Improving of thermohydraulic method for calculation of steam contact heat and mass exchange equipment

dc.contributor.authorBondar, Vladimir
dc.contributor.authorZaporozhets, Oleksandr
dc.contributor.authorSapiga, Victoria
dc.date.accessioned2024-06-04T08:39:00Z
dc.date.available2024-06-04T08:39:00Z
dc.date.issued2023
dc.description.abstractIntroduction. The complexity of determining the contact surface of phases and the boundaries of the continuous structure of liquid jets complicates the calculation of phase-contact heat and mass exchange mixing apparatuses. Materials and methods. The condensation process of water steam from a steam-gas mixture on a cylindrical free-falling liquid jet is considered under counter-current movement of the steam phase within a range of flow parameters characteristic of the food industry. Results and discussion. An empirical dependence for determining the onset of jet structure destruction adequately describes the process of its structural changes and is characterized by the fact that an increase in the Reynolds number leads to an increase in the critical height of jet destruction: the jet becomes more resistant to the action of the steam flow. With an increase in the dynamic pressure of the steam flow, corresponding to an increase in the Weber number, which characterizes a sharp decrease in the dimensionless height of dispersion, the jet intensively disintegrated, was destroyed at the outflow point, and was carried away by the steam flow. An original system of dimensionless similarity numbers, based on the results of jet hydrodynamics analysis, allows for determining the temperature change along the jet's length, taking into account the geometric characteristics of mixing heat exchanger distribution devices, flow geometric dimensions, steam-liquid flow parameters, and the thermophysical properties of the media. Empirical dependencies of the heat exchange process, considering the critical height of the existence of the continuous jet structure, are recommended for use in the thermohydraulic calculations of direct phase-contact heat exchange equipment. Conclusion. The novelty of the results lies in the introduction of empirical dependencies for calculating heat exchange, considering the critical height of the existence of the continuous structure of the liquid jet.
dc.identifier.citationBondar, V. Improving of thermohydraulic method for calculation of steam contact heat and mass exchange equipment / V. Bondar, O. Zaporozhets, V. Sapiga // Ukrainian Journal of Food Science. – 2023. – Volume 11, Issue 2. – Pp. 122-133
dc.identifier.orcidhttps://orcid.org/0000-0002-8106-4174
dc.identifier.orcidhttps://orcid.org/0000-0001-7171-624X
dc.identifier.urihttps://dspace.nuft.edu.ua/handle/123456789/43316
dc.language.isoen
dc.subjectsteam
dc.subjectjet
dc.subjectcondensation
dc.subjectheat exchange
dc.subjectmass exchange
dc.subjectequipment
dc.subjectпара
dc.subjectконденсат
dc.subjectтеплообмін
dc.subjectмасообмін
dc.subjectобладнання
dc.subjectкафедра процесів і апаратів харчових виробництв
dc.subjectкафедра теплоенергетики та холодильної техніки
dc.subjectкафедра мехатроніки та пакувальної техніки
dc.titleImproving of thermohydraulic method for calculation of steam contact heat and mass exchange equipment
dc.typeArticle

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