science 34, no. 3 (April 2022): 101891. http://dx.doi.org/10.1016/j.jksus.2022.101891.

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Boulenger, P., W. Driessen, E. van de Werfhorst, and M. Tielbaard. "Anaerobic effluent treatment by a pilot and full-scale plant at a chemical industrial complex." Water Science and Technology 42, no. 5-6 (September 1, 2000): 283–87. http://dx.doi.org/10.2166/wst.2000.0525.

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To test the feasibility of anaerobic treatment of an effluent from a chemical factory producing intermediates for synthetic fibres, test work with a 45 l UASB pilot plant was conducted. Following its successful operation, a full-scale anaerobic effluent treatment plant including a 400 m3 combined pre-acidification tank and a 990 m3 Biopaq®-UASB reactor was constructed. The results of the pilot plant and the full-scale anaerobic treatment plant have been compared, similarities and differences in performance are presented and evaluated. COD removal efficiencies above 80% and BOD efficiencies in excess of 85% achieved in the pilot trial were confirmed by the full-scale installation. Overall process design as well as operational data from the pilot trial and the full-scale plant is presented. Despite the differences in configuration, operational results of the full-scale plant are comparable to the results obtained from the pilot plant study making such a pilot plant a useful tool for the process design of an full-scale anaerobic effluent treatment plant.
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Bosander, J., and Å. D. Westlund. "Operation of full-scale fluidized bed for denitrification." Water Science and Technology 41, no. 9 (May 1, 2000): 115–21. http://dx.doi.org/10.2166/wst.2000.0184.

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The SYVAB company has extended the plant with a fluidized bed for post denitrification. The method was chosen mainly for two reasons. First, the relatively low investment cost and second, the flexibility in the process to adjust the discharged nitrogen according to the circumstances in the recipient. Start-up took place in April 1997 with an adaption period of four weeks. From mid September the same year the plant has been in full denitrifying operation. The average nitrate-nitrogen reduction rate has been 90% with 1.9 mg NO3–N in the outlet. Methanol is used as external carbon source. At the present purification rate the cost for total nitrogen reduction is 18 SEK (2.25 USD)/kg N.
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Dissertations / Theses on the topic "Full scale plant"

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Lau, Yip Hang. "Maximization of treatment capacity of a full-scale biological nitrogen removal plant through model simulation and full-scale stress test /." View abstract or full-text, 2005. http://library.ust.hk/cgi/db/thesis.pl?EVNG%202005%20LAU.

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Hercules, Selwyn Mark. "Full scale demonstration of filamentous bulking control at a biological nutrient removal activated sludge plant." Master's thesis, University of Cape Town, 2002. http://hdl.handle.net/11427/5040.

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Alajmi, Hasan Mubarak. "Effect of physical, chemical and biological treatment on the removal of five pharmaceuticals from domestic wastewater in laboratory-scale reactors and full-scale plant." Thesis, University of Newcastle upon Tyne, 2014. http://hdl.handle.net/10443/2469.

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Pharmaceuticals and their metabolites are known to enter the environment from the effluent of wastewater treatment plants. From statistical analysis on the usage of pharmaceuticals, and their effects on the environment, five pharmaceuticals were selected for this study (Metronidazole, Trimethoprim, Sulphamethoxazole, Paracetamol and Ranitidine). Trace concentrations of pharmaceuticals were determined using a sensitive analytical method, comprising solid phase extraction (SPE) and liquid chromatography with a mass spectrometry detector (LC- MS),operating in selected ion monitoring (SIM) mode. It was found that Metronidazole, Trimethoprim, Sulphamethoxazole, Paracetamol and Ranitidine were detected at the highest levels in the wastewater entering the Sulaibiya WWTP Kuwait, with concentrations of up to 58 ng.L , 1814 ng.L , 1669 ng.L , 2086 ng.L and 2009 -1 ng.L , respectively. High removal efficiencies of these pharmaceuticals were found in the Sulaibiya WWTP. One year study was conducted to investigate the occurrence, persistence and fate of a range of these pharmaceuticals at different sampling points at the Sulaibiya WWTP. The treatment processes consisted of screening, grit removal and diffused air activated sludge treatment (primary and secondary treatment), followed by microfiltration (MF), reverse osmosis (RO), and chlorine oxidation (tertiary treatment). During primary and secondary treatment, Metronidazole, Trimethoprim, Sulphamethoxazole, Paracetamol and Ranitidine were removed efficiently with average removals efficiencies of 83.4%, 86.1%, 77.5%, 97.5% and 77.5%, respectively. The RO system lowered these pharmaceuticals further, giving overall removal efficiencies of 97%, 99%, 99%, 100% and 100% for Metronidazole, Trimethoprim, Sulphamethoxazole, Paracetamol and Ranitidine, respectively. All selected pharmaceuticals were tested in laboratory scale reactors to assess their -1 removal by chlorination and ozonation, and results showed that 10 mg.L of chlorine -1 removed these pharmaceuticals better than 15 mg.L of ozone. Lab-scale aerobic reactors (2 L), seeded with activated sludge inoculum from the Sulaibiya WWTP and fed with different concentrations of pharmaceuticals (0.1, 1 and -1 10 mg.L ), spiked individually into a synthetic wastewater showed that the TOC could be removed efficiently without inhibition by these pharmaceuticals. The fate of Metronidazole, Trimethoprim, Sulphamethoxazole, Paracetamol and Ranitidine was investigated in a membrane bioreactors (MBR), and a sequencing batch reactors (SBR), operating under strictly aerobic, and anoxic/aerobic conditions at different concentrations of a pharmaceutical mixture (PM) of the same -1 -1 -1 pharmaceuticals (1 µg.L , 1 mg.L and 10 mg.L ). The COD and TOC removal -1 efficiency decreased when the PM concentration was increased to 10 mg.L . The removal of Metronidazole and Trimethoprim was moderately effective, and similar in all the reactors. Sulphamethoxazole and Paracetamol were removed efficiently, but -1 this decreased when the PM was increased to 10 mg.L for most of the reactors, whilst Ranitidine experienced high removal rates at all concentrations in all the reactors. Analysis of the microbial diversity in laboratory reactors treating pharmaceuticals wastewater showed decreases in microbial community diversity when the PM concentration was increased. Pure cultures of bacteria isolated on selected pharmaceutical growth media were also detected in the microbial communities of reactor sludge by performing polymerase chain reaction–denaturing gradient gel electrophoresis (PCR-DGGE).
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Belia, Evangelia. "Phosphorus release during treatment of sludge derived from a bench-scale EBPR plant." Thesis, University of Strathclyde, 2002. http://digitool.lib.strath.ac.uk:80/R/?func=dbin-jump-full&object_id=28864.

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This thesis describes the development of enhanced biological phosphorus removal (EBPR) in a lab-scale sequencing batch reactor (SBR) and the release of phosphorus during the storage and thickening of sludge produced in this reactor. In the first phase of the experimental work a fast start-up method for EBPR development was established by the addition of a pure culture of Acinetobacter lwoffi to a conventional activated sludge. Investigations revealed that the performance EBPR depended on the combination of influent COD and phosphorus values and that in the investigated range, EBPR functioned independently of the sludge retention time. Low dissolved oxygen levels had no effect on the phosphorus removal properties of the sludge. The second phase of the experimental work involved the investigation of the phosphorus released during sludge handling. It was found that phosphorus resolubilisation during sludge treatment took place in three distinct phases which included an initial period of extremely low phosphorus release. Alterations of the reactor influent and operational parameters and the sludge characteristics, affected the amount of phosphorus released during anaerobic storage and gravity thickening. It was found that for short retention times in the sludge processing units (1-48 hours), decreasing the influent phosphorus concentration, increasing the oxidised nitrogen content of the excess sludge and wasting the excess sludge from the aeration tank decreased the amount of phosphorus resolubilised. For longer retention times (2-7 days), it was found that increasing the influent COD, having a lower total phosphorus sludge content, higher sludge "stabilisation" rates and quiescent conditions of storage, decreased the amount of phosphorus released.
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Nägele, Hans-Joachim [Verfasser], and Thomas [Akademischer Betreuer] Jungbluth. "A full-scale study on efficiency and emissions of an agricultural biogas plant / Hans-Joachim Nägele. Betreuer: Thomas Jungbluth." Hohenheim : Kommunikations-, Informations- und Medienzentrum der Universität Hohenheim, 2013. http://d-nb.info/1045663751/34.

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Wilhelmsson, Ella. "Investigations of the Effects of Lowering the Temperature in Full Scale Mesophilic Biogas Digesters at a Wastewater Treatment Plant." Thesis, Linköpings universitet, Tema Miljöförändring, 2020. http://urn.kb.se/resolve?urn=urn:nbn:se:liu:diva-167059.

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This thesis has investigated the effects of running the two full scale biogas digesters at Slottshagen wastewater treatment plant at 34 °C compared to 37 °C, in terms of process stability, biogas production and energy savings with the aim of saving energy and money by not heating the digesters as much. The main objective was to investigate whether it is at all possible to operate the biogas process at 34 °C or if the process becomes inhibited or otherwise unstable. If the process could be operated at 34 °C it might mean savings of both energy and money, provided that there is still a sufficient production of biogas.The experiment lasted for three months and investigated the short-term effects of the reduction of temperature. The process was monitored closely, and samples from the reactors were collected and analysed twice a week to ensure the stability of the biogas process. Several parameters were monitored online, the biogas production and methane content amongst others. Other parameters were calculated, such as the degree of degradation and specific methane production. This was done to ensure process stability and a sufficient production of biogas. The energy balance was calculated to evaluate if energy was saved by lowering the temperature in the digesters.The results show that the biogas process does remain stable at 34 °C while still producing a satisfactory amount of biogas during the short time of the experiment. Calculations show that both energy and money has been saved during the experiment. However, the system is largely dependent on seasonal variations, therefore further studies over a longer time period would be desirable. During the course of the thesis it has also become evident that the biogas process at Slottshagen is irregular in several aspects, and that it would be beneficial to even the process out, especially with regards to the hydraulic retention time. Making the process more even would enable further improvements to be made and simplify interpretations and comparisons of processstability data.
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Pratt, John Graham le Maistre. "Application of the Fourier-Mellin transform to translation-, rotation- and scale-invariant plant leaf identification." Thesis, McGill University, 2000. http://digitool.Library.McGill.CA:80/R/?func=dbin-jump-full&object_id=33440.

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The Fourier-Mellin transform was implemented on a digital computer and applied towards the recognition and differentiation of images of plant leaves regardless of translation, rotation or scale. Translated, rotated and scaled leaf images from seven species of plants were compared: avocado ( Persea americana), trembling aspen (Populus tremuloides), lamb's-quarter (Chenopodium album), linden (Tilla americana), silver maple (Acer saccharinum), plantain (Plantago major) and sumac leaflets (Rhus typhina ). The rate of recognition was high among translated and rotated leaf images for all plant species. The rates of recognition and differentiation were poor, however, among scaled leaf images and between leaves of different species. Improvements to increase the effectiveness of the algorithm are suggested.
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Zimmerman, Cory Tyler. "Performance Analysis and Modeling of Pavements with a Cold Central Plant Recycled Base under Accelerated Loading Testing." Thesis, Virginia Tech, 2017. http://hdl.handle.net/10919/79131.

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Cold Central Plant Recycling (CCPR) has been used by many state highway agencies to save material, money, time, and energy in pavement construction and rehabilitation. The objectives of this thesis were to: (1) perform an instrumented verification analysis, (2) evaluate the response and performance of two pavement configurations with a CCPR base layer through accelerated pavement testing (APT), and (3) construct models using mechanistic-empirical pavement design software for comparison with the APT results. The pavement configurations featured a 5-inch CCPR mixture with either a 3-inch or 1.5-inch SM-9.5D surface mixture. Each section was instrumented with strain gauges, pressure cells, and thermocouples. A heavy vehicle simulator (HVS) was used to load three replicate test sections in each lane, with the temperature controlled at 39°C at a depth of 1.5 inches. Results from the instrument verification analysis showed that the strain gauges and pressure cells used in the experiment recorded pavement responses with a high degree of repeatability. In addition, the loading condition variables (speed, wheel load, and tire inflation pressure) affected the response following the expected trends and did not affect the repeatability of the instruments. The average CV of all strain gauge and pressure cell signals was approximately 0.009 or 0.9%, and 0.004 or 0.4%, respectively. In terms of the rutting comparison, the sections with the 3-inch surface layer outperformed the sections with the thinner 1.5-inch surface layer. However, the age of the pavement at the start of testing significantly affected the rutting performance. After adjusting for the pavement age at the time of testing, the section with the thicker surface showed approximately half of the rutting of the section with the thinner surface. The results from preliminary ME Design analysis indicate that the software cannot model the studied APT sections using the default material properties and calibration factors available at the time of analysis. In particular, the software does not seem to be prepared to model the CCPR materials.
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Christensen, Erik Niels. "Plans and specifications for a full-scale towing model validation experiment." Thesis, Monterey, California. Naval Postgraduate School, 1989. http://hdl.handle.net/10945/26167.

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Venkatesan, Luke. "The development of frother optimisation techniques in full scale flotation plants." Master's thesis, University of Cape Town, 2013. http://hdl.handle.net/11427/5386.

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In 2012, Anglo American Platinum assembled a technical task team of metallurgists for their concentrator operations. Although there has been extensive research in literature regarding the flotation response and behaviour of reagents, there still exists a gap between fundamental laboratory scale research and plant scale application. This thesis will focus on the development of techniques for optimising and characterising frother on a full scale plant using the Anglo American Platinum Bubble Sizer (AAPBS) which is a commonly used tool by the plant metallurgist. The techniques developed have been based on the application of fundamental research of frothers in literature. This thesis consists of three main focus areas: 1) Developing a technique for measuring the relationship between sauter mean bubble diameter and frother concentration on a full scale plant. 2) Developing a technique for estimating frother concentrations in process streams in full scale plant 3) Establishing whether the relationship between sauter mean bubble diameter and superficial gas velocity in a flotation bank of identical cells in series in a plant operating at frother concentration above the CCC is identical, and whether this can be used to detect the decrease of frother concentration to below the CCC at any point in the bank. Furthermore, the metallurgical performance of a bank with a decrease in frother concentration below the CCC midway through the bank was determined before and after the addition of frother, which was added as such that all the cells in the bank operate with a frother concentration above the CCC. There were two techniques investigated for measuring the relationship between sauter mean bubble diameter and frother concentration. Both techniques involved using the AAPBS and the use of forced air mechanically agitated tank cells. Technique 1 involved using the first rougher cell on a flotation plant, dosing frother at different rates into the cell to target different frother concentrations and then measuring the resultant bubble size whilst operating at a fixed air rate. The coalescence mechanism here was occurring in a three phase solids/aqueous/air system occurring in a continuous stirred tank. Similarly Technique 2 involved using the first rougher cell; however, the first cell was depleted of frother by bypassing the frother dosage line into the next cell. This was done to isolate the first rougher cell and to minimise disturbance to the rest of the rougher bank. Known concentrations offrother were made up in potable water and these were added into the AAPBS. Bubbles from the pulp phase enter the bubble riser tube which is long and narrow (3m x 25mm diameter) which is representative of two phase aqueous/air “plug flow” system. These bubbles coalesce to different degrees based on the known frother concentration. The resulting bubble size distribution was then be measured by taking photographs at the viewing pane of the AAPBS. The air rate in the cell was kept constant to within 0.7-0.9 cm/s and the photographs were analysed using software provided by stone three to determine the sauter mean bubble diameter and the bubble size distribution. Technique 1 was applied to Plant A UG2 concentrator which was using a polyglycol type frother called Betafroth 206C which has an undisclosed composition and a molecular weight of approximately 200 g/mol. The first rougher cell used was an Outokumpu 70 m3 forced air mechanically agitated tank cell. The results showed no clear relationship between sauter mean bubble diameter and frother concentration. Furthermore, the sauter mean bubble diameter was already very small and it appeared that the changes in between runs were more strongly linked to the superficial gas velocity than frother concentration. The fact that the sauter mean bubble diameter obtained was already small implied that the frother concentration in the cell was already high. This could have been due to an additional source of frother due to spillage or in the process water that potentially elevated the actual frother concentrations in the cell. Technique 1 also resulted in significant disturbances to the entire rougher bank because it involved changing the frother dosages to the bank. This would affect the flotation performance of the bank for a prolonged period and affect plant performance. Hence it was decided that technique 1 would not be suitable.
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Books on the topic "Full scale plant"

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New York State Energy Research and Development Authority., Fredonia (N Y. ), and O'Brien & Gere., eds. Full-scale demonstration of selector contact stabilization process Village of Fredonia Wastewater Treatment Plant: Final report. Albany, N.Y: The Authority, 1999.

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1928-, Kaufman Albert, and United States. National Aeronautics and Space Administration, eds. Develop and test fuel cell powered on site integrated total energy systems: Phase III, full-scale power plant development : 18th quarterly report, August-October 1985. [Washington, D.C: National Aeronautics and Space Administration, 1985.

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Truppi, Lawrence E. EPA complex terrain model development: Description of a computer data base from the Full Scale Plume Study, Tracy Power Plant, Nevada. Research Triangle Park, NC: U.S. Environmental Protection Agency, Atmospheric Sciences Research Laboratory, 1987.

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Troxel, S. W. Observations of plume dispersion in complex terrain by NOAA lidar during the 1984 Full Scale Plume Study at Tracy Power Plant. Boulder, Colo: U.S. Dept. of Commerce, National Oceanic and Atmospheric Administration, Environmental Research Laboratories, 1986.

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), Rosendale (N Y. Full-scale demonstration of selector-contact stabilization process at Town of Rosendale Wastewater Treatment Plant, Ulster County, New York: Final report. Albany, N.Y: New York State Energy Research and Development Authority, 2005.

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Pearl, Mike. Review of pilot and full scale soil washing plants. Abingdon: National Environmental Technology Centre, 1994.

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Canada Centre for Mineral and Energy Technology. Economic analysis of a demonstration-scale ethanol plant in Gatineau, Quebec. Ottawa, Ont: Efficiency and Alternative Energy Technology Branch, Energy, Mines and Resources Canada, 1992.

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Christensen, Erik Niels. Plans and specifications for a full-scale towing model validation experiment. Springfield, Va: Available from the National Technical Information Service, 1989.

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Mangs, Johan. Full-scale fire experiments on vertical and horizontal cable trays. Espoo, [Finland]: Technical Research Centre of Finland, 1997.

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Mangs, Johan. Full-scale fire experiments on vertical and horizontal cable trays. Espoo, [Finland]: Technical Research Centre of Finland, 1997.

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Book chapters on the topic "Full scale plant"

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Flintsch, Gerardo, Wenjing Xue, Brian Diefenderfer, and Fabrizio Meroni. "Evaluation of Cold Central-Plant Recycling (CCPR) Technique Using Full-Scale Accelerated Pavement Testing." In Lecture Notes in Civil Engineering, 270–79. Cham: Springer International Publishing, 2020. http://dx.doi.org/10.1007/978-3-030-55236-7_28.

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Szpyrkowicz, L., and S. N. Kaul. "Biochemical Removal of Nitrogen from Industrial Effluents: A Full Scale Plant Performance and Stability." In New Horizons in Biotechnology, 271–84. Dordrecht: Springer Netherlands, 2003. http://dx.doi.org/10.1007/978-94-017-0203-4_25.

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Wood-Black, Frankie. "Considerations for Scale-Up – Moving from the Bench to the Pilot Plant to Full Production." In ACS Symposium Series, 37–45. Washington, DC: American Chemical Society, 2014. http://dx.doi.org/10.1021/bk-2014-1163.ch003.

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Kim, Guehee, Kohei Nakajima, Takayuki Tatekawa, Naoya Teshima, Yoshio Suzuki, and Hiroshi Takemiya. "Full-Scale 3D Vibration Simulator of an Entire Nuclear Power Plant on Simple Orchestration Application Framework." In High Performance Computing on Vector Systems 2010, 93–106. Berlin, Heidelberg: Springer Berlin Heidelberg, 2010. http://dx.doi.org/10.1007/978-3-642-11851-7_7.

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Abid, Sami, Maroua Haddad, and Hassib Bouallagui. "Intermittent Aeration and Oxygen Flowrate Monitoring for Nitrogen Removal Enhancement in a Full-Scale Wastewater Treatment Plant." In Advances in Science, Technology & Innovation, 161–64. Cham: Springer International Publishing, 2022. http://dx.doi.org/10.1007/978-3-031-00808-5_38.

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Gibb, W. H., A. R. Jones, and F. Wigley. "The UK Collaborative Research Programme on Slagging in Pulverised Coal Furnaces: Results of Full-Scale Plant Trials." In The Impact of Ash Deposition on Coal Fired Plants, 3–18. Boca Raton: Routledge, 2022. http://dx.doi.org/10.1201/9780203736616-2.

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Aspegren, Henrik, Bengt Andersson, and Erik Arvin. "The Use of Factorial Designs to Identify Factors Affecting Particulate Removal in a Full Scale Tertiary Precipitation Plant with Flotation." In Chemical Water and Wastewater Treatment III, 19–28. Berlin, Heidelberg: Springer Berlin Heidelberg, 1994. http://dx.doi.org/10.1007/978-3-642-79110-9_2.

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Jafarinejad, Shahryar. "Comparison of the Full-Scale Municipal Wastewater Treatment Plant Designs Consisting of Modified Bardenpho Process with and Without Membrane Bioreactor for Nutrient Removal: Cost Analysis." In Sustainable Development of Water and Environment, 47–63. Cham: Springer International Publishing, 2021. http://dx.doi.org/10.1007/978-3-030-75278-1_5.

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Quentmeier, V., and M. Saake. "Consulting, Construction and Operating Results of a Full-Scale Biotechnological Plant for the Oxidation of Iron and Manganese with Simultaneous Elimination of Volatile Chlorinated Hydrocarbons from Ground Water." In Contaminated Soil ’90, 1157–59. Dordrecht: Springer Netherlands, 1990. http://dx.doi.org/10.1007/978-94-011-3270-1_264.

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Rodriguez-Mozaz, Sara, Daniel Lucas, and Damià Barceló. "Full-Scale Plants for Dedicated Treatment of Hospital Effluents." In The Handbook of Environmental Chemistry, 189–208. Cham: Springer International Publishing, 2017. http://dx.doi.org/10.1007/698_2017_13.

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Conference papers on the topic "Full scale plant"

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Al-Musleh, Essa, Mohamed Hussein, Mary Katebah, and Zineb Bouabidi. "Detailed exergy analysis of full scale LNG plant." In Qatar Foundation Annual Research Conference Proceedings. Hamad bin Khalifa University Press (HBKU Press), 2018. http://dx.doi.org/10.5339/qfarc.2018.eepd1131.

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Siddiqui, Hammad, Mariam Elnour, Nader Meskin, and Syed Zaidi. "Full-Scale Seawater Reverse Osmosis Desalination Plant Simulator." In Qatar University Annual Research Forum & Exhibition. Qatar University Press, 2020. http://dx.doi.org/10.29117/quarfe.2020.0067.

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Reverse Osmosis (RO) is an efficient and clean membrane-based technology for water desalination. This work presents a full-scale seawater reverse osmosis (SWRO) desalination plant simulator using MATLAB/Simulink that has been validated using the operational data from a local plant. It allows simulating the system behavior under different operating conditions with high flexibility and minimal cost.
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Naik, S., B. Stephan, and M. Henze. "GT36 Turbine Development and Full-Scale Validation." In ASME Turbo Expo 2021: Turbomachinery Technical Conference and Exposition. American Society of Mechanical Engineers, 2021. http://dx.doi.org/10.1115/gt2021-59470.

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Abstract This paper describes the full-scale turbine section validation of the GT36 heavy duty gas turbine, which was conducted in a test Power Plant in Birr, Switzerland. The GT36 Test Power Plant is extensively instrumented with both standard and specialised instrumentation. In the turbine section, specialised instrumentation includes metal and gas thermocouples, thermal paint, pressure sensors, hot gas rakes, strain gauges, five-hole probes, pyrometers and tip timing sensors. Similar specialised instrumentation also exists for the compressor, combustor and the rotor sections. Three major test campaigns were conducted over an extended period, which consisted of both long and short duration tests, including a range of off-design tests. Within the turbine section, detailed transient and steady-state measurements were obtained of the stage inlet pressures and temperatures, airfoil surface pressures and metal temperatures. These measurements indicated that both the aerodynamic and cooling performances of the turbine blades and vanes are highly consistent and repeatable over a range of operating conditions. Detailed comparisons of the measured engine pressures and temperatures with predictions also indicated that there was generally a very good match in the Mach numbers and metal temperatures for all the turbine blades and vanes.
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Lobarev, Alexey, Denis Plotnikov, George Chukov, Vladimir Potapov, Alexander Nikulin, and Anatoly Kurilov. "Testing System Development for Full-Scale Simulators of Nuclear Power Plant Unit." In 2022 Moscow Workshop on Electronic and Networking Technologies (MWENT). IEEE, 2022. http://dx.doi.org/10.1109/mwent55238.2022.9802215.

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Ruiz Lozano, Oscar, Alejandro Acero Oliete, Pedro López Julián, and Beniamino Russo. "Results of a full-scale model of a macrophyte wastewater treatment plant." In Proceedings of the 39th IAHR World Congress From Snow to Sea. Spain: International Association for Hydro-Environment Engineering and Research (IAHR), 2022. http://dx.doi.org/10.3850/iahr-39wc2521711920221112.

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Jianwei Liu and Wenlin Ma. "Odor and VOCs treatment from wastewater treatment plant using a full-scale biofilter." In 2011 International Conference on Business Management and Electronic Information (BMEI). IEEE, 2011. http://dx.doi.org/10.1109/icbmei.2011.5914235.

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van Heek, A. I. "ACACIA: A Small Scale Nuclear Power Plant With Cogeneration Capabilities." In ASME Turbo Expo 2002: Power for Land, Sea, and Air. ASMEDC, 2002. http://dx.doi.org/10.1115/gt2002-30512.

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Nuclear power currently only serves the market segment of large scale base load electricity generation. Other energy markets, like cogeneration and heat production or market segments like the smaller scale (but still industrial) electricity production are entirely served with fossil fuels (and hydropower). When these fuels at acceptable prices are being depleted and if actively marketed, and if an inherently safe small-scale nuclear plant could be developed and marketed, a huge market could emerge for this new form of nuclear power. Pebble Bed High Temperature Reactor technology is most suitable for designing small inherently safe nuclear reactors. The oldest small designs were meant for application as district heating plants, making full use of the self-controlling features of nuclear reactors. The ACACIA concept (AdvanCed Atomic Cogenerator for Industrial Applications) is a design for industrial cogeneration, producing 13.6 MW of electricity and 17 tons of industrial quality steam per hour, with a total efficiency of 63%. In case the electricity production would be maximized at the expense of the steam quality, an electrical output of 16.5 MW could be achieved, and the plant efficiency would rise to 86% (electric efficiency 41%). The heat source is a pebble bed reactor with 40 MW of thermal power. The energy conversion system is a direct recuperated helium cycle with a radial compressor and an axial helium turbine. A number of operational and safety related transients have been calculated with two different simulation codes. The safety related transient analyses show the reactor power and the fuel temperature bebaviour after a full loss of coolant accident, and illustrate the inhrently safe nature of the plant. The operational transient simulations show the suitability of the system for an industrial user. Furthermore, the transport of radioactive fission products within the primary circuit has been analyzed. A cost study shows high kWh-costs compared to large scale generating plants, but the treatment of scaling factors for this particular case needs continued attention. However, for those areas in the world without fossil fuel supply networks and with only small-scale demand, ACACIA will still be an economic option. To improve matching with non-utility market needs, the current ACACIA design will be adapted from a direct cycle system to an indirect cycle system, where primary cycle will be strictly separated from the remainder of the plant. A conceptual comparison with the direct cycle system will be discussed.
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Giust, Flavio D., Peter Grimm, and Rakesh Chawla. "Experimental Comparisons of 3D Reconstructed Pin-Power Distributions in Full-Scale BWR Fuel Assemblies." In 18th International Conference on Nuclear Engineering. ASMEDC, 2010. http://dx.doi.org/10.1115/icone18-29691.

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In this paper, reconstructed local fission rates obtained with the two-group nodal diffusion program PRESTO-2, used at the Leibstadt Nuclear Power Plant (KKL) in Switzerland, are compared with experimental results and MCNPX calculations. The experimental facility consists of a test zone, where the measurements are made, surrounded by a buffer zone and two driver zones that render the system critical and also contain the control rods. The test zone consists of a tank that contains a 3×3 array of BWR fuel assemblies of type SVEA-96+. Four cases are considered, all corresponding to a 1.23 m high active zone moderated with light water at room temperature: 1) axially uniform enrichment and gadolinium content, 2) like case 1 but with a L-shaped control blade completely inserted, 3) enrichment and gadolinium content change at the core mid-plane, 4) like case 2 but with the control blade partially inserted. The comparisons give insight into the accuracy of the pin power reconstruction methodology. The axially uniform case without control blade shows a good radial agreement and a well predicted axial curvature of the flux. On the other hand, systematic deviations are observed in the radial direction for the controlled cases, with the axial heterogeneities causing deviations around the discontinuity and also in the axial curvature of the flux.
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Kameda, Hiroyuki, Masaki Nakagawa, Akira Shibuya, Shiro Fukunishi, and Katsumi Ebisawa. "Seismic Safety Margin Assessment for NPP Utilizing Full-Scale Tests: Overview." In ASME 2010 Pressure Vessels and Piping Division/K-PVP Conference. ASMEDC, 2010. http://dx.doi.org/10.1115/pvp2010-25253.

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Seismic safety margin assessment is discussed for structural systems and components of nuclear power plants (NPP). Emphasis is placed on utilizing full-scale test results. This paper presents an overview of the ongoing project at Japan Nuclear Energy Safety Organization (JNES). It proposes a conceptual framework of the issue, and provides a basis for the three companion papers that will present application examples on actual NPP equipments. Discussion is focused on 1) motivation of the project arising from the Kashiwazaki-Kariwa NPP earthquake experience in 2007, 2) problem identification with varying targets (verification of experienced plant performance, seismic risk assessment, etc.), 3) formulation of seismic safety margin, 4) needs for realistic assessment of seismic safety margin by incorporating full-scale test results, and 5) activities of the JNES project.
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O, AUGUSTINE, and PETER OJO. "The Impact of Alum on the Bulking of a Full Scale Activated Sludge Plant." In Fourth International Conference on Advances in Bio-Informatics and Environmental Engineering - ICABEE 2016. Institute of Research Engineers and Doctors, 2016. http://dx.doi.org/10.15224/978-1-63248-100-9-57.

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Reports on the topic "Full scale plant"

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Gaskill, J. R., D. E. Larson, and G. P. Abrigo. Hanford Waste Vitrification Plant full-scale feed preparation testing with water and process simulant slurries. Office of Scientific and Technical Information (OSTI), March 1996. http://dx.doi.org/10.2172/560886.

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OBrien, Kevin, Yongqi Lu, Jason Dietsch, Zhenxing Zhang, Cole Maas, Timothy Thomas, Keisuke Iwakura, et al. Full-scale FEED Study for Retrofitting the Prairie State Generating Station with an 816 MWe Capture Plant using Mitsubishi Heavy Industries Post-Combustion CO2 Capture Technology. Office of Scientific and Technical Information (OSTI), August 2022. http://dx.doi.org/10.2172/1879443.

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Ruff, D. T. Phase III (full scale) agitated mixing test plan. Office of Scientific and Technical Information (OSTI), October 1994. http://dx.doi.org/10.2172/10191584.

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Klote, John H. Project plan for full scale smoke movement and smoke control tests. Gaithersburg, MD: National Bureau of Standards, 1988. http://dx.doi.org/10.6028/nbs.ir.88-3800.

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Gambill, J. B. Dynamic out-of-plane and in-plane testing of full-scale hollow clay tile infilled frames. [Final report]. Office of Scientific and Technical Information (OSTI), December 1994. http://dx.doi.org/10.2172/419321.

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Steven A. Benson, Charlene R. Crocker, Kevin C. Galbreath, Jay R. Gunderson, Mike J. Holmes, Jason D. Laumb, Michelle R. Olderbak, et al. PILOT-AND FULL-SCALE DEMONSTRATION OF ADVANCED MERCURY CONTROL TECHNOLOGIES FOR LIGNITE-FIRED POWER PLANTS. Office of Scientific and Technical Information (OSTI), February 2004. http://dx.doi.org/10.2172/836113.

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Steven A. Benson, Charlene R. Crocker, Kevin C. Galbreath, Jay R. Gunderson, Michael J. Holmes, Jason D. Laumb, Jill M. Mackenzie, et al. PILOT-AND FULL-SCALE DEMONSTRATION OF ADVANCED MERCURY CONTROL TECHNOLOGIES FOR LIGNITE-FIRED POWER PLANTS. Office of Scientific and Technical Information (OSTI), February 2005. http://dx.doi.org/10.2172/840345.

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Osborn, Douglas, and Matthew Solom. Terry Turbopump Expanded Operating Band Full-Scale Component and Basic Science Detailed Test Plan - Final. Office of Scientific and Technical Information (OSTI), February 2017. http://dx.doi.org/10.2172/1367492.

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Osborn, Douglas, and Matthew Solom. Terry Turbopump Expanded Operating Band Full-Scale Integral Long-Term Low-Pressure Experiments ? Preliminary Test Plan. Office of Scientific and Technical Information (OSTI), November 2018. http://dx.doi.org/10.2172/1482781.

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Solom, Matthew, Kyle Ross, Jeffrey N. Cardoni, and Douglas Osborn. Terry Turbopump Expanded Operating Band Full-Scale Component and Basic Science Detailed Test Plan-Revision 2. Office of Scientific and Technical Information (OSTI), August 2017. http://dx.doi.org/10.2172/1399210.

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