Published February 2018 | Version v1
Journal article

Performance analysis of an evaporation process of plate heat exchangers installed in a Kalina power plant

  • 1. EnBW Energie Baden-Württemberg AG, Karlsruhe (Germany)
  • 2. Karlsruher Institut für Technologie (Germany)

Description

Highlights: • Evaporation process of NH3-H2O mixture with plate heat exchangers of existing Kalina cycle is analyzed. • Three main key parameters are introduced: pressure drops, vapor fraction and heat transmission capacity. • Trend of parameters over a period from 2012 until 2017 are analyzed. • Operation data points are published to the scientific community. In geothermal power generation, ammonia-water (NH3H2O) mixtures are considered as working fluids in order to improve efficiency from low enthalpy heat sources. During the evaporation process, the NH3H2O working pair as zeotropic working fluid has the advantage to evaporate not isothermal temperature but over a temperature glide to adapt better to the heat source temperature profile. By today, there is a lack of performance data from operational generation units available in literature that can be used for scientific works based on computational calculations to compare with. In this paper the data logs from the evaporation process of the geothermal power plant are analyzed in order to review the evaporator's performance. Data had been gathered for a period of 5 years and three key performance parameters were defined: pressure drop, vapor fraction and heat transmission capacity. The main parameters that influence the performance are the temperatures, pressures and flow rates. It turned out, that the NH3 mass fraction plays only a minor role within the evaporation process.

Availability note (English)

Available from http://dx.doi.org/10.1016/j.energy.2017.12.105

Additional details

Identifiers

DOI
10.1016/j.energy.2017.12.105;
PII
S0360544217321485;

Publishing Information

Journal Title
Energy (Oxford)
Journal Volume
145
Journal Page Range
p. 105-115
ISSN
0360-5442
CODEN
ENEYDS

Optional Information

Copyright
Copyright (c) 2017 Elsevier Ltd. All rights reserved.