Abstract
Plate heat exchangers (PHE) are of primary importance for many technical applications. To use PHE effectively it is necessary to calculate the pressure drop correctly. Unfortunately, in open literature a large difference between the different authors occurs. As shown in an earlier work (Gusew and Stuke in Int J Chem Eng vol. 2019, 6) an essential portion of this difference lies in the pressure drop of the distribution zone. In this work new geometrical parameters are introduced to calculate the pressure drop of the distribution zone. The resulting correlations with new parameters include the pressure drop of both corrugated field and distribution zones. This new three-component model for hydraulic resistance show good agreement with experimental data for PHEs in turbulent flow regime. Furthermore, observed differences in data of other authors can be explained by the influence of the new introduced geometrical parameters of the distribution zone.
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Abbreviations
- a, b:
-
Coefficient in Eq. (14), dimensionless
- \(\overline a,\overline b\) :
-
Coefficient in Eq. (15), dimensionless
- A:
-
Area, m2
- AEC:
-
Area enlargement coefficient, dimensionless
- B, b:
-
Width, m
- D:
-
port diameter, m
- De :
-
equivalent diameter, =2t, m
- f:
-
Fanning friction factor
- GPI:
-
geometrical parameter acc. to Eq. (10), dimensionless
- L, l:
-
Length, m
- N:
-
number of parallel channels in distribution zone, dimensionless
- Npl:
-
number of different plate types in experiments, dimensionless
- Re:
-
Reynolds number, dimensionless, Re = pwDe/μ
- t:
-
wave amplitude of corrugation, m
- w:
-
velocity, m/s
- γ = 2t / Λ – :
-
geometrical parameter of corrugated field, dimensionless
- ε:
-
Error in Eq. (16), %
- Δp:
-
pressure losses, Pa
- Λ:
-
wavelength of corrugation, m
- μ:
-
dynamic viscosity, kg/(m∙s)
- ρ:
-
density, kg/m3
- φ:
-
chevron corrugation angle relative to flow direction, degree
- corr:
-
corrugation
- ch:
-
channel
- inlet:
-
inlet
- mean:
-
mean
- outlet:
-
outlet
- pl:
-
plate
- port:
-
inlet/outlet port
- se:
-
sudden expansion
- st:
-
static height difference
References
Arsenyeva O, Kapustenko P, Tovazhnyanski L, Khavin G (2013) The Influence of plate corrugations geometry on plate heat exchanger performance in specified process conditions. Energy 57:201–207
Akturk F, Uzol NS, Aradag S, Kakaҫ S (2015) Experimental investigation and performance analysis of a gasketed - plate heat exchangers. J Therm Sci Technol 35(1):43–52
Bond MP (1981) Plate Heat Exchangers for Effective Heat Transfer, Institution of Chem Eng GKD-ID: 57277, Band 162/67 April 1981, London, pp.162–167
Dovic D, Palm B, Svaic S (2009) Generalized correlations for predicting heat transfer and pressure drop in plate heat exchanger channels of arbitrary geometry. IJHMT 52:4553–4563
Gulenoglu C, Akturk F, Aradag S, Uzol NS (2014) Experimental comparison of performances of three different plates for gasketed plate heat exchangers. Int J Therm Sci 75:249–256
Gusew S, Stuke R (2019) Pressure Drop in Plate Heat Exchangers for single-phase Convection in Turbulent flow Regime: Experiment und Theory. Int J Chem Eng vol. 2019, Artikel ID 3693657, 11 pages
Focke WW, Zachariades J, Olivier I (1985) The effect of the corrugation inclination angle on the thermohydraulic performance of plate heat exchangers. IJHMT 28–8:1469–1479
Kays WM, London AL (1998) Compact Heat Exchangers, 3rd edn. Krieger Publ Comp
Khan TS, Khan MS, Ayub ZH (2017) Single phase flow pressure drop analysis in a plate heat exchanger. Heat Transfer Eng P.34.https://doi.org/10.1080/01457632.2016.1177430
Kumar B, Soni A, Singh SN (2018) Effect of geometrical parameters on the performance of chevron type plate heat exchanger. Exp Therm Fluid Sci 91:126–133
Kumbhare MB, Dawande SD (2013) Performance Evaluation of plate heat exchanger in laminar and turbulent flow conditions. Int J Chem Sci Appl 4(1):77–83
Lee E, Kang H, Son J, Kim Y (2012) The Performance characteristics of plate heat exchangers used in District heating and cooling with geometric design parameters. The 13th Int Symp District Heating Cooling
Martin H (1996) A theoretical approach to predict the performance of chevron-type plate heat exchanger. Chemical Engineering Process 35:301–310
Muley A, Manglik RM (2000) Enhanced thermal - hydraulic Performance Optimization of Chevron plate heat exchanger. Int J Heat Exch I:3–18
Sarraf K, Launay S, Tadrist L (2015) Complex 3D-flow analysis and corrugation angle effect in plate heat exchangers. Int J Therm Sci 94:126–138
Shah RK, Focke WW (1988) Plate Heat Exchangers and their Design Theory. In: Shah RK (ed), Subbarao EC, Maskelkar RA. Heat Transfer Equipment Design, Hemisphere Publishing Corp. Washington, DC: 227–254
Shaji K, Das SK (2013) Effect of plate Characteristics on Axial Dispersion and Heat Transfer in Plate Heat Exchangers. J Heat Transfer 135:041801-1 - 041801-10
Thonon B, Vidil R, Marvillet C (1995) Recent Research and Developments in Plate Heat Exchangers. J Enhanc Heat Transfer 2(1–2):149–155
Vakili-Farahani F, Amalfi RL, Thome JR (2014) Two-phase flow and boiling of R245FA in a 1 mm pressing depth plate heat exchanger. Part I: Adiabatic pressure Drop. Interfacial Phenom Heat Transfer 2(4): 325-342. Part II: Flow boiling heat transfer, Interfacial Phenom Heat Transfer, 2(4): 343-361
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Authors would like to thank firma Funke Wärmeaustauscher Apparatebau GmbH for providing the opportunity to publish this work.
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Gusew, S., Stuke, R. Plate heat exchangers: calculation of pressure drop for single phase convection in turbulent flow regime. Heat Mass Transfer 58, 419–430 (2022). https://doi.org/10.1007/s00231-021-03099-6
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DOI: https://doi.org/10.1007/s00231-021-03099-6