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Efficiency comparison of subcritical OTEC power cycle using various working fluids

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Abstract

This paper presents an investigation into the thermal efficiency and main component size of the subcritical ocean thermal energy conversion (OTEC) power cycle using various working fluids under different operation conditions. The analysis procedure was performed with a simulation program written in Engineering Equation Solver. With the given analysis conditions, efficiencies of three types of working fluids were evaluated and compared. It was found that the thermal efficiencies of the subcritical OTEC power cycle depend strongly on the evaporating and condensing temperature, and turbine efficiency, while not roughly depending on superheating degrees and pump efficiencies. With a thorough grasp of these results, an efficient OTEC power cycle can be designed. R717 and R404A yielded the highest and lowest thermal efficiencies among the wet fluids, and R22 showed the largest efficiency among the dry fluids. For the iso-entropic fluids, R245fa provided the highest thermal efficiency. In comparison of main component sizes, R404A and R744 had the largest and smallest condenser size, respectively. Also, R744 exhibited the smallest evaporator size, and R404A and R227ea show the largest size. And R744 and R245fa gave the largest and smallest pump size, respectively. From the results of thermal efficiency and main components for various working fluids in the OTEC power cycle, R717 in the subcritical OTEC power cycle is the preferred working fluid, except for its toxicity and flammability.

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Abbreviations

A:

Average (–)

cp :

Specific heat at constant pressure [J/(kg K)]

h:

Specific enthalpy (kJ/kg)

\(\Delta {\text{H}}({\text{T}}_{{{\text{t}},{\text{in}}}} )\) :

Specific enthalpy difference related to Eq. (1)

\({\text{Ja(T}}_{\text{t,in}} )\) :

Jakob number defined as \({{{\text{c}}_{\text{p}} {\text{T}}_{\text{t,in}} } \mathord{\left/ {\vphantom {{{\text{c}}_{\text{p}} {\text{T}}_{\text{t,in}} } {{\text{h}}_{\text{lv}} ( {\text{T}}_{\text{t,in}} )}}} \right. \kern-0pt} {{\text{h}}_{\text{lv}} ( {\text{T}}_{\text{t,in}} )}}\)

L:

Liquid (–)

m:

Mass flow rate (kg/s)

M:

Molecular weight (g/mol)

OTEC:

Ocean thermal energy conversion (–)

P:

Pressure (kPa, MPa)

Q:

Heat capacity (kW)

T:

Temperature (°C, K)

V:

Vapor (–)

VER:

Vapor expansion ratio (–)

W:

Power, work (kW)

\(\upeta\) :

Efficiency (–)

\(\Delta\) :

Difference (–)

\(\Delta\)h:

Latent heat (kJ/kg)

bp:

Normal boiling point

c:

Condenser, condensing

car:

Carnot

crit:

Critical

ds:

Deep seawater

e:

Evaporator, evaporating

in:

Inlet

lv:

Related to latent heat of evaporation

OTEC:

Ocean thermal energy conversion

p:

Pump

re:

Refrigerant

ss:

Surface seawater

suc:

Subcooling degree

suh:

Superheating degree

t:

Turbine

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Acknowledgments

This work was financially supported by the National R&D project of the “Development of Energy utilization technology with Deep Ocean Water” supported by the Korean Ministry of Land, Transport and Maritime Affairs.

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Correspondence to Chang-Hyo Son.

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Yoon, JI., Son, CH., Baek, SM. et al. Efficiency comparison of subcritical OTEC power cycle using various working fluids. Heat Mass Transfer 50, 985–996 (2014). https://doi.org/10.1007/s00231-014-1310-8

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  • DOI: https://doi.org/10.1007/s00231-014-1310-8

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