Literatura académica sobre el tema "Saline water conversion"
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Artículos de revistas sobre el tema "Saline water conversion"
Birkett, James. "Kicking off Saline Water Conversion: An Important Early Meeting". IDA Journal of Desalination and Water Reuse 1, n.º 1 (enero de 2009): 26–33. http://dx.doi.org/10.1179/ida.2009.1.1.26.
Texto completoDara, Saad, Arman Bonakdarpour, Meghan Ho, Rubenthran Govindarajan y David P. Wilkinson. "Conversion of saline waste-water and gaseous carbon dioxide to (bi)carbonate salts, hydrochloric acid and desalinated water for on-site industrial utilization". Reaction Chemistry & Engineering 4, n.º 1 (2019): 141–50. http://dx.doi.org/10.1039/c8re00259b.
Texto completoElsayad, OsamaA y Ayman Khater. "Prevalence of unified airway disease in Saline Water Conversion Corporation Society". Pan Arab Journal of Rhinology 11, n.º 2 (2021): 105. http://dx.doi.org/10.4103/pajr.pajr_34_20.
Texto completoYu, Hai Tian, Fu Li Tian, Hong Yu Wang, Ying Hui Hu y Wan Li Sheng. "An Application of Dunaliella Salina Algae: Biodiesel". Advanced Materials Research 953-954 (junio de 2014): 281–83. http://dx.doi.org/10.4028/www.scientific.net/amr.953-954.281.
Texto completoSang, Honghui, Weihua Guo, Yun Gao, Xiyun Jiao y Xiaobao Pan. "Effects of Alternating Fresh and Saline Water Irrigation on Soil Salinity and Chlorophyll Fluorescence of Summer Maize". Water 12, n.º 11 (30 de octubre de 2020): 3054. http://dx.doi.org/10.3390/w12113054.
Texto completoGoyal, Ashish y Pawan Sharma. "A model on the biological treatment of saline wastewater". International Journal of Biomathematics 10, n.º 02 (18 de enero de 2017): 1750021. http://dx.doi.org/10.1142/s1793524517500218.
Texto completoAnuwongpinit, Thanavit, Sakditat Sutthinoon, Pinit Tanachaichoksirikun y Boonchana Purahong. "Development of IoT portable device for saline water monitoring in Bang Kachao Area of Thailand". Journal of Physics: Conference Series 2559, n.º 1 (1 de agosto de 2023): 012005. http://dx.doi.org/10.1088/1742-6596/2559/1/012005.
Texto completoFellows, Christopher M., Ali A. Al Hamzah y Seungwon Ihm. "Pathways to magnesium supplementation of drinking water: An overview of the saline water conversion corporation experience". Chemical Engineering Journal Advances 16 (noviembre de 2023): 100574. http://dx.doi.org/10.1016/j.ceja.2023.100574.
Texto completoPeng, Shuquan, Fan Wang y Ling Fan. "Experimental Study on Influence of Vaporous Water on Salt Expansion of Sulfate Saline Soil". Advances in Civil Engineering 2019 (31 de julio de 2019): 1–9. http://dx.doi.org/10.1155/2019/6819460.
Texto completoHeberle, J. R. y C. F. Edwards. "Coal energy conversion with carbon sequestration via combustion in supercritical saline aquifer water". Energy Procedia 1, n.º 1 (febrero de 2009): 4055–62. http://dx.doi.org/10.1016/j.egypro.2009.02.212.
Texto completoTesis sobre el tema "Saline water conversion"
Mkhize, Mfanafuthi Mthandeni. "Multistage solar still desalination system". Thesis, Cape Peninsula University of Technology, 2018. http://hdl.handle.net/20.500.11838/2848.
Texto completoThe present study was centred on the design of a thermal multistage solar still desalination system. The design is a multistage with new configurations such as direct vapour input into each stage using vapour make-up tubes and the integration of a multistage with a basin type solar still. The incorporation of float a valve in the secondary seawater tank to regulate the seawater in the assembly eliminated the need of pumps to the system. The circulation of seawater between the evaporator and the evacuated tube solar collector (ETC) was through the pressure difference and the flow back was controlled through the incorporation of oneway flow valve. The ETC was used as a heat source to supply the thermal energy into the multistage system. The system had no electrical connections and therefore, no forced circulation as no pumps or any electrical components were used. The system consisted of six stages in total, the evaporator supplied the vapour to five of the six stages of the system. The system was tested on the roof of Mechanical Engineering Department and this location was chosen because of less sun’s intensity obstructions. The system was tested for nine (9) days but the distillate collection was not performed for the whole each day. This was due to the controlled access to the roof and the minor repairs that had to occur before the tests were conducted. The duration on which the tests were conducted varied in each day. The data was supposed to be logged from 08h00 am to 18h00 pm but this was not so due to the controlled access to where the tests were conducted. This data logging period was chosen based on the assumptions that the sun’s intensity would be at maximum within this period. The longest period of test was approximately 7 hours and the system managed to produce about 1500 ml and the maximum temperature for the day was 28oC. The system produced a minimum of 225 ml in the space of 3 hours and the temperature of the day was 26oC. The total amount of distillate produced was about 7600 ml and this amount was produced within the period of 49 hours. The 49 hours is equivalent to two days and 1 hour. It is anticipated that the system would have produced more should there be no repairs involved during the tests. The system produced a maximum of 48 ml at night and a minimum of 8ml in some nights. The night tests were not controlled and monitored due to limited access. It was noticed that the system was empty in each morning of the first few days of the tests. This emptiness contributed to the leakage occurred to the evaporator. The leakage of the evaporator was caused by unmonitored heat supplied by the ETC. The evaporator was constructed using unsuitable material and this was another factor which contributed towards the failure of the evaporator.
Chen, Yuanhong. "Electrohydrodynamic (EHD) desalination of sea water". Thesis, McGill University, 1992. http://digitool.Library.McGill.CA:80/R/?func=dbin-jump-full&object_id=60676.
Texto completoLourens, Christo Le Roux. "Seawater distillation through solar evaporation". Thesis, Cape Peninsula University of Technology, 2007. http://hdl.handle.net/20.500.11838/1272.
Texto completoAn investigation was performed into a new desalination plant operating on the principles of distillation through the utilisation of solar energy only. The need for such a system is due to the high energy requirements of current large scale desalination systems and that, in the future, more and more desalinated water will be required to sustain life in certain areas. A conceptual design of such a plant was completed and it proved its feasibility by providing an in depth explanation of the principles that govern its operation. A computer model, in the form of a MathCAD program, was developed to simulating this process flow. The accuracy of the program was investigated with the help of a pilot plant. It is shown that such a full scale plant would produce, in the region of Saldanha Bay, a town on the Western Coast of South Africa, 5000m3 ofpotable water a day with a solar absorption/evaporation area of 1,87knlrequiring only 1,75kWh per cubic meter of water produced. Its electrical energy requirements can be provided using solar panels allowing the plant to remain independent of external electrical supplies. This electrical energy requirement is less than 33% of the least energy intensive alternative method, reverse osmosis. Since the production rate is dependent on the absorption/evaporation area the plant can be scaled to fit the specific production rate required.
Gude, Veera Gnaneswar. "Desalination using low grade heat sources". access full-text online access from Digital Dissertation Consortium, 2007. http://libweb.cityu.edu.hk/cgi-bin/er/db/ddcdiss.pl?3296129.
Texto completoYüceer, Ahmet. "Pressure drops along the bores of hollow fibre membranes their measurement, prediction and effect on fibre bundle performance /". Connect to e-thesis, 1985. http://theses.gla.ac.uk/976/.
Texto completoBLL : D80152. Ph.D. thesis submitted to the Department of Mechanical Engineering, University of Glasgow, 1985. Includes bibliographical references. Print version also available.
Al, Abdulgader Hasan. "A novel hybrid ion exchange/nanofiltration process for water desalination". Thesis, Swansea University, 2014. http://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.678263.
Texto completoAlwaer, Ayad Almakhzum Mohamed. "A prototype desalination system using solar energy and heat pipe technology". Thesis, Cape Peninsula University of Technology, 2016. http://hdl.handle.net/20.500.11838/2455.
Texto completoThe water desalination process needs large quantities of energy, either directly from fossil fuel or electricity from the national grid. However, these sources of energy significantly contribute to problems such as global warming in addition to creating a drain on the economy, due to their high cost. This dissertation is a description of the research undertaken with the aim of producing a water desalination prototype; a novel approach that was designed using state-of-the-art solar water heating equipment, incorporating the technologies of evacuated tubes and heat pipes. During the execution of the project, various modifications to the original commercially-available solar water heating system were attempted, each aimed at increasing the production of pure water. Finally, the system proved capable of producing a reasonable amount of pure water after twelve lengthy indoor experiments conducted in a laboratory in the department of Mechanical Engineering at the Cape Peninsula University of Technology, Bellville Campus, Cape Town, South Africa. Each experiment lasted five days on the basis of seven hours of exposure to an average amount of simulated solar radiation, followed by seventeen hours daily of inactivity and partial cooling down of the system.
Nyamhingura, Amon. "Characterization and chemical speciation modelling of saline effluents at Sasol Synthetic Fuels Complex-Secunda and Tukuta power station". Thesis, University of the Western Cape, 2009. http://etd.uwc.ac.za/index.php?module=etd&action=viewtitle&id=gen8Srv25Nme4_7974_1297940655.
Texto completoThe study shows conclusively that brine composition and concentration is highly variable at these South African power utilities and processes such as RO, contact with ash and CO2 ingress can have an impact upon the overall brine quality. Aq.QA was found to be a more accurate tool for classifying waters according to dominant ions than Stiff diagrams but Stiff diagrams still have the superior advantage of being a mapping tool to easily identify samples of similar composition as well as quickly identify what has been added or what has been removed from a water stream. Chemical speciation could identify effluent streams where CO2 dissolution had taken place.
Lambrechts, Rhynhardt. "A performance and energy evaluation of a fertiliser-drawn forward osmosis (FDFO) system". Thesis, Cape Peninsula University of Technology, 2018. http://hdl.handle.net/20.500.11838/2747.
Texto completoGlobally, water is considered an essential resource as it sustains human, animal and plant life. Water is not only essential for all forms of life but imperative for economic growth. The world’s population is increasing at a disquieting rate, which will result in an increased demand for fresh water and food security. The agricultural industry is the main consumer of global freshwater and utilises fertilisers in order to meet food demands. The demand for water in South Africa (SA) has increased considerably due to the rapid expansion of the agricultural industry, and of the municipal and industrial sectors. Agricultural developments in SA are affected greatly as the country is facing a current drought crisis as a result of low rainfall and large water demands. With an abundance of saline water globally, desalinisation will be a major contributor to solving the global freshwater crisis. With limited fresh water resources accompanied by the agricultural industry as a major consumer, alternative measures are required to desalinate water specifically for agricultural use. Forward osmosis (FO) is a membrane technology that gained interest over the past decade because it has several advantages over pressure-driven membrane processes such as reverse osmosis (RO). FO technology is based on the natural osmotic process which is driven by a concentration gradient between two solutions separated by a semi-permeable membrane. Naturally, water will permeate through the membrane from a solution of low solute concentration or low osmotic pressure (OP) known as a feed solution (FS) to a solution of a higher concentration or higher OP also known as a draw solution (DS). Whilst various research studies have contributed to several advances in FO, several process limitations such as reverse solute flux (RSF), concentration polarisation (CP) and membrane fouling remain problematic, hindering FO for large-scale applications. Further investigation is therefore warranted and crucial in order to understand how to mitigate these limitations to develop/improve future processes. The aim of this study was to evaluate a fertiliser-drawn forward osmosis (FDFO) system by investigating the effects of membrane orientation, system flow rate, DS concentration, and membrane fouling on an FDFO systems performance and energy consumption. The FS used was synthetic brackish water with a sodium chloride (NaCl) content of 5 g/L whereas a potassium chloride (KCl) synthetic fertiliser was used as a DS. The membrane utilised was a cellulose triacetate (CTA) membrane and was tested in forward osmosis mode (FO mode) and pressure retarded osmosis mode (PRO mode) whilst the system flow rate was adjusted between 100, 200 and 400 mL/min. Additionally, the DS concentration was altered from 0.5, 1 and 2 M KCl, respectively. Experiments were performed using a bench scale FO setup which comprised of an i) FO membrane cell, ii) a double head variable peristaltic pump for transporting FS and DS’s respectively, iii) a digital scale to measure the mass of the DS, iv) a magnetic stirrer to agitate the FS, v) two reservoirs for the FS and DS, respectively, vi) a digital multiparameter meter to determine FS electrical conductivity (EC) and vii) a digital electrical multimeter to measure system energy consumption. Each experiment comprised of seven steps i) pre-FDFO membrane control, ii) membrane cleaning, iii) FDFO experiment, iv) post-FDFO membrane control, v) membrane cleaning, vi) membrane damage dye identification and vii) membrane cleaning. Pre- and post-FDFO membrane control experiments operated for 5 h whilst each membrane cleaning procedure operated for 30 min. The FDFO experiment operated for 24 h whilst the membrane damage dye identification operated until a minimum of 10 mL water was recovered. The process parameter which largely contributed to a beneficial system performance and specific energy consumption (SEC) was the increase in DS concentration. Water fluxes increased approximately threefold from a DS concentration increase from 0.5 to 1 M, followed by an additional 30 to 50 % rise in water flux at a DS concentration increase 1 to 2 M. SEC decreased by 58 and 53 % for FO and PRO modes, respectively, with a DS concentration increase from 0.5 to 1 M. An additional 35 and 37 % SEC reduction for FO and PRO modes was obtained for a DS concentration increase from 1 to 2 M. Altering the membrane from FO to PRO did not contribute to a beneficial system performance nor did it improve SEC. However, at a DS concentration of 0,5 M, the PRO mode obtained a 5.3 % greater water recovery compared to the FO mode. Conversely, at a DS concentration of 1 and 2 M, the FO mode achieved 5.4 and 7.0 % greater water recoveries compared to the PRO mode. The increase in flow rate also did not increase system performance significantly, however, a fluctuation in system SEC was observed. Throughout the study, no membrane fouling was observed, however, possible minute traces of membrane fouling could be observed from the membrane surface electron microscope (SEM) images. Additionally, minor changes in post- FDFO membrane control water recovery results were noticed which support the possible occurrence of membrane fouling during the FDFO experiment.
Delgado, Guillermo Guadalupe. "Treatment of RO concentrate using VSEP technology". To access this resource online via ProQuest Dissertations and Theses @ UTEP, 2009. http://0-proquest.umi.com.lib.utep.edu/login?COPT=REJTPTU0YmImSU5UPTAmVkVSPTI=&clientId=2515.
Texto completoLibros sobre el tema "Saline water conversion"
Noam, Lior, ed. Measurements and control in water desalination. Amsterdam: Elsevier, 1986.
Buscar texto completoAmerican Water Works Association. Water Desalting Committee, ed. Water desalting planning guide for water utilities. Hoboken, N.J: J. Wiley & Sons, 2004.
Buscar texto completoEisenhauer, Roy J. Laverkin Springs, Utah on-site pretreatment and desalting processes evaluations. Denver, Colo: Applied Sciences Branch, Division of Research and Laboratory Services, Engineering and Research Center, 1985.
Buscar texto completoRaucher, Robert S. Guidelines for implementing seawater and brackish water desalination facilities. Denver, CO: Water Research Foundation, 2010.
Buscar texto completoGallucci, M. Massa. Studio tecnico-informativo sugli impianti di dissalazione anche alimentati solarmente. Roma: Comitato nazionale per la ricerca e per lo sviluppo dell'energia nucleare e delle energie alternative, 1987.
Buscar texto completoHans-Günter, Heitmann, ed. Saline water processing: Desalination and treatment of seawater, brackish water, and industrial waste water. Weinheim, Federal Republic of Germany: VCH, 1990.
Buscar texto completoUnited States. Congress. House. Committee on Agriculture. Authorizing the construction by the Secretary of Agriculture of a salinity laboratory at Riverside, CA: Report (to accompany H.R. 5215) (including the Congressional Budget Office cost estimate). [Washington, D.C.?: U.S. G.P.O., 1986], 1986.
Buscar texto completoYonan, Dina. The environmental impact of Carlsbad seawater desalination plant San Diego. [San Diego, California]: National University, 2013.
Buscar texto completoMiriam, Balaban y International Desalination Association, eds. Desalination and water reuse: 1994 desalination directory. 6a ed. [Chieta] Italy: Balaban Desalination Publishers, 1994.
Buscar texto completoWoto, Teedzani. The experience with small-scale desalinators for remote area dwellers of the Kalahari Botswana. Kanye, Botswana: Rural Industries Promotions, 1987.
Buscar texto completoCapítulos de libros sobre el tema "Saline water conversion"
Almutairi, Raid, Zaid Albeladi y Ali Elrashidi. "Assessment of Health and Safety Hazards Affecting Workers at Saline Water Conversion Corporation Lathe Workshop". En Digitalisation: Opportunities and Challenges for Business, 824–37. Cham: Springer International Publishing, 2023. http://dx.doi.org/10.1007/978-3-031-26956-1_77.
Texto completoYudelman, M. "Water and Food in Developing Countries in the Next Century". En Feeding a World Population of More Than Eight Billion People. Oxford University Press, 1998. http://dx.doi.org/10.1093/oso/9780195113129.003.0010.
Texto completoBunker, Bruce C. y William H. Casey. "Oxide Films in Metal Corrosion: Oxide Defect Chemistry". En The Aqueous Chemistry of Oxides. Oxford University Press, 2016. http://dx.doi.org/10.1093/oso/9780199384259.003.0019.
Texto completoActas de conferencias sobre el tema "Saline water conversion"
Mobley, Paul D., Rebecca Z. Pass y Chris F. Edwards. "Exergy Analysis of Coal Energy Conversion With Carbon Sequestration Via Combustion in Supercritical Saline Aquifer Water". En ASME 2011 5th International Conference on Energy Sustainability. ASMEDC, 2011. http://dx.doi.org/10.1115/es2011-54458.
Texto completoEmdadi, Arash, Yunus Emami, Mansour Zenouzi, Amir Lak, Behzad Panahirad, Aydin Lotfi, Farshad Lak y Gregory J. Kowalski. "Potential of Electricity Generation by the Salinity Gradient Energy Conversion Technologies in the System of Urmia Lake-Gadar Chay River". En ASME 2014 8th International Conference on Energy Sustainability collocated with the ASME 2014 12th International Conference on Fuel Cell Science, Engineering and Technology. American Society of Mechanical Engineers, 2014. http://dx.doi.org/10.1115/es2014-6310.
Texto completoEmdadi, Arash, Mansour Zenouzi y Gregory J. Kowalski. "Determining the Potential of Salinity Gradient Energy Source Using an Exergy Analysis". En ASME 2016 10th International Conference on Energy Sustainability collocated with the ASME 2016 Power Conference and the ASME 2016 14th International Conference on Fuel Cell Science, Engineering and Technology. American Society of Mechanical Engineers, 2016. http://dx.doi.org/10.1115/es2016-59532.
Texto completoThyagarajan, Ashok, Vijay Dhir y Debjyoti Banerjee. "Experimental Investigation of Solar-Thermal Desalination Platform Leveraging Dynamic Flash Evaporation and Swirl Flow Separator". En ASME 2022 International Mechanical Engineering Congress and Exposition. American Society of Mechanical Engineers, 2022. http://dx.doi.org/10.1115/imece2022-96099.
Texto completoWalles, Wilhelm y Luis Mulford. "Solar energy via salino voltaics from brine and water regenerated via solar stills". En Intersociety Energy Conversion Engineering Conference. Reston, Virigina: American Institute of Aeronautics and Astronautics, 1994. http://dx.doi.org/10.2514/6.1994-4026.
Texto completoAjeesh, M. V., R. Panneer Selvam, R. Sundarvadivelu, G. Dhinesh, R. Saravanan, S. V. S. Phani Kumar y M. V. Ramana Murthy. "Hydrodynamic Analysis of an Inverted Catenary Coldwater Pipeline of a LTTD Plant". En ASME 2015 34th International Conference on Ocean, Offshore and Arctic Engineering. American Society of Mechanical Engineers, 2015. http://dx.doi.org/10.1115/omae2015-41521.
Texto completoSeevam, Patricia, Julia Race, Martin Downie, Julian Barnett y Russell Cooper. "Capturing Carbon Dioxide: The Feasibility of Re-Using Existing Pipeline Infrastructure to Transport Anthropogenic CO2". En 2010 8th International Pipeline Conference. ASMEDC, 2010. http://dx.doi.org/10.1115/ipc2010-31564.
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