Кафедра "Інтегровані технології, процеси і апарати"

Постійне посилання колекціїhttps://repository.kpi.kharkov.ua/handle/KhPI-Press/1789

Офіційний сайт кафедри http://web.kpi.kharkov.ua/itpa

Від 2005 року кафедра має назву "Інтегровані технології, процеси і апарати", первісна назва – кафедра загальної хімічної технології, процесів і апаратів.

Кафедра загальної хімічної технології, процесів і апаратів створена в 1933 році, а очолив її професор Максим Ісидорович Некрич, який у свій час закінчив Паризький університет – Сорбонну (Франція). Але ще в 1927 році професор М. Д. Зуєв починає читати студентам курс загальної хімічної технології, доповнюючи його розрахунком процесів і апаратів, а також контрольно-вимірювальних приладів. У 1964 році від кафедри загальної хімічної технології, процесів і апаратів відокремилася нова кафедра – "Автоматизації хімічних виробництв".

Від 1977 року кафедру очолював Леонід Леонідович Товажнянський, кандидат технічних наук, доцент, на той час проректор ХПІ, а згодом – доктор технічних наук, професор, Заслужений діяч науки і техніки України, Заслужений працівник вищої школи, лауреат Державної премії, Дійсний член Академії наук вищої школи України, ректор НТУ «ХПІ». Виконувачем обов’язків завідувача кафедри у період з 1977 по 1981 роки був І. С. Чернишов.

Від 1 лютого 2018-го року кафедра входить до складу Навчально-наукового інституту хімічних технологій та інженерії Національного технічного університету "Харківський політехнічний інститут".

У складі науково-педагогічного колективу кафедри працюють: 2 доктора та 12 кандидатів технічних наук; 2 співробітника мають звання професора, 11 – доцента.

Переглянути

Фільтри

2016 - 20183

Налаштування

Автор: search.filters.author.Babak, Tatyana

Результати пошуку

Зараз показуємо 1 - 3 з 3
  • Ескіз
    Документ
    The innvestigation of the process streams integration in the multi­effect evaporation plant for the concentration of sorghum syrup
    (Технологический центр, 2018) Babak, Tatyana; Golubkina, Olga; Ponomarenko, Yevgeniya; Solovey, Ludmila; Khavin, G. L.
    The study on the integration of heat streams of the evaporation station for sorghum syrup concentrating is presented. The relevance of the research is is why the research, aimed at reducing the consumption of external energy and enhancing operating efficiency, is relevant and has practical value. The main purpose of the work is to create a scientifically substantiated design with enhanced economic indicators of operation, ensuring saving in consumption of hot utility (steam) and cooling water. The problem was solved using the pinch-analysis. Heat streams, requiring heating and cooling, were identified, and the alternative project based on the selection of the value of minimum temperature difference ΔTmin, was created. This value was calculated and substantiated based on the data on thermal streams. The stream of condensate of return steam, the heat excess of which had not been used so far, was added to the system. For the alternative project, the layout of heat exchange equipment was proposed, calculation of plate heat exchangers was performed. The designed network of heat exchangers made it possible to decrease the annual steam consumption by 18 %. Cost-effectiveness analysis was conducted by comparing the indicators for two of the projects of the syrup preheating department for the evaporation station. The proposed alternative project saves power consumption of cooling water by 35.9 kW, of heating vapor steam – by 60.5 kW. At the interest rate of profit tax of 18 %, implementation of the alternative project will pay off in 4 months. As a result, net annual gain of an enterprise is planned to increase by 16 %, at virtually the same payback period of the projects. Application of the methods of heat streams integration made it possible to develop an effective project of sorghum syrup preheating before evaporation and ensure saving of external utilities.
  • Ескіз
    Документ
    Advantages of using channels with different corrugation height in the plate heat exchangers
    (Технологический центр, 2018) Khavin, G. L.; Babak, Tatyana
    In the case when there is a difference in consumption on the side of the cold and hot heat carriers, the use of channels with the same corrugation height in one heat exchanger leads to a decrease in velocity of the heat carrier on the side with low consumption. Low velocity contributes to appearance of deposits on the heat transfer surface, which leads to disruption of operation mode of the apparatus and a forced clean-up stop. In case of using channels with a different corrugation height (cross-section area), velocities in the channels are aligned and intensity of emergence and growth of contamination falls sharply. It also allows us to reduce the heat transfer surface area of the apparatus and fully implement permissible pressure losses on the sides of the heat exchanger. For designing of heat exchangers of this structure, the authors developed the mathematical model that allows making calculations of heat exchangers for assigned operation conditions with the use of geometrical data of the plates, thermophysical properties of heat carriers and criterial equations for plates of the selected type. The calculation algorithm involves determining of the ratio between corrugation heights. Practical value lies in the fact that the proposed approach makes it possible to extend the service life of the heat exchanger prior to a maintenance stop. This enables provision of continuity of the technological process and decreases operation costs. Calculation of the heat exchanger of hot water supply by the parallel scheme of attachment to heating networks and the heat exchanger of stage 1 of the two-stage hybrid scheme was presented. Calculation data indicate a decrease in the heat transfer surface area compared to heat exchangers with channels of equal height, full realization of pressure losses and their alignment in the channels, which facilitates an increase in resistance to contamination of the plates’ surface. Calculation showed the advantage of using apparatuses with channels of different cross-section area. The higher the ratio between consumption of heat carriers in the channels, the stronger this advantage.
  • Ескіз
    Документ
    Possibility of Heat Pump use in Hot Water Supply Systems
    (2016) Babak, Tatyana; Duić, Neven; Khavin, G. L.; Boldyryev, Stanislav; Krajačić, Goran
    The problem of modernization of the heat module with two-stage mixing scheme connection of hot water supply by installations of the heat pump during interheating period is considered. Heating water of the in-house circuit of the building heating system is used as a heat source for heat pump. The district cooling of the residential areas is possible through the heaters during the summer. R600 refrigerant is chosen for heat pump for its environmental-friendliness and low-pressure of evaporation and condensation. The economic calculation is made for interheating period comparing the operation with and without heat pump. This paper advances selection of optimum amount of heat to be recovered during low potential heat utilisation and targets for heating and cooling capacities.