Faculty Publications

Now showing 1 - 4 of 4

Basic concepts of ultrasound and its effects on fuel processing
(Bentham Science Publishers, 2023) Poddar, M.K.; Dikshit, P.K.; Chakma, S.
Ultrasound-assisted technique is well-known for process intensification via chemical and physical changes under the influence of acoustic cavitation. Acoustic cavitation is the phenomenon of nucleation, growth, and collapse of cavitation bubbles into a liquid medium that augments the reaction kinetics and the final process yield. This chapter provides a fundamental and detailed understanding of the acoustic cavitation phenomenon. It includes the history and origin of the acoustic wave and its formation, the concept of cavitation bubbles, bubble nucleation and growth mechanism, cavitation effects, and its types. Numerous process parameters, such as applied frequency, intensity, temperature, dissolved gas content, etc., also directly or indirectly influence the cavitation threshold are also highlighted. Further, the ultrasound's physical and chemical effects involving various chemical and biochemical processes to enhance the process yield are also reviewed. The mode of generation of ultrasound energy and its measurement technique are also briefly discussed. Finally, an overview of modeling and simulation of radial motion of single bubble growth, its oscillation in both ultrasound-assisted and conventional systems, and bubble growth rate under rectified diffusion are also discussed in detail. © 2023 Bentham Science Publishers. All rights reserved.
Nucleate pool boiling heat transfer measurement and flow visualization for ammonia-water mixture
(2011) Sathyabhama, A.; Ashok Babu, T.P.
Visualization of bubble nucleation during nucleate pool boiling outside a vertical cylindrical heated surface was done for ammonia-water binary mixture in order to obtain a descriptive behavior of the boiling, which was directly compared with the measured heat transfer coefficient data at low pressure of 4-8 bar and at low mass fraction of 0 < x < 0.3 and at different heat flux. Still images taken with high speed camera are used to demonstrate the decrease in boiling heat transfer coefficient with increase in ammonia mass fraction. Jensen and Memmel model has better agreement with experimental bubble diameter. Further work is required to obtain quantitative information about bubble nucleation parameters. It is found that both Calus and Rice and Stephan-Koorner correlation can predict the experimental heat transfer coefficient values with a maximum deviation of ±20%. © 2011 American Society of Mechanical Engineers.
Heat transfer and force balance approaches in bubble dynamic study during subcooled flow boiling of water–ethanol mixture
(Taylor and Francis Ltd. michael.wagreich@univie.ac.at, 2018) Suhas, B.G.; Sathyabhama, A.
In this paper, the subcooled flow boiling heat transfer coefficient of pure water, water–ethanol mixture and pure ethanol is determined experimentally in horizontal rectangular channels for various parameters like heat flux, mass flux and channel inlet temperatures. Flow visualization is carried out using high speed camera. The bubble departure diameter, growth period and waiting period of bubbles are determined. Correlations are developed for subcooled flow boiling Nusselt number of water–ethanol mixture based on force balance approach and heat transfer approach. The parameters considered for correlation are grouped as dimensionless numbers by Buckingham ?-theorem. The significance of each dimensionless number on heat transfer coefficient is discussed. The correlations developed for subcooled flow boiling heat transfer coefficient are validated with the experimental data. They are found to be in good agreement with the experimental data. It is found that the correlation based on force balance approach predicts the subcooled flow boiling Nusselt number well when compared with that of heat transfer approach correlation. © 2017 Taylor & Francis.
Enhanced boiling heat transfer of water on a liquid-infused surface
(Elsevier Ltd, 2023) Prasad Yandapalli, A.V.V.R.; Moreno Resendiz, E.M.; Kuravi, S.; Sathyabhama, S.; Kota, K.
The aim of this study was to experimentally demonstrate a counter-intuitive phenomenon that a surface covered with a liquid has the potential for enhancing heat transfer for the boiling of water over it. To this end, a highly-wetting surface with a zero contact angle for multiple liquids, i.e., an Ultra-Omniphilic Surface (UOS) was prepared on aluminum (Al 6061 alloy) using a simple and easy-to-implement bulk micro-manufacturing approach and a non-boiling liquid (NBL) was infused over this surface to occupy its sub-surface micro/nano-cavities. The resulting liquid-infused UOS is called a Binary Surface (BiS) for it has two distinct superficial phases — solid phase as islands and liquid phase as NBL puddles. Saturated nucleate pool boiling experiments were conducted on the BiS and the critical heat flux (CHF) and the boiling heat transfer coefficient (HTC) were measured. The results were compared with the UOS and a plain/polished surface (PS) prepared from the same aluminum alloy sample. In addition, high-speed visualization was employed for capturing the bubble dynamics at different heat fluxes and parameters such as bubble departure diameter (Dd), bubble departure frequency (f), and nucleation site density (NSD) were measured. The results revealed that the nucleate pool boiling performance of water on the BiS surpasses both the PS and the UOS. The HTC on the BiS was 1.33 times and two times larger than the UOS and the PS, respectively. The CHF obtained on the BiS was comparable to that on the UOS and 1.47 times larger than that on the PS even though a considerable portion of the BiS surface area was covered with the NBL and unavailable for boiling. Remarkably, an inspection of the high-speed videos has suggested the presence of the same NBL as the reason for the better boiling heat transfer performance of the BiS. The NBL that was spread over the BiS as puddles was found to (1) prevent the growth of large vapor bubbles and (2) extend the isolated bubble regime by delaying the lateral coalescence of adjacent bubbles. A comparison of the results between UOS and BiS suggests that – as far as boiling enhancement is concerned – mechanisms for tackling vapor bubbles could be superior to those that involve improving surface wettability. © 2023

Faculty Publications

Browse

Filters

Settings

Sort By

Results per page

Search Results