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Performance of multiple mini-tube heat exchangers as an internal heat exchanger of a vapor-injection cycle heat pump

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Abstract

A multiple mini-tube (MMT) heat exchanger was considered as an internal heat exchanger of vapor-injection cycle heat pump. Heat transfer and pressure drop in multiple mini-tube heat exchangers were numerically and experimentally investigated. Results show that the best performance of the MMT heat exchanger can be obtained when the intermediate-pressure two-phase refrigerant is supplied to the shell-side and this refrigerant reaches a saturated vapor state at the exit of the heat exchanger.

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Abbreviations

A :

Area (m2)

Bo :

Boiling number

C :

Specific heat (J/kg K)

D :

Diameter (m)

f :

Friction factor

G :

Mass flux (kg/m2 s)

h :

Heat transfer coefficient (W/m2 K)

i :

Specific enthalpy (kJ/kg)

k :

Thermal conductivity (W/m K)

L :

Length (m)

\(\dot{m}\) :

Mass flow rate (kg/s)

Pr :

Prandtl number

Re :

Reynolds number

T :

Temperature (K)

U :

Overall heat transfer coefficient (W/m2 K)

x :

Vapor quality

ε :

Wall roughness (mm)

ρ :

Density (kg/m)

\(\phi^{2}\) :

Frictional two-phase multiplier

μ :

Viscosity (Pa s)

a :

Actual

s :

Shell-side

sp :

Single-phase

t :

Tube-side

tp :

Two-phase

v :

Vapor

l :

Liquid

hp :

High-pressure- side

int :

Intermediate-pressure-side

in :

Inlet

max :

Maximum

out :

Outlet

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Acknowledgments

This work was supported by the Human Resources Development program (No. 20124010203230) of the Korea Institute of Energy Technology Evaluation and Planning (KETEP) Grant funded by the Korea government Ministry of Trade, Industry and Energy and Basic Science Research Program through the National Research Foundation of Korea (NRF) funded by the Ministry of Education, Science and Technology (NRF-2012R1A1A2007320).

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Correspondence to Ji Hwan Jeong.

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Jang, J.Y., Jeong, J.H. Performance of multiple mini-tube heat exchangers as an internal heat exchanger of a vapor-injection cycle heat pump. Heat Mass Transfer 52, 741–752 (2016). https://doi.org/10.1007/s00231-015-1592-5

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  • DOI: https://doi.org/10.1007/s00231-015-1592-5

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