Open AccessTHERMAL INTEGRATION OF COMPRESSION REFRIGERATION UNITS IN DAIRY FACILITIES
Author(s) -
Serhii Bykanov,
Tatiana Babak,
Roman Stotskyi
Publication year - 2021
Publication title -
vestnik nacionalʹnogo tehničeskogo universiteta "hpi". himiâ, himičeskaâ tehnologiâ i èkologiâ/vìsnik nacìonalʹnogo tehnìčnogo unìversitetu "hpì". serìâ: himiâ, himični tehnologiï ta ekologiâ
Language(s) - English
Resource type - Journals
eISSN - 2708-5252
pISSN - 2079-0821
DOI - 10.20998/2079-0821.2021.01.14
Subject(s) - heat exchanger , refrigeration , pinch analysis , subcooling , refrigerant , cooling capacity , streams , chiller , environmental science , heat recovery ventilation , thermodynamics , heat transfer , computer network , physics , computer science
The heat integration of an ammonia compression refrigeration unit, that is used in different dairy facilities, was carried out by the pinch analysis methods. The schematic diagram of such unit with a cooling capacity of 1000 kW was taken as a basis. The main cycle temperatures, refrigerant consumption and its specific heat capacity were calculated for a given refrigerating capacity. Based on these data, a stream table was formed, that included a hot stream of a refrigerant – ammonia – and also two cold streams: water for chemical water treatment and water for technology. The hot stream of ammonia was divided into three streams: cooling of ammonia vapors, condensation and subcooling. Heat capacities flowrates and heat loads (stream enthalpy change) of the streams were determined. The minimum temperature difference in heat exchangers DTmin = 8°С was determined on the basis of technical and economic calculations for this process. The composite curves were plotted for the minimum temperature difference. The pinch temperatures were determined by the problem table algorithm for the hot and cold streams. The minimum values of hot and cold utilities load (QHmin and QСmin) were determined. The heat recovery capacity was determined, which was 701.8 kW. A grid diagram was built and heat exchangers are arranged in accordance with CP and N rules. The retrofit of process flowsheet is proposed on the basis of the grid diagram that includes the installation of three heat exchangers, one cooler and two heaters to achieve the target temperatures and flow rates. The use of Alfa Laval plate heat exchangers is proposed as heat exchange equipment. The payback period of the design is about two years.