Abstract
The article presents the fundamental principles of mixing condensers calculation. The design calculation flow chart of apparatuses of this type is proposed. A good convergence of the droplet motion hydromechanics with the other authors works results is identified. The operating conditions calculation results of the contact condenser as a part of the chemical energy unit with hydrocarbon raw material partial oxidation showed that mass transfer impact on the heat exchange is quite significant (the Gukhman criterion is 0.0076), which affects the high process intensity (heat transfer coefficient is ∼179 W/(m2·°C)). However, as expected, the device is characterized by the low resistance of ∼6 Pa.
Export citation and abstract BibTeX RIS
Content from this work may be used under the terms of the Creative Commons Attribution 3.0 licence. Any further distribution of this work must maintain attribution to the author(s) and the title of the work, journal citation and DOI.