Relevant bibliographies by topics / Dewatering

Academic literature on the topic 'Dewatering'

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Published: 4 June 2021
Last updated: 10 March 2023

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Journal articles on the topic "Dewatering"

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Pan, Jill Ruhsing, Chihpin Huang, Minyih Cherng, Kung-Cheh Li, and Cheng-Fang Lin. "Correlation between dewatering index and dewatering performance of three mechanical dewatering devices." Advances in Environmental Research 7, no. 3 (May 2003): 599–602. http://dx.doi.org/10.1016/s1093-0191(02)00052-7.

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Alimohammadi, M., H. A. Tackley, C. B. Lake, I. Spooner, T. R. Walker, R. Jamieson, C. Gan, and K. Bossy. "Effect of different sediment dewatering techniques on subsequent particle sizes in industrial derived effluent." Canadian Journal of Civil Engineering 47, no. 10 (October 2020): 1145–53. http://dx.doi.org/10.1139/cjce-2019-0269.

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A paucity of literature has compared geotextile dewatering methods to more conventional dewatering methods (i.e., centrifuge, sedimentation) in the context of how geotextile dewatering performs at reducing particulate matter in dewatering effluent. Particulate matter is the primary source of inorganic and organic contaminants (i.e., dioxins and furans) in an unconsolidated sediment (estimated 577 000 m3) that has accumulated in a wastewater stabilization basin in Nova Scotia, Canada. Physical and chemical properties of contaminated sediment were initially characterized, and subsequent laboratory experiments were carried out for three common dewatering methods: sedimentation, centrifugation, and geotextile filtration. Filtrate quality of suspended solids (number, particle size distribution of particles) was examined for differences based on three dewatering techniques assessed. All three methods provided effective removal of particulate matter during dewatering, but geotextile dewatering could be a more cost-effective and practical solution for dewatering of these sediments.
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BARTHES, H., A. BORDAS, D. BOUILLOT, M. BUZON, P. DUMONT, J. FERMIN, J. C. LANDRY, et al. "TUNNELS - DEWATERING." Proceedings of the Institution of Civil Engineers - Civil Engineering 102, no. 5 (May 1994): 26–29. http://dx.doi.org/10.1680/icien.1994.26806.

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Keller, Karsten, and Werner Stahl. "Vibration dewatering." Chemical Engineering and Processing: Process Intensification 33, no. 5 (November 1994): 331–36. http://dx.doi.org/10.1016/0255-2701(94)02004-3.

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LIU, HONGHAI, XIAOKAI ZHANG, and JINGWEN ZHANG. "STUDY OF DEWATERING CHARACTERISTICS OF EUCALYPTUS WOOD BY SUPERCRITICAL CO2." WOOD RESEARCH 67(6) 2022 67, no. 6 (December 13, 2022): 908–18. http://dx.doi.org/10.37763/wr.1336-4561/67.6.908918.

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Wood collapse is a major defect for their applications in solid wood production. Supercritical CO2(ScCO2) dewatering can quickly remove water in wood and effectively reduce the capillary tension leading to collapse of wood structure. In this study, Eucalyptus exsertaF.V. Muellwoodwas dewatered using ScCO2at 35,45,55°Cand 15,20,25 MPa, separately. The dewatering characteristics and wood deformationwere statistically analyzed and compared after dewatering. The results show that the dewatering rateof ScCO2isaffected by moisture content (MC)of wood, showing the higher the MC, the faster the dewatering. Itisalso affected significantly by pressure, indicating increased dewatering ratewith thepressure. The effect of temperature on dewatering rate is not apparent as the pressure is less than 25MPa, but it becomes significantat 25MPacondition, showing an increased dewatering rate with temperature. In this experiment, the greatest dewatering rate was 19.8%·h-1at 55°Cand 25MPa. The transversal shrinkage of all specimens after 5 cycles dewatering waslower than1.5%, indicating the ScCO2dewatering could effectively inhibit collapse of eucalyptus wood structure. Thetransversal shrinkage decreases with the pressure, and is not affected significantly by temperature.
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IWAI, Shigerhisa, Tadao KUROKAWA, and Hideki FUZII. "Sludge dewatering by multi rotating disc dewatering machines." Journal of Environmental Conservation Engineering 18, no. 10 (1989): 635–39. http://dx.doi.org/10.5956/jriet.18.635.

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Muralidhara*, H. S., H. Hampel**, and H. Kröoening***. "DEWATERING OF HAMBURG'S DREDGED MATERIAL BY ELECTROACOUSTIC DEWATERING." Drying Technology 6, no. 3 (September 1988): 535–46. http://dx.doi.org/10.1080/07373938808916397.

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Yu, Xiao Yan, Su Li Zhi, Run Juan Wang, Shu Ting Zhang, and Xue Bin Lu. "Influence of Chemical Conditioning on Electroosmotic Dewatering Behavior for Activated Sludge." Advanced Materials Research 573-574 (October 2012): 126–30. http://dx.doi.org/10.4028/www.scientific.net/amr.573-574.126.

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Applying electroosmosis to sludge dewatering practically, methods for improving electroosmotic dewatering must be explored. The influence of initial pH, adding Al2 (SO4)3 dose and ash content in sludge on electroosmotic dewatering behavior was investigated. The results show that acid or alkaline environment is unfavorable for electroosmotic dewatering, especially initial pH of sludge closing to the isoelectric point, electroosmotic dewatering behaves worst. With increasing Al2(SO4)3 coagulant-aid dose, the decreasing rate of water content becomes slower gradually during electroosmotic dewatering. Besides, higher ash content in sludge has a better effect on vaccum filtration, but slightly impact on electroosmotic dewatering. When ash content increases to 69.9% from 52.4%, final water content reduces to 64.3% from 78.3% using vaccum filtration, and the decreasing amount of water content by electroosmotic dewatering ranges from 16.5% to 12.3%.
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Yang, Lin. "Effect of Temperature and Pressure of Supercritical CO2 on Dewatering, Shrinkage and Stresses of Eucalyptus Wood." Applied Sciences 11, no. 18 (September 18, 2021): 8730. http://dx.doi.org/10.3390/app11188730.

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Supercritical CO2 (SuCO2) dewatering can mitigate capillary tension and reduce wood collapse. In this study, Eucalyptus urophylla × E. grandis specimens were dewatered by SuCO2 at temperatures of 35, 40 and 55 °C, in pressures of 10 and 30 MPa, respectively, for 1h. Effects of temperature and pressure on dewatering rate, moisture content (MC) distribution and gradient, shrinkage and residual stress of wood after dewatering were investigated. The results indicate that the SuCO2 dewatering rate is much faster than that of conventional kiln drying (CKD). The dewatering rate increases with increasing of temperature and pressure; however, pressure has a significant influence, especially for the high-temperature dewatering process; the MC distribution after 1h dewatering is uneven and MC gradients decrease with reducing of mean final MC of wood. MC gradients along radial direction are much smaller than that in tangential direction; collapse of wood significantly reduces after dewatering due to SuCO2 decreasing the capillary tension, and residual stress of wood during dewatering is mainly caused by pressure of SuCO2, which decreases with increasing temperature. SuCO2 dewatering has great potential advantages in water-removal of wood prone to collapse or deformation.
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Avancini, Livia Luiza de Souza, Matheus Muller, and Delma de Mattos Vidal. "Application of polyelectrolytes for improving the dewatering performance of drinking water treatment sludge using geotextiles." Ambiente e Agua - An Interdisciplinary Journal of Applied Science 16, no. 5 (October 6, 2021): 1–14. http://dx.doi.org/10.4136/ambi-agua.2723.

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The sludge generated at drinking water treatment plants (WTPs) is a high-moisture content residue, and therefore difficult to handle, transport, dispose of or recover. During the last decades, geotextile tubes have been successfully applied to reduce the residue volume, facilitate its handling and subsequent reuse. This study aimed to understand the factors that interfere in the filtration and dewatering efficiencies and to experimentally analyze the dewatering process of WTPs sludge, evaluating different test procedures and investigating the influence of the type and dosage of polymeric additives on dewatering performance. Geotextile cone dewatering tests and geotextile bag dewatering tests were performed, using four different woven geotextile samples and an aluminum sulfate WTP sludge sample. The results showed that the use of geotextile cone dewatering tests for geotextile selection and for additive selection and dosage was representative for the dewatering process intended, reflecting the results verified in the geotextile bag dewatering tests. Sludge chemical conditioning increased dewatering rate and solids retention during the tests’ early stages, but it did not result in a higher final solids content sludge cake. Keywords: dewatering systems, geosynthetics, waste management.
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Dissertations / Theses on the topic "Dewatering"

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Basim, Gul Bahar Jr. "Fine Coal Dewatering." Thesis, Virginia Tech, 1997. http://hdl.handle.net/10919/35680.

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Fine coal constitutes a relatively small portion of a product stream in a coal cleaning plant. However, its processing cost is approximately three times higher than the cost of processing coarse coal. Therefore, many coal companies chose to discard the fines to refuse ponds, causing a loss of profit and creating environmental concerns. This problem can be solved by developing more efficient fine coal dewatering processes, since bulk of the cost associated with processing fine coal is due to dewatering. For this reason, Virginia Tech has developed new chemicals that can increase the efficiency of mechanically dewatering coal fines. To determine the performance of the novel reagents on fine coal dewatering, laboratory vacuum filtration and centrifugation tests were conducted. The utilization of the novel dewatering aids in the dewatering systems decreased the final moisture contents of the filter cakes to sufficiently low values. There was approximately 50% reduction in the cake moisture of many coal samples with the usage of the novel dewatering aids. The tests were performed on various coal samples from different coal preparation plants. This gave the advantage of testing the novel dewatering aids at many different conditions since each sample had its own characteristics. The vacuum filtration tests were extensively used to compare the efficiency of each novel reagent in dewatering. The best performing dewatering aids were determined and they were further utilized to analyze the effects of operational variables, such as; drying cycle time, cake thickness, vacuum pressure level and slurry temperature on dewatering. A statistical analysis was also performed to observe the effect of each factor quantitatively. The analyses were very useful in terms of determining the synergistic effects of these factors in dewatering of fine coal. The centrifuge tests were conducted to examine the efficiency of the novel reagents in a different dewatering application. The experimental results showed a significant improvement in centrifuge dewatering with the usage of proper coal sample. The moisture contents of fairly thick cakes decreased down to 5-10%. This outcome was very satisfactory since most of the dewatering aids commonly used in the coal industry were observed to increase the final cake moisture in centrifuge dewatering instead of decreasing it. Finally, surface chemistry analyses were performed on the coal samples and slurries to analyze the changes in the chemistry of the dewatering system in the presence of the novel dewatering aids. It was observed that there was a favorable improvement in the system chemistry, which was helpful in terms of decreasing the cake moisture content. These observations were also consistent with the results of the dewatering tests. The combined effect of the novel additives in decreasing the surface tension of the slurry and increasing the contact angle of the coal surface at the same time was concluded to be the reason for their significant performance as dewatering aids.
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Smyth, Ian Charles. "Cyclonic dewatering of oil." Thesis, University of Southampton, 1988. https://eprints.soton.ac.uk/411627/.

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Åslund, Peter. "On Suction Box Dewatering Mechanisms." Doctoral thesis, KTH, Fiber- och polymerteknik, 2008. http://urn.kb.se/resolve?urn=urn:nbn:se:kth:diva-4780.

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In previous studies on suction box dewatering, three mechanisms were identified that determine the dry content of a web, viz. web compression, displacement of water by air and rewetting. In the present work, the relative importance of the three mechanisms was investigated through direct measurement of the web deformation, the dry content changes during and after the suction pulse, the air flow through the fibre network and the saturation of the web after the suction pulse. Suction pressure, suction time and rewetting time were varied. The experiments were done with chemical and mechanical pulp webs of various grammages. It was found that a large web deformation took place during the suction pulse, particularly at its beginning. Compression dewatering was found to be the most dominant dewatering mechanism. Displacement dewatering started after most of the web compression had occurred. Its contribution to the increase in dry content was most pronounced for higher suction pressures, longer suction times and for chemical pulp webs. A surprisingly large expansion of the web was observed immediately after the suction pulse. This expansion was the effect of rewetting. This rewetting strongly reduced the dry content of the web if the web had not been immediately separated from the forming fabric at the end of the suction pulse. Under the conditions studied, the decrease in dry content amounted to the order of 3 to 6 %. Rewetting was smaller for longer suction times and higher suction pressures. A considerable air flow through the web occurred under these conditions. This air flow apparently moved water from the forming fabric into the suction box, thus making less water available for rewetting. Rewetting for mechanical pulp webs was more pronounced and took place faster than for chemical pulps. The use of a membrane on top of the web during suction box dewatering proved to be advantageous for reducing the air flow through the web. However, under the conditions investigated, the dry content could not be improved. Although the web compression was increased when using a membrane, especially at a higher suction pressure, rewetting after the suction pulse had an even larger negative impact on the dry content, which, as a result, was lower.
QC 20100924
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Usher, Shane Patrick. "Suspension dewatering : characterisation and optimisation /." Connect to thesis, 2002. http://eprints.unimelb.edu.au/archive/00000972.

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Ju, Shuohui. "Electroosmotic dewatering of bentonite suspensions." Thesis, McGill University, 1990. http://digitool.Library.McGill.CA:80/R/?func=dbin-jump-full&object_id=59868.

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Electroosmotic dewatering of Bentonite suspensions under conditions of constant DC voltage and constant DC current was investigated experimentally in a column 5 cm in diameter. The suspensions were prepared with CaCl$ sb2$ in distilled water with concentrations up to 1 M. The initial solid content was between 9.1 wt% and 26 wt% and the initial bed height ranged from 1.0 cm to 5.2 cm. Constant voltages from 4.0 V to 8.0 V and constant currents from 90 mA to 110 mA were used.
Electroosmosis removed 20-60% of the water with energy expenditures well below the energy required to vaporize the water. Higher voltages or currents removed more water. Removal rates were increased by the addition of CaCl$ sb2$. The lowest bed height (1 cm) gave the lowest energy of dewatering, but the final water removal was low. For constant voltage experiments with an initial field strength of 2.8 V/cm, bed heights around 2 cm gave the highest water removal. The initial solid content had little effect on the final solid content. The Helmholtz/Smoluchowski theory did not predict correctly the effects of electrolyte concentration, solid content and bed height on the rate of electroosmotic dewatering.
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Neeson, S. J. N. "New technologies in sludge dewatering." Thesis, Queen's University Belfast, 2012. http://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.546397.

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Bevan, Marc A. "Geoenvironmental impacts of construction dewatering." Thesis, University of Southampton, 2005. http://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.431942.

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Zhang, Yi. "Suspension dewatering with aggregate densification." Thesis, University of Manchester, 2014. https://www.research.manchester.ac.uk/portal/en/theses/suspension-dewatering-with-aggregate-densification(7599d818-8f26-4e2d-b80f-b4fa243dba52).html.

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This thesis concerns design of two pieces of suspension dewatering equipment (i.e. transient batch settlers and steady state continuous gravity thickeners). In a transient batch settler, very slow densification of aggregates within the suspension is considered whilst the drag on the solids in the suspension is assumed to be negligible. The interface of the suspension is then determined by a balance between gravity and the gradient of the compressive yield stress of the gelled suspension. The compressive yield stress functional form in general could be either a weakly gelled formula, or a strongly gelled formula. These formulae differ in the way they behave for solids concentrations in the neighbourhood of the suspension gel point. The effects of the above two gel formulae, the evolution of the compressive yield stress functional form over time during aggregate densification, different initial suspension heights, and different initial feed solids volume fractions upon the predictions of consolidated bed structures and solids volume fractions obtained at the bottom of a batch settler, and upon the evolution of the heights of the suspension and the consolidated bed have been explored. A sufficiently tall initial suspension height might lead to insignificant increases in the solids volume fractions obtained at the bottom of batch settlers after time-dependent aggregate densification. The interfaces of the suspension and the consolidation zone coincide after aggregate densification if the gel point, which increases with time, is larger than the initial feed solids volume fractions. Moreover, the maximum permitted underflow solids fluxes predicted from steady state thickeners have been investigated and compared. Pre-shearing of aggregates which densifies aggregates to have smaller diameters upon entering the thickener is necessary if large underflow solids fluxes and small underflow solids volume fractions are specified. The solids volume fraction at the top of the consolidated bed which is the densified gel point is influenced by the extent of pre-shearing of aggregates. An algorithm for determining this densified gel point has also been developed. In reality, thickeners contain not just a consolidating bed, but also a hindered settling region above it. When the hindered settling region is considered in a thickener, the effects of the extent of aggregate densification that has occurred in the hindered settling region and how that impacts upon thickener performance and sludge rheological properties have been explored in this thesis. A new algorithm for predicting the densified gel point obtained at the top of the consolidated bed has been developed when the hindered settling region is present. The effects of underflow solids volume fractions, aggregate densification rate parameters and pre-shearing of aggregates upon the predictions of maximum permitted underflow solids fluxes, sludge rheological properties, and thickener performance have been explored. The predictions of thickener performance using both the weakly and strongly gelled formulae have also been achieved. In cases where it is possible to neglect the hindered settling region, substantial increases in the maximum permitted underflow solids fluxes, and substantial decreases in the consolidated bed heights and the total solids residence times have been achieved after aggregate densification for a comparatively small underflow solids volume fraction. The benefits arising from aggregate densification are more modest if the underflow solids volume fraction is larger. On the other hand, when the hindered settling region is included, more densification of aggregates occurring in the hindered settling region might lead to taller consolidated bed heights for a specified suspension flux and a specified aggregate densification rate parameter due to higher underflow solids volume fractions.
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Astorsdotter, Jennifer. "Dewatering Cellulose Nanofibril Suspensions through Centrifugation." Thesis, KTH, Skolan för kemivetenskap (CHE), 2017. http://urn.kb.se/resolve?urn=urn:nbn:se:kth:diva-215079.

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Cellulose nanofibrils (CNF) is a renewable material with unique strength properties. A difficulty in CNF production is that CNF suspensions contain large amounts of water. If CNF suspension volume can be decreased by dewatering facilitated by centrifugation, then transportation costs and storage costs can be reduced. The aim of this thesis is to investigate the impact various parameters have on CNF centrifugation dewatering and identify optimal conditions for maximal water removal. A laboratory study was conducted using four materials; 2.0 w% enzymatically treated CNF (CNF1), 1.9 w% carboxymethylated CNF (CNF2) and two commercial samples (1.9 w% CNFA and 1.8 w% CNFB). The main method was analytical centrifugation up to 2330 g. Parameters tested were initial concentration before centrifugation, temperature, NaCl addition, pH, and applied solid compressive pressure (g-force and surface weight). In addition to centrifugation experiments the four materials were characterized with laser diffraction, UV-vis absorption, Dynamic light scattering, and dry weight measurements. Analysis of the experimental data collected show that increase in initial concentration give a higher final concentration, but less water is removed. Furthermore, temperature changes have no effect on separation of CNF and water. At an applied solid compressive pressure of 3 kPa and initial concentration at 1.5 w% the concentrations 5.5 w%, 1.5 w%, 4.0 w%, and 4.3 w% can be reach for CNF1, CNF2, CNFA, and CNFB respectively. After extrapolation of polynomial functions fitted to experimental data an applied solid compressive pressure of 22 kPa and initial concentration at 1:5 w%, the concentrations 9.1 w%, 1.5 w%, 6.9 w%, and 7.9 w% are predicted for CNF1, CNF2, CNFA, and CNFB respectively. The thickening of CNF suspensions achieved and predicted in this thesis implies possibilities for large amounts of water removal, e.g. the water content in a CNF1 suspension is reduced from 65.7 litres/kg CNF to 10.0 litres/kg CNF at the solid compressive pressure 22 kPa. The concentrations at 22 kPa are determined by extrapolation from experimental data <3 kPa solid compressive pressure. The carboxymethylated CNF2 can not be dewatered unless it is diluted or if salt or pH is adjusted. This is directly correlated to the electrostatic forces in the suspension and the Debye length. Addition of salt or lowered pH also eliminate any concentration gradients in diluted and centrifuged CNF2 suspensions.
Cellulosa nanofibriller (CNF) är ett förnybart material med unika styrkeegenskaper. En svårighet med produktion av CNF är att CNF suspensioner innehåller stora mängder vatten. Om volymerna av CNF suspensioner kan minskas med avvattning genom centrifugering, då kan transport- och lagerkostnader sänkas. Målet med det här examensarbetet är att undersöka vilken inverkan olika parametrar har på CNF-avvattning genom centrifugering och identifiera optimala förhållanden för maximalt avlägsnande av vatten. En laboratoriestudie utfördes på fyra olika material. De fyra materialen är 2 w% enzymatiskt behandlad CNF (CNF1), 1.9 w% karboxymetylerad CNF (CNF2) och två kommersiella prover (1.9 w% CNFA och 1.8 w% CNFB). Den huvudsakliga metoden var analytisk centrifugering upp till maximalt 2330 g. De testade parametrarna var initial koncentration innan centrifugering, temperatur, NaCl tillsats, pH, och applicerat fast kompressionstryck (g-kraft och ytvikt). Förutom centrifugeringsexperimenten så karaktäriserades the fyra mmaterialen med laser diffraktion, UV-vis absorption, dynamisk ljusspridning och vägningar av torrhalt. Analys av den experimentella data som insamlats visar att en ökad initial koncentration ger en högre slutkoncnentration, men mindre vatten kan bortföras. Temperaturförändringar har ingen effekt på separation av CNF och vatten. Vid ett applicerat fast kompressibelt tryck på 3 kPa och en initial koncentration 1.5 w% kan koncentrationerna 5.5 w%, 1.5 w%, 4.0 w%, och 4.3 w% nås för CNF1, CNF2, CNFA, och CNFB. Efter extrapolering av polynoma funktioner passad till experimentell data förutspås att koncentrationerna 9.1 w%, 1.5 w%, 6.9 w%, och 7.9 w% kan nås för CNF1, CNF2, CNFA, and CNFB vid 22 kPa och en initial koncentration på 1.5 w%. Förtjockningen av CNF suspensioner som kan, eller förutspås kunna nås genom centrifugering i det här examensarbetet innebär att det är möjligt att avlägsna stora mängder vatten, till exempel kan vatteninnehållet i CNF1 minskas från 65.7 liter/kg CNF till 10.0 liter/kg CNF vid 22 kPa fast kompressionstryck. Koncentrationerna vid 22 kPa fast kompressionstryck är extrapolerade från exprimentell data <3 kPa fast kompressionstryck. Den karboy- metylerade CNF2 kan inte avvattnas om den inte späds ut eller om salt eller pH justeras. Detta är direkt kopplat till de elektrostatiska krafterna i suspensionen och Debye längden. Tillsats av salt eller sänkt pH eliminerar också de koncentrationsgradienter som kan förekomma i utspädda centrifugerade CNF2 suspensioner.
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Grant, Christine Sharon. "Electro-osmotic dewatering of mineral ultrafines." Thesis, Georgia Institute of Technology, 1986. http://hdl.handle.net/1853/12117.

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Books on the topic "Dewatering"

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Dewatering biosolids. Lancaster, Pa: Technomic Pub., 1997.

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E, Albertson Orris, ed. Dewatering municipal wastewater sludges. Park Ridge, N.J., U.S.A: Noyes Data Corp., 1991.

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Aho, Martti. Artificial dewatering of peat. Espoo: Valtion teknillinen tutkimuskeskus, 1987.

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Dawdy, Blake F. Septage sludge dewatering feasibility study. [Toronto]: Environment Ontario, Research and Technology Branch, 1991.

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Smith, C. W. Well point dewatering of phosphatic clays. Washington, D.C: U.S. Dept. of the Interior, Bureau of Mines, 1989.

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Vandermeyden, Carel. Nonmechanical dewatering of water plant residuals. Denver, CO: AWWA Research Foundation and American Water Works Association, 1998.

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Mines, USDI Bureau of. Improved flocculation method for dewatering coal. S.l: s.n, 1985.

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Powers, J. Patrick. Construction dewatering: New methods and applications. 2nd ed. New York: Wiley, 1992.

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Parekh, B. K. Dewatering studies of fine clean coal. S.l: s.n, 1992.

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Center for Environmental Research Information (U.S.), ed. Design manual: Dewatering municipal wastewater sludges. Cincinanati, OH: U.S. Environmental Protection Agency, Office of Research and Development, Center for Environmental Research Information, 1987.

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Book chapters on the topic "Dewatering"

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Preene, Martin. "Dewatering." In Selective Neck Dissection for Oral Cancer, 1–8. Cham: Springer International Publishing, 2017. http://dx.doi.org/10.1007/978-3-319-12127-7_89-1.

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Carter, P. "Dewatering." In Drainage Design, 266–81. Boston, MA: Springer US, 1992. http://dx.doi.org/10.1007/978-1-4757-5027-0_11.

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Gill, Charles Burroughs. "Dewatering." In Materials Beneficiation, 105–27. New York, NY: Springer New York, 1991. http://dx.doi.org/10.1007/978-1-4612-3020-5_6.

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Preene, Martin. "Dewatering." In Encyclopedia of Earth Sciences Series, 222–29. Cham: Springer International Publishing, 2018. http://dx.doi.org/10.1007/978-3-319-73568-9_89.

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Kelletat, Dieter, Jiyu Chen, John M. Rybczyk, Shea Penland, Mark A. Kulp, Iver W. Duedall, George A. Maul, et al. "Dewatering." In Encyclopedia of Coastal Science, 387. Dordrecht: Springer Netherlands, 2005. http://dx.doi.org/10.1007/1-4020-3880-1_120.

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Gurjar, Bhola R., and Vinay Kumar Tyagi. "Sludge dewatering." In Sludge Management, 87–109. Leiden, The Netherlands : CRC Press/Balkema, [2017]: CRC Press, 2017. http://dx.doi.org/10.1201/9781315375137-7.

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Wakeman, Richard J. "Dewatering of Filter Cakes: Vacuum and Pressure Dewatering." In Mathematical Models and Design Methods in Solid-Liquid Separation, 286–309. Dordrecht: Springer Netherlands, 1985. http://dx.doi.org/10.1007/978-94-009-5091-7_12.

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Obarska-Pempkowiak, Hanna, Magdalena Gajewska, Ewa Wojciechowska, and Janusz Pempkowiak. "Dewatering of Sewage Sludge Dewatering in Reed Systems." In GeoPlanet: Earth and Planetary Sciences, 157–69. Cham: Springer International Publishing, 2015. http://dx.doi.org/10.1007/978-3-319-13794-0_9.

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Leclerc, D., and S. Rebouillat. "Dewatering by Compression." In Mathematical Models and Design Methods in Solid-Liquid Separation, 356–91. Dordrecht: Springer Netherlands, 1985. http://dx.doi.org/10.1007/978-94-009-5091-7_15.

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Speight, James G. "Dewatering and Desalting." In Dewatering, Desalting, and Distillation in Petroleum Refining, 47–78. Boca Raton: CRC Press, 2022. http://dx.doi.org/10.1201/9781003184959-2.

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Conference papers on the topic "Dewatering"

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Kaswalder, Francesco, Davide Cavalli, Idemilson Fritzke, and Andrea Bassi. "High capacity dewatering plants." In 23rd International Conference on Paste, Thickened and Filtered Tailings. Gecamin Publications, Santiago, 2020. http://dx.doi.org/10.36487/acg_repo/2052_10.

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Akse, James, Richard Wheeler, John Holtsnider, and John Fisher. "Brine Dewatering Using Ultrasonic Nebulization." In 41st International Conference on Environmental Systems. Reston, Virigina: American Institute of Aeronautics and Astronautics, 2011. http://dx.doi.org/10.2514/6.2011-5170.

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Mappus, B. E., and A. G. Torstrick. "Pipeline Hydrotesting, Dewatering, and Commissioning." In Offshore Technology Conference. Offshore Technology Conference, 2007. http://dx.doi.org/10.4043/19062-ms.

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Takasaki, Masaya, Takanori Endo, and Takeshi Mizuno. "Ultrasonic dewatering in minute holes." In 2013 IEEE International Ultrasonics Symposium (IUS). IEEE, 2013. http://dx.doi.org/10.1109/ultsym.2013.0127.

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Rhyner, Frederick C., Jesse Richins, Ahmed Elmekati, and Joseph Sun. "Dewatering at Crane Valley Dam." In GeoCongress 2012. Reston, VA: American Society of Civil Engineers, 2012. http://dx.doi.org/10.1061/9780784412121.343.

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Niederhauser, Mark, and K. Wilson. "Innovative coal refuse dewatering system." In 14th International Seminar on Paste and Thickened Tailings. Australian Centre for Geomechanics, Perth, 2011. http://dx.doi.org/10.36487/acg_rep/1104_04_niederhauser.

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Westra, Remko, Borre Leif Knudsen, Henrik Bjartnes, and Boubker Ibouhouten. "Qualification Of InLine DeWatering Technology." In SPE Offshore Europe Oil and Gas Conference and Exhibition. Society of Petroleum Engineers, 2013. http://dx.doi.org/10.2118/166644-ms.

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Satyamurthy, R., K. Liao, and S. K. Bhatia. "Investigations of Geotextile Tube Dewatering." In Geo-Frontiers Congress 2011. Reston, VA: American Society of Civil Engineers, 2011. http://dx.doi.org/10.1061/41165(397)217.

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Seidle, J. P. "A Numerical Study of Coalbed Dewatering." In SPE Rocky Mountain Regional Meeting. Society of Petroleum Engineers, 1992. http://dx.doi.org/10.2118/24358-ms.

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Beard, R. E., and H. S. Muralidhara. "Mechanistic Considerations of Acoustic Dewatering Techniques." In IEEE 1985 Ultrasonics Symposium. IEEE, 1985. http://dx.doi.org/10.1109/ultsym.1985.198681.

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Reports on the topic "Dewatering"

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R.H. Yoon and G.H. Luttrell. Advanced Dewatering Systems Development. Office of Scientific and Technical Information (OSTI), July 2008. http://dx.doi.org/10.2172/953468.

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Thomson, N. R. Soil vapor extraction with dewatering. Office of Scientific and Technical Information (OSTI), August 1996. http://dx.doi.org/10.2172/447173.

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Parekh, B. K. Dewatering studies of fine clean coal. Office of Scientific and Technical Information (OSTI), January 1991. http://dx.doi.org/10.2172/5987026.

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Parekh, B. K. Dewatering studies of fine clean coal. Office of Scientific and Technical Information (OSTI), January 1991. http://dx.doi.org/10.2172/6013331.

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Kim, B., M. Zelinski, C. Criner, N. Senapati, H. Muralidhara, B. Jirjis, R. Beard, C. Cummings, and S. Chauhan. Electroacoustic dewatering of food and other suspensions. Office of Scientific and Technical Information (OSTI), May 1989. http://dx.doi.org/10.2172/5557923.

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Cyrus K Aidun. ACOUSTIC FORMING FOR ENHANCED DEWATERING AND FORMATION. Office of Scientific and Technical Information (OSTI), November 2007. http://dx.doi.org/10.2172/920309.

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Wu Zhang, David Yang, Amar Amarnath, Iftikhar Huq, Scott O'Brien, and Jim Williams. Development of an Ultra-fine Coal Dewatering Technology and an Integrated Flotation-Dewatering System for Coal Preparation Plants. Office of Scientific and Technical Information (OSTI), December 2006. http://dx.doi.org/10.2172/946468.

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Beck, Dave. Development of A Continuous Process for Displacement Dewatering. Office of Scientific and Technical Information (OSTI), October 2006. http://dx.doi.org/10.2172/895289.

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Parekh, B. K., R. Hogg, and A. Fonseca. Evaluation of hyperbaric filtration for fine coal dewatering. Office of Scientific and Technical Information (OSTI), January 1992. http://dx.doi.org/10.2172/6704445.

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Wilson, J. W., and R. Q. Honaker. Ultrafine coal single stage dewatering and briquetting process. Office of Scientific and Technical Information (OSTI), December 1995. http://dx.doi.org/10.2172/205928.

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