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dc.contributor.authorKravchenko, Volodymir-
dc.contributor.authorSurkov, Sergii-
dc.contributor.authorGhanem, Hussam-
dc.date.accessioned2019-11-29T06:58:34Z-
dc.date.available2019-11-29T06:58:34Z-
dc.date.issued2016-
dc.identifier.citationKravchenko, V., Surkov, S., Hussam Ghanem. (2016). Modelling and optimization of seawater desalination process usung mechanical vapour compression. Odes`kyi polytechnichnyi Universytet, Pratsi, 2 (49), 47-55.en
dc.identifier.citationKravchenko, V. Modelling and optimization of seawater desalination process usung mechanical vapour compression / V. Kravchenko, S. Surkov, Hussam Ghanem // Пр. Одес. політехн. ун-ту. – Одеса, 2016. - Вип. 2 (49). - P. 47-55.en
dc.identifier.otherDOI: 10.15276/opu.2.49.2016.08-
dc.identifier.urihttp://dspace.opu.ua/jspui/handle/123456789/9714-
dc.description.abstractIn the conditions of global climate changes shortage of fresh water becomes an urgent problem for an increasing number of the countries. One of the most perspective technologies of a desalting of sea water is the mechanical vapour compression (MVC) providing low energy consumption due to the principle of a heat pump. Aim: The aim of this research is to identify the reserves of efficiency increasing of the desalination systems based on mechanical vapour compression by optimization of the scheme and parameters of installations with MVC. Materials and Methods: The new type of desalination installation is offered which main element is the heat exchanger of the latent heat. Sea water after preliminary heating in heat exchangers comes to the evaporator-condenser where receives the main amount of heat from the condensed steam. A part of sea water evaporates, and the strong solution of salt (brine) goes out of the evaporator, and after cooling is dumped back in the sea. The formed steam is compressed by the compressor and comes to the condenser. An essential singularity of this scheme is that condensation happens at higher temperature, than evaporation. Thanks to this the heat, which is comes out at devaporation, is used for evaporation of sea water. Thereby, in this class of desalination installations the principle of a heat pump is implemented. Results: For achievement of a goal the following tasks were solved: the mathematical model of installations with MVC is modified and supplemented; the scheme of heat exchangers switching is modified; influence of design data of desalination installation on the cost of an inventory and the electric power is investigated. The detailed analysis of the main schemes of installation and mathematical model allowed defining ways of decrease in energy consumption and the possible merit value. Influence of two key parameters - a specific power of the compressor and a specific surface area of the evaporator-condenser - on a value of given expenses of desalination installation is analyzed. The optimum ratio of these parameters is defined.en
dc.language.isoen_USen
dc.publisherOdessa Politechnic Universityen
dc.subjectdesalting of sea wateren
dc.subjectmechanical vapour compressionen
dc.subjectnumerical modelingen
dc.titleModelling and optimization of seawater desalination process usung mechanical vapour compressionen
dc.title.alternativeМоделювання й оптимізація процесу опріснення морської води в установках з механічним стисненням париen
dc.typeProfessional articleen
opu.kafedraКафедра прикладної екології та гідрогазодинамікиuk
opu.citation.journalOdes'kyi Politechnichnyi Universytet. Pratsien
opu.citation.volume49en
opu.citation.firstpage47en
opu.citation.lastpage55en
opu.citation.issue2en
opu.staff.idssv@opu.uaen
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