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Applied Thermal Engineering
journal homepage: www.elsevier.com/locate/apthermeng
Research Paper
Experimental thermal and hydraulic characterization of R448A and
comparison with R404A during flow boiling
G. Lillo, R. Mastrullo, A.W. Mauro
⁎
, F. Pelella, L. Viscito
Department of Industrial Engineering, Università degli Studi di Napoli – Federico II, P.le Tecchio 80, 80125 Naples, Italy
HIGHLIGHTS
•
Flow boiling heat transfer and pressure drop data of R448A inside a horizontal tube.
•
HTC increases with heat and mass flux. No particular effect of saturation temperature.
•
Possible stratified-wavy flow for G = 150 kg/m
2
s.
•
HTC and pressure drop data compared to R404A values at same operating conditions.
•
Assessment of existing two-phase heat transfer and pressure drop correlations.
ARTICLE INFO
Keywords:
Flow boiling
R448A
Heat transfer coefficient
Pressure drop
Assessment
ABSTRACT
Refrigerant R404A is going to be banned in Europe for different applications due to its very high GWP of 3943.
R448A is a suitable alternative (GWP of 1390) among other new mixtures, and is thus receiving considerable
attention in literature. However, despite several overall system studies, there is a lack of flow boiling data for this
new blend. This paper therefore presents an experimental investigation on two-phase heat transfer and pressure
drop of R448A in a single horizontal stainless steel (AISI 316) tube with an internal diameter of 6.0 mm. The
effect of the operating parameters is firstly analyzed for the whole range of vapor qualities, by changing the mass
flux from 146 to 601 kg/m
2
s and the bubble saturation temperature from 23.3 to 56 °C (reduced pressures from
0.266 to 0.554). For the heat transfer coefficient measurements, the imposed heat flux is also varied from 2.5 to
40 kW/m
2
, leading to a total amount of 460 data points. Several pressure drop and heat transfer coefficient data
are then compared to those of conventional refrigerant mixture R404A at the same operating conditions,
showing different relative importance of nucleate and convective boiling contributions. Finally, the agreement
between the R448A experimental database and some two-phase boiling heat transfer coefficient and frictional
pressure drop prediction methods is evaluated with a statistical analysis. The best results are respectively ob-
tained with the correlations of Gungor and Winterton and of Friedel.
1. Introduction
Refrigerant R404A has been widely used for years in commercial
refrigerators and heat pump systems as a suitable replacement for R22,
having the advantage to be employed also at low evaporating tem-
peratures, thanks to its Normal Boiling Point of 226.7 K [1]. However,
despite its zero-ODP (Ozone Depletion Potential), R404A has a very
high GWP (Global Warming Potential) value of 3943. For these reasons,
fluid leakages and superficial operations during plants dismantlement
are a significant cause of direct greenhouse gas emissions.
The GWP limitations in Europe affecting the commercial systems
where R404A is currently used are expressed by the EU Regulation No
517/2014 [2]. Specifically, stationary refrigeration equipments must
avoid fluids with GWP > 2500 by 2020, whereas multipack cen-
tralized refrigeration systems carry the GWP limit of 150 by 2022 and
refrigerators and freezer should employ fluids with GWP < 2500 in
2020 and GWP < 150 in 2022.
Despite the political effort in reducing the direct greenhouse gas
emissions, there is not a definitive solution to replace high GWP re-
frigerants, but numerous alternatives have been proposed, as reviewed
by Mota-Babiloni et al. [3]. Particularly, HFC mixtures R407A, R407F
and R422A have been presented as light retrofit fluids for R404A,
showing a similar or even higher efficiency with half of the GWP [4],
but with an economical drawback of a high purchase cost [5]. Other
https://doi.org/10.1016/j.applthermaleng.2019.114146
Received 23 January 2019; Received in revised form 4 June 2019; Accepted 16 July 2019
⁎
Corresponding author.
E-mail address: alfonsowilliam.mauro@unina.it (A.W. Mauro).
Applied Thermal Engineering 161 (2019) 114146
Available online 17 July 2019
1359-4311/ © 2019 Published by Elsevier Ltd.
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