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Journal articles on the topic 'Clarification of water'

Author: Grafiati

Published: 4 June 2021

Last updated: 6 February 2022

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1

Liew, A. G., M. J. M. M. Noor, S. A. Muyibi, A. M. S. Fugara, T. A. Muhammed, and S. E. Iyuke. "Surface water clarification usingM. oleiferaseeds." International Journal of Environmental Studies 63, no. 2 (2006): 211–19. http://dx.doi.org/10.1080/00207230500117670.

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2

Ta, C. T., and C. A. Woodward. "A treatability index for reservoir water." Water Science and Technology 37, no. 2 (1998): 27–33. http://dx.doi.org/10.2166/wst.1998.0096.

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A Treatability Index is developed to allow comparison of different reservoir waters according to their effects on a water treatments works. For the water treatment works which employs rapid gravity filters, the index is the product of the algal concentration, the clarification coefficients of algae and the filtration rate. The index is applied to reservoir waters within Thames Water area. Algae observed in reservoirs are grouped according to their shapes. Among these groups, twenty frequently observed species were selected and their clarification coefficients were measured. The treatability in

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3

Sweeney, Bernard W. "The Clarification of the Clean Water Act." Sustainability: The Journal of Record 7, no. 5 (2014): 231–33. http://dx.doi.org/10.1089/sus.2014.9770.

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4

Tengrang, Ugsornphak, and Sininart Chongkhong. "Optimizing Clarification of Pineapple Peel." Advanced Materials Research 941-944 (June 2014): 1060–64. http://dx.doi.org/10.4028/www.scientific.net/amr.941-944.1060.

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Alpha-amylase is a potentially useful enzyme for the pretreatment and pre-hydrolysis (clarification) of pineapple peel. The clarified products contain sufficient glucose content for ethanol fermentation. The influences of quantity of the peel to water (10-16 %w: weight of peel to weight of water), alpha-amylase amount (100-240 U/g: U of amylase to g of peel), pH value (5.5-7.0), temperature (70-100oC) and time (60-240 min) were investigated by RSM (Response surface methodology). To obtain 31.8 g/L of the highest glucose concentration, the clarification is to be performed by 16 %w peel to water

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5

Gao, Bo, Qi Yan Feng, and Xiang Dong Li. "Clarification of High-Salinity Mine Water with Plants." Advanced Materials Research 610-613 (December 2012): 1398–401. http://dx.doi.org/10.4028/www.scientific.net/amr.610-613.1398.

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High-salinity mine water has been often treating with electrodialysis, multi-effect. But there are still some problems. So we study high-salinity mine water treatment for 24 days with different plants and salinity. The sample was selected from Zhang Xiao Lou coal in Xuzhou. The resultes show that: Cress is able to adapt the water with high salinity and absorb the contamination. When the dosage of NaCl is 1 g/L and 2 g/L, TDS removal efficiency can reach 69.36% and 56.47%. With the increase of NaCl from 0 to 1 g/L, the treatment capacity of the plant increased gradually, and the treatment capac

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6

Jahn, Samia AI Azharia. "Drinking water from Chinese rivers: challenges of clarification." Journal of Water Supply: Research and Technology-Aqua 50, no. 1 (2001): 15–27. http://dx.doi.org/10.2166/aqua.2001.0002.

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7

Радовенчик, Вячеслав Михайлович, Софія Володимирівна Глиняна, Ярослав Вячеславович Радовенчик, and Надія Василівна Калініченко. "Aluminium coagulants efficiency evaluation for natural water clarification." Eastern-European Journal of Enterprise Technologies 2, no. 10(68) (2014): 17. http://dx.doi.org/10.15587/1729-4061.2014.23355.

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8

Wiley, Patrick E., and Jonathan D. Trent. "Clarification of algae-laden water using electrochemical processes." Water Supply 16, no. 2 (2015): 314–23. http://dx.doi.org/10.2166/ws.2015.140.

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Algae contamination of surface water and drinking water supplies is a significant problem particularly in rural areas. A decentralized inexpensive technology that would effectively remove algae from water would be beneficial. Electrocoagulation (EC) combined with electroflotation (EF) as a single process (ECF) is a promising algae harvesting technique with no moving parts that may be powered using a modest array of photovoltaic panels if a low power system can be developed. Here, an ECF system was constructed to study the energy required to remove algae from a simulated drinking water supply.

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9

White, Richard, Beverley Swales, and Martyn Butcher. "Clarification about use of water in burns treatment." Nursing Standard 27, no. 10 (2012): 33. http://dx.doi.org/10.7748/ns.27.10.33.s50.

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10

Booker, N. A., D. Keir, A. J. Priestley, C. B. Ritchie, D. L. Sudarmana, and M. A. Woods. "Sewage Clarification with Magnetite Particles." Water Science and Technology 23, no. 7-9 (1991): 1703–12. http://dx.doi.org/10.2166/wst.1991.0625.

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A new approach to sewage treatment which involves rapid clarification of raw sewage with fine magnetite particles is described. The process, which is essentially a greatly accelerated chemical coagulation, provides a quick separation of the sewage into two liquid streams, one clarified, the other highly concentrated. Development of the process up to and including operation of a fully continuous pilot is outlined and potential advantages and disadvantages identified.

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11

Tan, Yu Fei, Zhi Gao Li, and Li Bai. "Design and Simulations of Water Purification Heating System in Cold Rural Areas." Applied Mechanics and Materials 764-765 (May 2015): 1204–8. http://dx.doi.org/10.4028/www.scientific.net/amm.764-765.1204.

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Biological treatment process of water purification often cannot be completed under low temperature in northern rural areas. On the basis of determining the thermal characteristics of clarification pool and biofilter pool of the purification systematically, we designed and proposed a purification heating system in which solar collector and straw boiler run in parallel, and further built the mathematical model of purification. We simulated heating effect on clarification pool and biofilter pool when heating pipes were placed in different locations by using Fluent. It indicated that, the heating

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12

Ramey, Dotti F., Junko Munakata-Marr, and Tzahi Y. Cath. "Tailored water treatment using enhanced primary clarification for nutrient recovery and production of water for turfgrass irrigation." Environmental Science: Water Research & Technology 3, no. 4 (2017): 671–85. http://dx.doi.org/10.1039/c7ew00019g.

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Enhanced primary clarification coupled with hypoaerobic biological treatment can produce fertigation water having targeted nitrogen and phosphorus concentrations without substantial changes to biological treatment and without increasing energy requirements.

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13

Isaxodjayev, Xayrulla, Nizonjon Usmonov, Yusufbek Abdullabekov, and Zoxid Xasanov. "Experimental electro coagulation unit for pretreament of mains water for dteam generation at thermal power plants." E3S Web of Conferences 216 (2020): 01126. http://dx.doi.org/10.1051/e3sconf/202021601126.

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The article covers the state of pre-chemical treatment of natural water at Tashtpp with the use of aluminum sulphate and the creation of an experimental unit for producing coagulant, aluminum sulphate, as well as a block diagram of the proposed electrocoagulation unit for pre-treatment and clarification of water. An electrocoagulation technology for pre-treatment and clarification of water for Tashtpp steam boilers has been developed.

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14

Shamyan, Varuzhan Levon. "Technological and Constructive Proposals on Sand Trap and Removal from Industrial and Domestic Waste Water." Advanced Materials Research 1020 (October 2014): 626–30. http://dx.doi.org/10.4028/www.scientific.net/amr.1020.626.

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Abstract: The studies on operating effectiveness of sand traps in partially acting facilities of the Yerevan Aeration Plant have shown that along the satisfactory clarification of silts (sand) of mineral origin at the facility bed materials of organic origin are also trapped causing sand traps failure their main function which is clearly separation of the two types of waste waters. In addition serious problems and difficulties arise also in the sand removal. Therefore, in this paper it is suggested both technological ( grounded reduction of the number of sand traps and including in the mechani

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15

Yakovlіev, V. S., and B. A. Voinarovskyi. "THE EFFICIENCY WATER CLARIFICATION IN MODELS OF VERTICAL TANK." ACADEMIC JOURNAL Series: Industrial Machine Building, Civil Engineering 1, no. 48 (2017): 244–50. http://dx.doi.org/10.26906/znp.2017.48.807.

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The purpose of this article is to analyze theoretical and experimental data on the structures and analyze the performance of type clarifier, as well as to highlight the shortcomings of the proposed designs. It was found that for the experiments it is necessary to create a physical model of the vertical sediment tank in the laboratory using the following factors: material costs, technological parameters, design parameters. The purpose of this article is to show the effect of the velocity of upward flow of water inside the vertical settler on the efficiency of its lighting on the physical model

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16

CHANG, S. Y., R. T. TOLEDO, and H. S. LILLARD. "Clarification and Decontamination of Poultry Chiller Water for Recycling." Poultry Science 68, no. 8 (1989): 1100–1108. http://dx.doi.org/10.3382/ps.0681100.

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17

Folkard, Sutherland, and Jahn. "Water clarification with natural coagulants and dissolved air flotation." Waterlines 5, no. 2 (1986): 23–26. http://dx.doi.org/10.3362/0262-8104.1986.044.

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18

Heath, Gregory, John Carr, Walter Bailey, Salil Kharkar, Kenneth Watson, and Michael Demko. "Preliminary Design of the DC Water Enhanced Clarification Facility." Proceedings of the Water Environment Federation 2013, no. 18 (2013): 605–20. http://dx.doi.org/10.2175/193864713813668349.

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19

Dushkin, S. S., and O. P. Galkina. "More Effective Clarification of Circulating Water at Coke Plants." Coke and Chemistry 62, no. 10 (2019): 474–80. http://dx.doi.org/10.3103/s1068364x19100041.

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20

Martono, Y., F. E. R. Pranawati, C. A. Riyanto, and J. Muninggar. "Clarification and encapsulation of Stevia rebaudiana Bertoni water extract." Journal of Physics: Conference Series 1307 (August 2019): 012016. http://dx.doi.org/10.1088/1742-6596/1307/1/012016.

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21

Wittmann, Erich, Annie Tazi-Pain, Thierry Chanussot, et al. "Clarification of a highly turbid karstic water by microfiltration." Desalination 145, no. 1-3 (2002): 309–13. http://dx.doi.org/10.1016/s0011-9164(02)00428-9.

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22

Arora, Harish, James R. DeWolfe, Ramon G. Lee, and Thomas P. Grubb. "Evaluation of dissolved air flotation process for water clarification and sludge thickening." Water Science and Technology 31, no. 3-4 (1995): 137–47. http://dx.doi.org/10.2166/wst.1995.0524.

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Dissolved air flotation was evaluated using pilot and bench tests for water clarification and sludge thickening. A DAF pilot study was conducted on one water source with low turbidity, high color, high organic content and algal blooms. For this water, coagulation with alum, cationic polymer and pH around 6.1 resulted in removal of turbidity, color and algae. THMFP and TOC were removed by approximately 25 and 50 percent, respectively. A river water source was used in another pilot study to identify limits on source water turbidity for the DAF process. Tests conducted with induced high turbidity

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23

Edzwald, James K., and Michael B. Kelley. "Control of Cryptosporidium: from reservoirs to clarifiers to filters." Water Science and Technology 37, no. 2 (1998): 1–8. http://dx.doi.org/10.2166/wst.1998.0089.

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Control of Cryptosporidium in potable waters requires an integrated multiple barrier approach of source water protection of water supply reservoirs and treatment technology through clarification, filtration, and disinfection. Pristine lakes and protected reservoirs have far lower concentrations of oocysts (mean values less than 10 oocysts/100 L) than unprotected supplies. Coagulation is critical to the effective control of Cryptosporidium by clarification and filtration. Coagulation conditions that produce filtered waters of low turbidities, particle counts, and effectively remove natural orga

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24

Tong, Zhen Gong. "Analyzing the Implement of Whirling Clarification Technique in Wastewater Treatment." Advanced Materials Research 113-116 (June 2010): 871–76. http://dx.doi.org/10.4028/www.scientific.net/amr.113-116.871.

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The Micro-Whirling Coagulation process whose core is the Micro-whirling reactor is the key to the Whirling Clarification technique. The Micro-whirling reactor and its working mechanism which is whirling-coagulation and contact-flocculation are illustrated in this paper. Also it tells us the application on clarification tank in one wastewater reuse plant of BAOSTEEL. After being alteration to the standard clarification tank which is put the Micro-whirling reactor into the first and second flocculation area and put the inclined pipes into the sedimentation area, the treatment scale of the whirli

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25

Inha, Laura M., Tapio S. Katko, and Riikka P. Rajala. "Improved Water Services Cooperation through Clarification of Rules and Roles." Water 11, no. 10 (2019): 2172. http://dx.doi.org/10.3390/w11102172.

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Water services face global challenges, many of which are institutional by nature. While technical solutions may suit several situations, institutional frameworks are likely to vary more. On the basis of constructive research approach and new institutional economics we analyze and illustrate water services and the roles of various water sector actors in Finnish water utility setting using the “soccer analogy” by the Nobel Laureate D.C. North: Institutions are the “formal and informal rules of the game” while organizations are the “players”. Additionally, we assess the Finnish water governance s

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26

Wood, Jim, Samir Dhanvantari, Mingdi Yang, et al. "Feasibility of Stormwater Treatment by Conventional and Lamellar Settling With and Without Polymeric Flocculant Addition." Water Quality Research Journal 39, no. 4 (2004): 406–16. http://dx.doi.org/10.2166/wqrj.2004.052.

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Abstract Stormwater treatment by lamellar and conventional clarification, with and without flocculant addition, was investigated in Toronto, Ontario, using a pilot-scale rectangular clarifier vessel with removable lamellar plates. During the 2001 to 2003 field seasons, 76 stormwater runoff events were characterized with respect to flow and quality, and further investigated for stormwater treatment. Most stormwater constituent concentrations at this site exceeded those for the U.S. NURP median urban site. A cationic polymeric flocculant dosed at 4 mg/L, with lamellar clarification, provided the

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27

Lysov, V. A., and D. A. Butko. "Integrated use of sludge treatment and disposal facilities." Вестник гражданских инженеров 17, no. 1 (2020): 156–61. http://dx.doi.org/10.23968/1999-5571-2020-17-1-156-161.

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The paper discusses a method of dehydration and disposal of sludge from water treatment plants using sludge collectors. It is shown that sludge collectors not only receive and process sludge, but can also be used as preliminary settlers for clarification of muddy waters and accumulating (spare) capacity in the water treatment chain of industrial enterprises.

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28

Lazarevic, Vesna, Ivan Krstic, Ljiljana Takic, Miodrag Lazic, and Vlada Veljkovic. "Clarification and filtration of the floculated partuicles suspension from a chemical treatment of waste oil-in-water emulsions from a non-ferrous metalworking plant." Chemical Industry 65, no. 1 (2011): 53–60. http://dx.doi.org/10.2298/hemind100801054l.

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The effects of the coagulation/floculation conditions on clarification and filtration of the floculated particle suspension obtained by the chemical treatment of the waste oil-in-water emulsion (OWE) from a non-ferrous metalworking plant were studied. The treatment involved the addition of aluminum(III) sulfate and lime to the OWE. The main goal was to define the optimum conditions for clarification and filtration of the floculated particle suspension. The factors involved were amounts lime (i.e. pH) and filter aid added the OWE on clarification and filtration rates. At pH>10, the clarifica

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29

Braghetta, A., M. Price, C. Hentz, E. Stevenson, and C. Kolkhorst. "Impact of pretreatment on UF operation and removal of dissolved organics." Water Supply 1, no. 5-6 (2001): 331–39. http://dx.doi.org/10.2166/ws.2001.0130.

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Pilot testing of low-pressure membrane filtration (microfiltration and ultrafiltration) was performed on surface waters at two different pilot locations: the Alameda County Water District (ACWD) in Fremont, CA and the Medina River outside San Antonio, TX. Clarification pretreatment and adsorption pretreatment were evaluated at each site for impacts on operational membrane performance and on removal of dissolved organic compounds including total organic carbon (TOC), UV254, color and precursors to disinfection by-products. At the ACWD test site, studies were also conducted with spiking of taste

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30

Plyatsuk, L. D., I. O. Roy, Y. Y. Chernysh, I. S. Kozii, L. L. Hurets, and A. A. Musabekov. "Clarification of the Recent Scientific Approaches in Magnetic Water Treatment." Journal of Engineering Sciences 6, no. 1 (2019): f12—f18. http://dx.doi.org/10.21272/jes.2019.6(1).f3.

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31

Darracq, Guillaume, Jeannette Chokki, Alexis Ragot, Xavier Bigarnet, Jean Baron, and Michel Joyeux. "Clarification: Impact on Ultrafiltration Membrane Fouling in Drinking Water Treatment." Journal - American Water Works Association 107, no. 12 (2015): E712—E721. http://dx.doi.org/10.5942/jawwa.2015.107.0166.

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32

Morita, Alice K. M., and Marco A. P. Reali. "Fiber filter built with polypropylene fibers applied to water clarification." Water Supply 19, no. 4 (2018): 1036–43. http://dx.doi.org/10.2166/ws.2018.150.

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Abstract Flexible fiber filters are recently developed modular filtration units which have been applied to wastewater and water treatments, satisfactorily removing solids even when operated at high application rates. In this paper, polypropylene fibers, in lieu of the commonly used polyamide fibers, were tested for constructing filtration modules containing parallel fibers. The studied fibers were analyzed by means of scanning electronic microscopy and through solubility assays in hydrochloric acid and sodium hydroxide, aiming to evaluate the risks of using them as filtering media. Three polyp

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33

DEGUCHI, Yoshihiro, Kenta TAMURA, Ryota MURANAKA, et al. "B121 Clarification of Sodium-Water Chemical Reaction Using Laser Diagnostics." Proceedings of the National Symposium on Power and Energy Systems 2014.19 (2014): 45–48. http://dx.doi.org/10.1299/jsmepes.2014.19.45.

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34

Kukobat, Radovan, Ljiljana Vukic, Dijana Drljaca, and Sasa Papuga. "Water temperature and flocculant concentration influence on the surface water clarification with process modeling." Zastita materijala 55, no. 3 (2014): 304–12. http://dx.doi.org/10.5937/zasmat1403304k.

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35

KAI, Hotaka, Yasuhiro ISHIBASHI, Hisatoshi SHIMASE, Shinichi KAMOHARA, and Takehiro TAKEMASA. "Life Cycle Evaluation of Clarification System for Circulation Cooling Water by Electrolyzed Effective Water." Journal of Life Cycle Assessment, Japan 4, no. 3 (2008): 244–52. http://dx.doi.org/10.3370/lca.4.244.

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36

Hartwig, P. "Combined wastewater feed directly into final clarification – advantage for receiving rivers." Water Science and Technology 66, no. 8 (2012): 1621–26. http://dx.doi.org/10.2166/wst.2012.236.

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With a view to a reduction of the discharge from combined water outflow, the increase of the influent to a wastewater treatment plant can be an efficient solution, for cases in which the discharge concentration of the wastewater treatment plant would not deteriorate significantly as a result. Through bypassing the aeration with combined water and a direct feed of the combined water into the final clarification (Mina-Process) the specific sludge volume loading, which is significant to the efficiency of the final clarification, will not be raised. But the adsorption capability of the aerated slu

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37

Buelvas-Caro, Saúl David, Yelitza del Rosario Aguas-Mendoza, and Rafael Enrique Olivero-Verbel. "Clarification of superficial waters of the magdalena river using seeds of Tamarindus indica as bio-coagulants." Respuestas 25, no. 2 (2020): 170–76. http://dx.doi.org/10.22463/0122820x.2960.

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Biocoagulants have emerged as an environmentally friendly and efficient alternative to surface water clarification, allowing the use of agro-industrial waste as a bioavailable source for the treatment of high turbidity water. The objective of this research was to compare the efficiency in the surface water coagulation process of the Magdalena river using aluminum sulfate and tamarind seeds (Tamarindus indica) dissolved in aqueous solution and saline solution. The clarification process was carried out by testing jar, for this was performed an extraction of the hot and cold tamarind coagulant wh

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38

Bennoit, H., A. Peter-Fröhlich, V. Schmidt, and C. Schuster. "BIOLOGICAL TREATMENT OF MUNICIPAL WASTEWATER IN BERLIN, USING A 10 m DEEP BASIN AND FLOTATION FOR SECONDARY CLARIFICATION." Water Science and Technology 30, no. 4 (1994): 81–88. http://dx.doi.org/10.2166/wst.1994.0163.

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For municipal treaunent of wastewater, the space-saving 10 m deep basins biological treaunent is an interesting alternative to conventional activated sludge basins of shallow construction. Results of pilot tests in the Berlin-Ruhleben wastewater clarification plant have shown that the biological P-elimination, nitrification and denitrification processes can be implemented as in shallow basins. However, the activated sludge did not settle satisfactorily. So flotation was implemented in the process for secondary clarification and in the meantime has shown to be a big advantage. In a year-long te

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39

Sun, Nan, Shui Li Yu, Li Xin Ma, Xiao Bei Xu, and Xue Song Yi. "Design and Research on New Efficient Clarification Tank Treating Raw Water of Low-Temperature and High-Color." Advanced Materials Research 183-185 (January 2011): 999–1003. http://dx.doi.org/10.4028/www.scientific.net/amr.183-185.999.

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Based on advantages of plated sedimentation tank, mechanical stirring clarification tank, Densadge, design new efficient clarification tank treating raw water of low-temperature and high-color. Its functions of mixture, flocculation, precipitation and sludge concentration are gather in integral whole. This paper introduces mainly the tank structures, characteristics of technology, design principle, application parameters and operating conditions treating raw water of low-temperature and high-color, laboratory researches show that the tank possess the following characteristics: small occupation

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40

KANEKO, Susumu. "Future of domestic waste water treatment and small-type combined disposal clarification tanks. Spread of small-type combined disposal clarification tanks and future disposal clarification tank administration." Journal of Environmental Conservation Engineering 17, no. 5 (1988): 297–301. http://dx.doi.org/10.5956/jriet.17.297.

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41

Haarhoff, Johannes, and Lucas R. J. van Vuuren. "Design parameters for dissolved air flotation in South Africa." Water Science and Technology 31, no. 3-4 (1995): 203–12. http://dx.doi.org/10.2166/wst.1995.0530.

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Dissolved air flotation has been used in South Africa for more than 25 years in the field of water and waste-water treatment, with practically all the development and verification done locally. This substantial body of knowledge and experience was recently condensed into a document titled A South African Design Guide for Dissolved Air Flotation. A general literature survey was combined with a detailed survey of 26 dissolved air flotation plants operating in Southern Africa, to arrive at suggested design parameters. Two broad categories of applications were covered in the guidelines - those of

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42

Bozkaya-Schrotter, B., C. Daines, A. S. Lescourret, A. Bignon, P. Breant, and J. C. Schrotter. "Treatment of trace organics in membrane concentrates I: pesticide elimination." Water Supply 8, no. 2 (2008): 223–30. http://dx.doi.org/10.2166/ws.2008.056.

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The objective of this study was to eliminate organic micropollutants in the membrane system concentrates, which is produced by drinking water production plants, in order to protect existing water resources. This work is divided into two parts, pesticide elimination (I) and natural organic matter removal (II) in membrane system concentrates. Seven commonly detected pesticides in French surface waters, i.e. atrazine, sulcotrione, bentazone, isoproturon, diuron, glyphosate and acetochlore, were selected as the model micropollutants. Removal/degradation of these pesticides was studied by testing c

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43

Jokela, P., and J. Immonen. "Dissolved air flotation clarification of activated sludge and wastewaters from chemical industry." Water Science and Technology 47, no. 1 (2003): 205–10. http://dx.doi.org/10.2166/wst.2003.0055.

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Wastewaters from separate chemical factories are treated together in an extended aeration activated sludge plant. The factories produce chemicals for paper industry (e.g. starch), latexes and animal feed. The components of the wastewaters include styrene, tertiary butanol and vinyl acetate. Activated sludge is clarified by sedimentation. During winter time, when the water temperature was 3-12°C, the clarification deteriorated causing carry over of suspended solids containing COD. Enhancement of suspended solids and COD removals was studied in a dissolved air flotation jar test unit. Flotation

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44

Edzwald, J. K., and J. E. Tobiason. "Fate and removal of Cryptosporidium in a dissolved air flotation water plant with and without recycle of waste filter backwash water." Water Supply 2, no. 2 (2002): 85–90. http://dx.doi.org/10.2166/ws.2002.0049.

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Pilot plant research focused on the removal of Cryptosporidium oocysts by dissolved air flotation (DAF) clarification and by dual media filtration and on the impacts of the recycle of waste filter backwash water containing oocysts. No impacts from recycle of filter backwash (10% rate) were found for turbidity, particle counts (2-15 μm), and UV254 on DAF and filtration performance. DAF achieved Cryptosporidium log removals of 1.6 to 2.2 without or with recycle of filter backwash. No impacts of recycle were found on filtration, and cumulative (DAF plus filtration) log oocyst removals exceeded 4

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45

Радовенчик, Ярослав Вячеславович, and Вячеслав Михайлович Радовенчик. "FEATURES OF WATER CLARIFICATION PROCESS USING MATERIAL WITH CAPILLARY PROPER-TIES." Proceedings of the NTUU “Igor Sikorsky KPI”. Series: Chemical engineering, ecology and resource saving, no. 1 (May 15, 2017): 78–83. http://dx.doi.org/10.20535/2306-1626.1.2017.119477.

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Zotova, Natalia, Axel Franzke, Alan Armstrong, and Donna G. Blackmond. "Clarification of the Role of Water in Proline-Mediated Aldol Reactions." Journal of the American Chemical Society 129, no. 49 (2007): 15100–15101. http://dx.doi.org/10.1021/ja0738881.

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Sato, Kuniaki, Noriko Iwashima, Toshiyuki Wakatsuki, and Tsugiyuki Masunaga. "Clarification of water movement properties in a multi-soil-layering system." Soil Science and Plant Nutrition 57, no. 4 (2011): 607–18. http://dx.doi.org/10.1080/00380768.2011.594966.

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Zhengong, Tong. "The Vortex Flocculation Clarification Technology and Its Application in Water Treatment." Journal of Computational and Theoretical Nanoscience 13, no. 3 (2016): 1820–25. http://dx.doi.org/10.1166/jctn.2016.5118.

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St-Pierre, Médéric, and Julie M. Thériault. "Clarification of the Water Saturation Represented on Ice Crystal Growth Diagrams." Journal of the Atmospheric Sciences 72, no. 7 (2015): 2608–11. http://dx.doi.org/10.1175/jas-d-14-0357.1.

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Abstract:

It has been known for a long time that the shape of ice crystals depends on both the air temperature and the relative humidity of the environment. The relationships among these factors have been summarized in classification diagrams and are intensively referred to in the cloud physics literature. To put in perspective the atmospheric conditions in which the different ice crystal habits grow with respect to the level of saturation in the atmosphere, the vapor density excess and supersaturation with respect to ice at liquid water saturation have been included on those diagrams as a function of a

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Li, H., and J. Sansalone. "CFD Model of PM Sedimentation and Resuspension in Urban Water Clarification." Journal of Environmental Engineering 146, no. 3 (2020): 04019118. http://dx.doi.org/10.1061/(asce)ee.1943-7870.0001649.

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