Перегляд за Автор "Sydorenko, V."

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    Discrete-pulsed energy input in wastewater treatment technologies
    (КПІ ім. Ігоря Сікорського; ТОВ «Українська водна спілка», 2022) Obodovych, O.; Sabliy, L.; Sydorenko, V.; Pereiaslavtseva, O.; Khomenko, V.
    Wastewater treatment is an important environmental problem of the national economy of any country. Therefore, increasing the efficiency of wastewater treatment through the use of innovative technologies and equipment is becoming relevant. Basically, for the biological treatment of wastewater from organic and biogenic pollution, aerotanks with different aeration systems are used. The aeration and mass transfer of the mixture of waste water and activated sludge accounts for up to 80 % of operating costs. The article deals with the problems of using thermal physics in wastewater treatment by intensifying the mass transfer process and accelerating the biological oxidation reaction. The intensification occurs due to the impact on the treated medium (waste water) of the input energy by the discrete-pulse method. The method is implemented using new heat and mass transfer equipment, namely a rotary-type aerator-oxidizer (AORT). A diagram of a rotary-type aerator-oxidizer and a technological scheme for biological wastewater treatment using this apparatus are presented. A procedure has been developed for determining the volumetric coefficient of oxygen mass transfer from the gas phase to the liquid phase during biological wastewater treatment. A number of studies have been carried out on the dependence of the concentration of oxygen dissolved in water on the number of treatment cycles at: different angular speed of rotation of the rotor unit; different frequencies of flow pulsations; different flow shear rates. It is shown that the maximum concentration of dissolved oxygen is reached in 1–2 passes through the apparatus of the processed mixture. The thermophysical and energy characteristics of the operation of a rotary-type aeration-oxidation plant are determined depending on the frequency of flow pulsations. A comparative assessment of the heat-mass exchange and energy indicators of modern aeration devices used for wastewater treatment with the AORT installation has been carried out and it has been shown that when using the AORT installation, energy costs for aeration are reduced by 20 %.
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    Intensification of the absorption of oxygen by water using a rotor-pulsating apparatus
    (КПІ ім. Ігоря Сікорського; ТОВ «Українська водна спілка», 2022) Sablii, L.; Obodovych, O.; Sydorenko, V.
    One of the important components of the quality of food products is the quality of water used. A common way to remove unwanted impurities from water is aeration, i.e. the oxidation of chemical compounds in water by oxygen. Aeration devices with mechanical energy input in comparison with other groups of devices, namely with energy input with gas phase and with liquid phase, have low power consumption and additional mixing of the processed medium. The work presents a study of oxygen absorption in water in an experimental setup with rotor-pulsating apparatus for water treatment in beverage production technology. In this paper, the energy and technological parameters of aeration of a model aqueous solution of a certain concentration of sodium sulfide in an experimental setup with a rotor-pulsating apparatus as an aerator are determined. The experimental aeration setup allows conducting research in several modes and consists in particular of a vessel, a rotor-pulsating apparatus, two ejectors - one at the entrance to the rotor-pulsating, the other at the outlet, the recirculation pipeline. Air from the atmosphere enters each of the ejectors through a separate air duct. The aeration of the studied water took place in the recirculation mode for 20 minutes. Determination of the oxygen mass transfer rate is determined by the iodometric titration method on the rate of oxidation of sodium sulfite. Experiments were conducted without using a catalyst. It is determined that when placing the ejector unit at the rotorpulsating apparatus inlet at the angular rotor unit velocity of 240.02; 270.18, and 300.02 s-1, the oxygen mass transfer rate is 1.39; 1.49 and 1.73 kg m3 /h. At the location of the ejector unit at the outlet of the rotor-pulsating apparatus, the velocity of the oxygen mass transfer under the same conditions is 1.17; 1.36 and 1.63 kg m3 /h respectively. However, the power consumption of the second scheme exceeds the power consumption by the first scheme by 50%.