scholarly journals Calculated dependence of determination of actual dose of microsand and influence of its value on efficiency of coagulation process in Actiflo clarifier

Vestnik IGEU ◽  
2021 ◽  
pp. 5-12
Author(s):  
E.A. Karpychev

Operational test of the preliminary water cleaning systems is the first and most critical stage when putting into pilot operation a water treatment plant at a thermal power plant (TPP). We have sufficient experience of equipment setting up and operating when most traditional devices of preliminary water purification are used. Also, the main stages and features of the work carried out are known, and a sufficient amount of methodological literature has been published, compared to employment of modern and promising devices. These devices include Actiflo clarifiers. The main feature of the Actiflo technology is introduction of microsand into the stream of treated water. It forms the so-called “centers” of coagulation and is used to make wastewater sludge heavier. The development of a methodology to assess the impact of the actual dose of microsand on the water clarification process will contribute to the solution of the priority task of adapting the promising Actiflo technology for water treatment systems of TPPs. In laboratory studies, the method of pilot coagulation has been used. It allows us to assess the efficiency of coagulation process using generally accepted methods of quantitative analysis of indicators of natural water quality. In subsequent industrial tests, along with the quantitative analysis of water, the actual value of the microsand dose has been assessed using measurements of the proportions of separate fractions in the formed sand-sludge pulp. The results of laboratory and industrial studies of “cold” coagulation process of the Kama River water using Actiflo clarifiers have been obtained. The dependence of efficiency effect of water clarification on the dose of coagulant and the dose of microsand has been determined. To check and maintain the operating mode of the clarifier, a method to assess the actual values of the microsand dose has been developed and proposed. The research results are applicable for low-turbidity colored surface water sources. The results of operating tests of Actiflo clarifiers can be used as practical examples for coagulating water in devices similar in design, for example, VTI-M clarifiers. The proposed method to assess the actual dose of microsand can be used as a technological parameter during the development of the parameter tables when Actiflo clarifiers are used.

2021 ◽  
Author(s):  
Tara Callingham ◽  
Daniel Ooi ◽  
Linhua Fan ◽  
Felicity Roddick

Abstract Feedwater to Euroa Water Treatment Plant contains increasingly high levels of natural organic matter (NOM) which were determined to cause its strong earthy odour. A multidisciplinary approach was used to evaluate the coagulation process to better remove the taste and odour (T&O) causing organics from water supplied to the local towns. Such high levels of NOM require elevated doses of coagulant for removal, accounting for approximately 60% of the chemical costs. A need arose to reduce these operational costs. However, community expectations regarding T&O, and social and environmental impacts, are not typically considered in this process. The local water corporation, Goulburn Valley Water, undertook a case study involving a comparison of three coagulants to optimise the chemical coagulation process from a multidisciplinary (triple bottom line, TBL) perspective. The financial assessment incorporated operational costs and potential infrastructure requirements. The social assessment investigated the overall impacts on staff operating the water treatment plant and their broader community involvement. The environmental assessment focused on the impact on downstream infrastructure from changes in sludge volumes and wastewater quality, and third-party greenhouse gas emissions from chemical deliveries. From a TBL viewpoint, aluminium chlorohydrate was the most beneficial option.


1992 ◽  
Vol 26 (5-6) ◽  
pp. 1255-1264
Author(s):  
K. L. Martins

During treatment of groundwater, radon is often coincidentally removed by processes typically used to remove volatile organic compounds (VOCs)-for example, processes such as liquid-phase granular activated carbon (LGAC) adsorption and air stripping with vapor-phase carbon (VGAC). The removal of radon from drinking water is a positive benefit for the water user; however, the accumulation of radon on activated carbon may cause radiologic hazards for the water treatment plant operators and the spent carbon may be considered a low-level radioactive waste. To date, most literature on radon removal by water treatment processes was based on bench- or residential-scale systems. This paper addresses the impact of radon on municipal and industrial-scale applications. Available data have been used todevelop graphical methods of estimating the radioactivity exposure rates to facility operators and determine the fate of spent carbon. This paper will allow the reader to determine the potential for impact of radon on the system design and operation as follows.Estimate the percent removal of radon from water by LGAC adsorbers and packed tower air strippers. Also, a method to estimate the percent removal of radon by VGAC used for air stripper off-gas will be provided.Estimate if your local radon levels are such that the safety guidelines, suggested by USEPA (United States Environmental Protection Agency), of 25 mR/yr (0.1 mR/day) for radioactivity exposure may or may not be exceeded.Estimate the disposal requirements of the waste carbon for LGAC systems and VGAC for air stripper “Off-Gas” systems. Options for dealing with high radon levels are presented.


1996 ◽  
Vol 68 (7) ◽  
pp. 1179-1186 ◽  
Author(s):  
Stephen D. J. Booth ◽  
Daniel Urfer ◽  
Gerard Pereira ◽  
Karl J. Caber

2019 ◽  
Vol 124 ◽  
pp. 01029
Author(s):  
A. A. Filimonova ◽  
N. D. Chichirova ◽  
A. A. Chichirov ◽  
A. I. Minibaev

The main sources of highly concentrated multicomponent technological solutions at thermal power plants (TPPs) are water treatment plants. Analysis of operation of the ion-exchange water treatment plant at the Nizhnekamsk Thermal Power Plant-1 showed that half of alkali supplied to regeneration of the anion-exchange alkali filters is not used, but is discharged for neutralization and then to wastewater. Due to the fact that the cost of alkali used in technological processes is quite high, it is economically feasible to process the alkaline waste with the alkali extraction and its reuse in the production cycle. The article presents the experimental results on the electro-membrane separation of alkaline waste regeneration solutions and wash water after anion-exchange filter regeneration. The revealed differences in the selectivity of various ion transfer through the electrodialysis apparatus membranes, depending on time and amount of transmitted electricity, allowed us to establish the possibility of obtaining an alkaline solution purified from impurities.


2015 ◽  
Vol 46 (4) ◽  
pp. 291-335 ◽  
Author(s):  
M. Pivokonsky ◽  
J. Naceradska ◽  
I. Kopecka ◽  
M. Baresova ◽  
B. Jefferson ◽  
...  

2010 ◽  
Vol 2010 ◽  
pp. 1-10 ◽  
Author(s):  
E. V. Grigorieva ◽  
E. N. Khailov

A model of a waste water treatment plant is investigated. The model is described by a nonlinear system of two differential equations with one bounded control. An optimal control problem of minimizing concentration of the polluted water on the given time interval is stated and solved analytically with the use of the Pontryagin Maximum Principle and Green's Theorem. Computer simulations of a model of an industrial waste water treatment plant show the advantage of using our optimal strategy. Possible applications are discussed.


2020 ◽  
Vol 216 ◽  
pp. 01083
Author(s):  
Alena Vlasova ◽  
Sergei Vlasov

АnnotationTechnological installation of waste water disposalafter washing of H-cation filters is quite promising idea of avoiding penalties and reuse of waste water in cycle of thermal power plants (TPP). The development of this unit is based on reactions that occur when mixing several TPP water treatment plant wastes, namely, neutralization and exchange-type reactions. As neutralizing reagent, the sludge of the water treatment plant is used, which consists of CaCO3 by 80%. This method reduces the concentration of sul-phate-containing components in wastewater to a standard level, and also provides neutral wastewater with-out the use of additional purchase reagents.


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