ArticlePDF Available

Measurement of electrical properties of refrigerants and refrigerant–oil mixtures

Authors:

Abstract and Figures

The paper deals with the description of a new pressure proof device developed at ILK Dresden for measuring electrical properties of refrigerants, oils and refrigerant–oil mixtures under pressure. The determination can be performed based on DIN EN 60247. This standard is valid for the determination of the relative permittivity, the dielectric dissipation factor and the direct current (DC) resistivity of isolating fluids at atmospheric pressure. The measurements can be made in a temperature range from −30 °C to 90 °C at pressures up to 80 bar under dry atmospheric conditions. The sensitivity of the method as well as its considerable flexibility meets the requirements of the industrial and commercial refrigeration. Challenges regarding the development and performance of the measuring cell as well as some preliminary experimental results are presented. The focus of the experiments is on environmentally friendly refrigerants (GWP < 150) such as R744, R1234yf and R152a, and their mixtures with lubricants.
Content may be subject to copyright.
Measurement of electrical properties of refrigerants and
refrigeranteoil mixtures
S. Feja*
ILK Dresden gGmbH, Bertolt-Brecht-Allee 20, Dresden 01309, Germany
article info
Article history:
Received 4 November 2011
Received in revised form
7 March 2012
Accepted 11 March 2012
Available online 21 March 2012
Keywords:
Air conditioning
Dielectric constant
Dielectric property
Electric resistance
R134a
R744
R152a
R1234yf
abstract
The paper deals with the description of a new pressure proof device developed at ILK
Dresden for measuring electrical properties of refrigerants, oils and refrigeranteoil
mixtures under pressure. The determination can be performed based on DIN EN 60247.
This standard is valid for the determination of the relative permittivity, the dielectric
dissipation factor and the direct current (DC) resistivity of isolating fluids at atmospheric
pressure. The measurements can be made in a temperature range from 30 Cto90Cat
pressures up to 80 bar under dry atmospheric conditions. The sensitivity of the method as
well as its considerable flexibility meets the requirements of the industrial and commercial
refrigeration. Challenges regarding the development and performance of the measuring
cell as well as some preliminary experimental results are presented. The focus of the
experiments is on environmentally friendly refrigerants (GWP <150) such as R744, R1234yf
and R152a, and their mixtures with lubricants.
ª2012 Elsevier Ltd and IIR. All rights reserved.
Mesures des proprie
´te
´se
´lectriques des frigorige
`nes et des
me
´langes de frigorige
`ne / huile
Mots cle
´s:Conditionnement d’air ; Constante die
´lectrique ; Proprie
´te
´die
´lectrique ; Re
´sistance e
´lectrique ; R134a ; R744 ; R152a ; R1234yf
1. Introduction
Due to the increasing applications of hermetic and semi-
hermetic compressors in refrigeration the question of the
electrical properties of the refrigeranteoil mixtures used is
becoming an important issue. The MAC-systems in electro
and hybrid vehicles, whose electrical systems will be designed
for voltages up to 500 V, are only one example for this interest.
The knowledge about the specific resistivity of the working
fluid mixtures and their application in electrical refrigeration
machines is becoming more and more important. Beyond that
the knowledge on the dielectric permittivity leads to
* Tel.: þ49 351 4081 767; fax: þ49 351 4081 755.
E-mail address: Steffen.Feja@ilkdresden.de.
www.iifiir.org
Available online at www.sciencedirect.com
journal homepage: www.elsevier.com/locate/ijrefrig
international journal of refrigeration 35 (2012) 1367e1371
0140-7007/$ esee front matter ª2012 Elsevier Ltd and IIR. All rights reserved.
doi:10.1016/j.ijrefrig.2012.03.011
fundamental statements about the behaviour of molecules in
an electrical field, which could be used for energetic optimi-
zation of air conditioning systems. Although the determina-
tion of the permittivity (dielectric constant, ε
x
) of oils has been
performed at the ILK Dresden since 1965, very little has been
published on this topic (e.g. Pa
¨tz et al., 1968). The analysis of the
dielectric constant and the DC resistivity of refrigerants and
refrigeranteoil mixtures in the relevant temperature interval
between 30 C and þ90 C and at pressures up to 100 bar is
quite challenging. Only a few research groups around the world
have been working on this subject (Barao et al., 1995,1996,1998;
Baustian et al., 1986;Bo
¨hmer and Loid, 1988;Fellows et al., 1991;
Hwang et al., 2008;Meurer et al., 2001;Ribeiro & Nieto de Castro,
2009;Tanaka et al., 1999) mostly using pure substances, but no
refrigeranteoil systems.
Actually, no measuring standards for the determination of
the permittivity and electrical resistivity of refrigeranteoil
systems are defined. Therefore, the investigations are per-
formed with a novel test setup, which is based on DIN EN
60247 (2005),ASTM D 924 (2008) and ASTM D 1169 (2011) set
for the determination of electrical properties of transformer
oils. The capacity and the resistivity of a cylinder gap appa-
ratus without protective ring have been measured directly
filled with air (10
2
mbar), calibrations substances and test
fluids in the gap. The permittivity and the specific resistivity of
the test fluids are calculated from these measurements
according DIN EN 60247 (2005).
2. Experimental methodology
With respect to the nature of refrigerants and refrigerant
mixtures the measurements require a pressure-tight cell,
which allows investigation in a homogeneous electrical field
necessitating homogeneous refrigeranteoil mixtures.
However, in addition to these requirements the enormous
sensitivity of high-resistance and permittivity measurements
are challenging. Especially the permittivity is very sensitive to
external influences (e.g. partial capacitances, impurities,
evolving pressure). Furthermore, the measurement setup has
to cover a high measurement range with respect to the pure
working fluids, i.e. oils and refrigerants. DC resistivities
ranging from 10
5
to 10
15
Um have to be determinable at
constant current. On the other hand, the examination of the
capacitance used to calculate the permittivity requires alter-
nating current.
Thus, the redesign of the measurement cell had to be
performed with respect to the required experimental param-
eters including:
- thermal control (30 Cto90C) of the test cell and both
electrodes
- pressure proof (up to 80 bar refrigerant pressure).
Fig. 1 shows the electrode setup of the test cell. The gap
between the two electrodes is 2 mm. The outer temperature
and pressure sensor (Kulite HKL/T 375 M) was screwed in the
visible NPT screwing in the outer electrode. Due to the high
voltage of 500 V required for the resistivity measurement as
well as the partial capacitance generated by the sensor this
part of the cell had to be reconstructed. Therefore, the pres-
sure sensor was fixed between the storage container and the
test cell and electrically decoupled from the outer electrode by
a pressure-tight synthetic hose.
The temperature of the outer electrode is defined by the
temperature of the surrounding thermostat bath. The test cell
is embedded in a silicon bath distinguished by a low dielectric
constant and an electrical conductivity below 10
12
Sm
1
.As
temperature sensor a Pt100 is inserted into the inner elec-
trode. A Precision Component Analyzer 6425 from Wayne Kerr
is used as the capacitance detection unit. Additionally a Ter-
raOhmmeter TO-3 from FISCHER ELEKTRONIK is utilized for
detection of the DC resistivity.
Furthermore a storage container which acts as a sample
reservoir for pre-conditioning of the refrigeranteoil mixtures
is connected to the test cell (Fig. 2).
The capacitance measurement is performed at 1 kHz AC
and 1 V. To control the values of the capacitance measure-
ment and to get further information on the dependence of the
dissipation factor from the properties of the liquid the dissi-
pation factor and the AC resistance is measured too. After the
AC measurement the cell is short-circuited for 1 min. After
this the electrodes are connected with the TerraOhmmeter.
After another minute the zero current is determined. This
zero current should be 1000 times less than the measuring
current to avoid an influence on the DC measurement. Next
the DC voltage is applied to the system. The DC resistance is
measured at 500 V given a load of 250 V/mm according to DIN
EN 60247 (2005). If the fluids exhibit a resistivity lower than
10
6
Um the voltage is set to 1 V instead of 500 V. This is done
because the current becomes too high and therefore is not
within the measurement range of the TerraOhmmeter used.
The voltage is set to 1 V so that the measurement range is as
wide as possible. 1 min after turning on the voltage the
resistance is measured and after a further minute the current
is measured to check the influence of the zero current.
The temperature range of the measurements is set above
the ambient temperature because of condensing water at the
electrode top surface. The resulting partial capacitances affect
Nomenclature
ε
x
dielectric constant, permittivity
Ttemperature (K)
wtemperature (C)
xconcentration (wt%)
C
a
idle capacity (empty cell) F
C
g
correction capacity F
C
e
electrode constant F
C
n
capacity with calibration liquid F
C
x
capacity with measuring liquid F
ε
n
dielectric constant calibration liquid
rspecific resistivity Um
Uvoltage V
Icurrent A
Kcell constant m
international journal of refrigeration 35 (2012) 1367e13711368
the determined permittivity of the sample. In the worst case,
the condensed film connects the inner and the outer electrode
which prevents a precise measurement of the electrical prop-
erties. Efforts to overcome this shortcoming are being made.
3. Experimental results
3.1. Calibration
According to DIN EN 60247 the test cell has to be calibrated at
room temperature in empty and liquid-filled state (calibration
substance). The idle capacity is marginally affected by
temperature in the range of 30 Cto90C. The capacity of the
empty cell without protective ring is divided into the parts
correction capacity (C
g
) and electrode constant (C
e
)(DIN EN
60247 (2005)) (Eq. (1)).
Ca¼CeþCg(1)
The terms C
g
and C
e
can be determined using the calibration
substance following Eqs. (1) and (2).
Ce¼CnCa
εn1(2)
Although the capacity of the cell filled with calibration
substance is temperature dependent, the terms C
e
and C
g
are
temperature independent. The permittivity ε
x
of an unknown
liquid is now determined using C
x
from the capacitance
measurement according to Eq. (3).
εx¼CxCg
Ce
(3)
For determining the specific DC resistivity the resistance of
the filled cell is determined at constant voltage. In DIN EN
60247 the specific DC resistivity is calculated according to
Eq. (4).
r¼KU
Iwith K¼0:113$capacity of the empty cell (4)
Using the idle capacity C
a
in this equation (Eq. (4)) is only
valid for cells constructed with a protective ring. After
comprehensive study using our cell, the value of the electrode
constant C
e
must be used as the capacity of the empty cell in
Eq. (4) for cells without a protective ring. Due to the wide range
of DC resistivities of insulating fluids from 10
5
to 10
15
Um this
misinterpretation of the DIN EN 60247 (2005) is not crucial
using the correct oil for hermetic compressors, but should be
considered comparing the results from different suppliers.
The test cell was calibrated after each cleaning process
with n-Heptane as calibration liquid at room temperature.
The cell was also calibrated with more polar fluids such as
Acetone and Fluorobenzene. These calibrations gave the same
results as the calibration with n-Heptane, but it was very time
Fig. 1 ea: Inner (left) and outer electrode (right). b: Assembled measurement cell.
Fig. 2 eBlock diagram of the test setup to determine electrical properties of refrigeranteoil mixtures.
international journal of refrigeration 35 (2012) 1367e1371 1369
consuming to remove the water content from the substances.
In fact the water content influences the measurement of the
dielectric constant and so a calibration with these fluids is too
complicated for daily measurements under normal laboratory
conditions.
3.2. Measurements of refrigerants, oils and
refrigeranteoil mixtures
First the pure refrigerants R134a, R1234yf, R152a and R744
were measured (Fig. 3). These refrigerants are the most
popular candidates for use in electro-mobile air conditioning
systems. The results of the permittivity measurement of
R134a were in agreement with the results given in Barao et al.
(1995),Meurer et al. (2001),Barao et al. (1996) and Fellows et al.
(1991). Also the value of the permittivity of R152a is compa-
rable to the results presented in Barao et al. (1998) and Fellows
et al. (1991) (Fig. 4). The permittivity of all four refrigerants
decreases with increasing temperature whereas the resistivity
doesn’t show a consistent temperature dependence. With
increasing temperature the resistivity decreases (R134a),
increases (R1234yf), or remains almost constant (R152a).
Comparing permittivity and resistivity values, R152a
exhibits the highest permittivity and the lowest resistivity in
comparison to the other refrigerants. The resistivity of R134a
and of R1234yf is nearly the same. The resistivity of liquid and
supercritical R744 is higher than 10
14
Um (data not shown).
The measurements were carried out at the saturation pres-
sure of the fluids.
After measuring the pure refrigerants, refrigeranteoil
mixtures were measured using at least one commercial oil
(Fig. 4). Interestingly, the permittivity of a mixture containing
nearly 75 wt% oil does not differ much from the permittivity of
the pure oil whereas the addition of 50 wt% oil to the refrig-
erant significantly decreases the permittivity compared to the
pure refrigerant sample. The same could be observed in case
of the resistivity measurements. No linear correlation has
been observed between the concentration and the electrical
properties of the pure fluids.
Before and after the measurements the water contents of
the oils were measured to check the influence of water on the
electrical properties.
4. Conclusion and outlook
A device to determine electrical properties of refrigeranteoil
mixtures under pressure has been developed. The test device
is based on the existing method of measuring the electrical
properties of isolating fluids under atmospheric pressure, as
described in the literature. The electrical properties direct
current resistivity and permittivity of refrigerants, oils and
refrigeranteoil mixtures were determined in a temperature
range of 20 Ce90 C. Further efforts are being made to design
Fig. 3 ePermittivity and resistivity of R744, R134a, R1234yf and R152a.
Fig. 4 ePermittivity and resistivity of R152a mixed with the POE oil ISO VG 80.
international journal of refrigeration 35 (2012) 1367e13711370
a measuring cell which allows the determination of electrical
properties of refrigeranteoil mixtures below ambient
temperature. Apart from that, the influence of the water
content and the impurities of oil and-/or refrigerant on the
electrical properties (possibly monitored by sensors) will be
subject of further studies.
Acknowledgments
This work was supported by the grant of the Bundesministe-
rium fu
¨r Wirtschaft und Technologie “FuE-Fo
¨rderung
gemeinnu
¨tziger externer Industrieforschungseinrichtungen
in Ostdeutschland eInnovationskompetenz (INNO-KOM-
Ost)” Modul Vorlaufforschung VF090028. The author wishes to
thank Jan Hegewald (Hegewald & Peschke, Mebund Pru
¨f-
technik GmbH, Nossen) for establishing and testing the
apparatus and Steven Rhode (TU Dresden) for his help with
the measurements. Special thanks go to Sven Heinrich (H. -P.
FISCHER ELEKTRONIK GmbH & Co.) for supporting us with the
development of the measuring cell.
references
ASTM D 924, 2008. Standard Test Method for Dissipation Factor
(Or Power Factor) and Relative Permittivity (Dielectric
Constant) of Electrical Insulating Liquids. ASTM International.
ASTM D 1169, 2011. Standard Test Method for Specific Resistance
(Resistivity) of Electrical Insulating Liquids. ASTM
International.
Barao, T., Nieta de Castro, C.A., Mardolcar, U.V., Okambawa, R.,
St-Arnaud, J.M., 1995. Dieelectric constant, dielectric virial
coefficient and dipole moments of 1,1,1,2-Tetrafluorethane. J.
Chem. Eng. Data 40, 1242e1248.
Barao, M.T., Nieto de Castro, C.A., Mardolcar, U.V., 1996. The
dielectric constant of liquid HFC 134a and HCFC 142b. Int. J.
Thermophys. 17, 573.
Barao, M.T., Mardolcar, U.V., Nieto de Castro, C.A., 1998. Dielectric
constant and dipole moments of 1,1,1-Trifluoro-2,2-
Dichloroethane (HCFC 123) and 1,1-Difluoroethane (HFC 152a)
in the liquid phase. Fluid Phase Equil. 1753, 150e151.
Baustian, J.J., Pate, M.B., Bergles, A.E., 1986. Properties of oil-
refrigerant liquid mixtures with applications to oil
concentration measurement: part II-electrical and optical
properties. ASHRAE Trans. 92 (Pt.1), 74e92.
Bo
¨hmer, R., Loid, A., 1988. Dielectric properties of condensed
fluoromethanes and fluoromethane mixtures. J. Chem. Phys.
89 (8), 4981e4986.
DIN EN 60247, 2005. Isolierflu
¨ssigkeiten eMessung der
Permittivita
¨tszahl, des dielektrischen Verlustfaktors (tan d) und
des spezifischen Gleichstrom-Widerstandes. DIN EN. http://
www.beuth.de/cn/J-650DE375B16CD477738B952469BEEDA9.2/
d29ya2Zsb3duYW1lPWV4YUJhc2ljU2VhcmNoJnJlZj10cGwta
G9tZSZsYW5ndWFnZWlkPWRl.html.
Fellows, B.R., Richard, R.G., Shankland, I.R., 1991. Electrical
characterization of alternate refrigerants. In: Actes Congr. Int.
Froid, 18th Seint-Hyacinthe, Que, vol. 2, pp. 398e402.
Hwang, Y., Radermacher, R., Hirata, T., 2008. Oil mass fraction
measurement of CO
2
/PAG mixture. Int. J. Refrigeration 31,
256e261.
Meurer, C., Pietsch, G., Haacke, M., 2001. Electrical properties
of CFC- and HCFC-substitutes. Int. J. Refrigeration 24,
171e175.
Pa
¨tz, G., Ha
¨ntzschel, H., Neubert, J., 1968. Messung elektrischer
Eigenschaften von Ka
¨ltemaschineno
¨len. Fachbericht Nr. 97/
68. ILK Dresden.
Ribeiro, A.P.C., Nieto de Castro, C.A., 2009. Dielectric properties of
liquid refrigerants: facts and trends. In: IIR 3rd Conference on
Thermophysical Properties and Transfer Processes of
Refrigeration, Boulder, CO, paper No 108.
Tanaka, Y., Matsuo, S., Sotani, T., Kondo, T., Matsuo, T., 1999.
Relative permittivity and resistivity of liquid HFC
refrigerants under high pressure. Int. J. Thermophys. 20 (1),
107e117.
international journal of refrigeration 35 (2012) 1367e1371 1371
... Similar to Meurer et al. [2], the cell by Dschung and Kindersberger [26] measures a resistivity value for R134a which is two orders of magnitude lower than that measured by Feja S. (2012). The factors causing this may similarly be attributed to the use of a parallel plate cell with a higher cell constant. ...
... Feja [28] tested the DC resistivity using a field strength of 250 kV/m. He did not use a guard ring and instead calibrated the test cell with a reference liquid in advance. ...
... An analysis of resistivity cell designs has been presented including a description of considerations that need to be addressed when attempting to develop a resistivity cell for insulating liquids, particularly for HFCs Fig. 10. Resistivity results for R152a, R134a and R1234yf plotted as a function of temperature [28]. used in pharmaceutical metered dose inhalers and industrial refrigerants. ...
Article
Full-text available
The expansion of applications involving hydrofluorocarbons has generated a demand for devices capable of measuring the electrical volume resistivity of such liquids across diverse operating conditions. The narrow operating range of commercial offerings, particularly in regard to pressure, compels researchers to develop custom cells for the desired test conditions. A review of resistivity cell designs developed over the past three decades is presented. Academic studies in the past have focussed on the development of cells for the purpose of testing the resistivity of refrigerants in liquid phase under high pressures. The fundamental principles underlying resistivity measurement are discussed while emphasis is placed on practical aspects of cell design. The review addresses facets including contemporary standards, limitations and constructional details of academic and commercial cells. It should serve as a guide for future researchers attempting to develop custom resistivity cells for dielectric liquids.
... Values concerning the DC resistivity of R134a and R152a were first published by Fellows et al. 8 and later by Feja 9 . Fellows tested the resistivities using both AC and DC voltages and measured the DC resistivity for R134a and R152a to be 6.6 × 10 8 Ωm and 2.2 × 10 7 Ωm, respectively. ...
... Fellows tested the resistivities using both AC and DC voltages and measured the DC resistivity for R134a and R152a to be 6.6 × 10 8 Ωm and 2.2 × 10 7 Ωm, respectively. Feja 9 tested several electrical properties, including the relative permittivity, dielectric dissipation factor, and DC resistivity, across a temperature range between − 30 and 90 °C, and tested mixtures with different concentrations of polyester oil. They found the DC resistivity of R134a and R152a to be 10 8 Ωm and 10 7 Ωm, respectively. ...
Article
Full-text available
Metered-dose inhalers employ propellants to produce pharmaceutical aerosols for treating respiratory conditions like asthma. In the liquid phase, the DC volume resistivity of pharmaceutical propellants, including R134a, R152a, and R227ea, was studied at saturation pressures and room temperature (not vapour phase). These measurements are essential for industries like refrigerants. Aerosols from metered dose inhalers (MDIs) with these propellants become electrically charged, affecting medicament deposition in lung. The resistivity was measured using a novel concentric cylinder-type capacitance cell designed in-house. The resistivity for the propellants (R134a, R152a, and R227ea) was found to be 3.02 × 1010 Ωm, 2.37 × 109 Ωm and 1.31 × 1010 Ωm, respectively. The electrical resistivity data obtained was found to be at least two orders of magnitude higher than the limited data available in the literature. Challenges in the resistivity cell’s development and performance are discussed, with a focus on various propellants and their mixtures with ethanol and moisture concentrations. The resistivity of propellant mixtures containing moisture concentrations ranging from 5 to 500 ppm and ethanol concentrations ranging between 1000 and 125,000 ppm was determined. The resistivity was tested across 10-min and 1-h periods and was performed in accordance with the contemporary IEC 60247 standard.
... where M is the molecular weight, g/mol; P, P cr are the saturation and critical pressures respectively, Pa; Q is the heat flow, W; F A is the heat transfer surface, m 2 . The HTC, calculated for the different dielectric working fluids [11,28] at 60°C by means of Cooper's correlations are represented in Table 1 for the Intel Core i9-12900K CPU design. ...
Chapter
Two-phase immersion cooling technology is a promising and perspective thermal control solution for the data centre aiming to substantially improve its power usage effectiveness (PUE). In the paper, the theoretical and practical questions are considered to deal with the use of immersion solutions. It was clearly shown that the use of two-phase immersion technology for the cooling of a single CPU is not an effective solution as compared to conventional methods with, for instance, phase change materials in the thermal interface. At the same time, the effectiveness of technology has been proved for the powerful dense packing of circuit boards. A simple correlation for the determination of the minimal distance between circuit boards in packing has been proposed. It has been shown based on a demonstration experiment, that a two-phase thermosiphon immersion solution with HFE7000 fluid provides the efficient cooling of a 60 kW dense pack of circuit boards with PUE < 1.01.
... where M is the molecular weight, g/mol; P, P cr are the saturation and critical pressures respectively, Pa; Q is the heat flow, W; F A is the heat transfer surface, m 2 . The HTC, calculated for the different dielectric working fluids [11,28] at 60°C by means of Cooper's correlations are represented in Table 1 for the Intel Core i9-12900K CPU design. ...
Chapter
Energy saving in every process of human activity is a strong trend aiming to reduce carbon dioxide emissions from fossil energy sources. Residential natural gas consumption for space and water heating is still substantial and must be reduced. The wide use of a ground-source heat pump (GSHP) could mitigate the impact of households on climate change. In the paper, the concept of a ground-source two-phase thermosiphon with pump assistance is proposed. Using a pump to lift working fluid from the bottom of the thermosiphon to the upper zone allows its exploitation as a heat sink for the heat pump or as a separate cold source. It has been shown that using a pump assistant two-phase thermosiphon in GSHP could reduce the total power consumption for space heating and conditioning by at least 12%. The experimental study has justified the efficiency of the pump assistant thermosiphon in transferring the heat top-down.Keywordsground-sourceheat pumpthermosiphontwo-phasehouseholds
... This charge separation is caused by the electronegativity of the atoms within [259], the HCFO R1233zd(E) is less polar with a polarity of 3.81 · 10 −30 C m [260]. Comparing this value with the electric dipole moment of typical POE lubricants, which are in the range of 3 -4·10 −30 C m [261,262], it can be seen that the polarity of R1233zd(E) is closer to the one of POE lubricants. From this, a higher solubility and also a higher boiling point elevation can be concluded. ...
Thesis
Full-text available
The Organic Rankine Cycle (ORC) can be applied to generate power from low-temperature heat sources and thus supports a sustainable energy system. In order to make this technology more competitive, this thesis contributes to their development, particularly for geothermal applications. To this end, environmentally friendly working fluids and new plant architectures are being investigated. Recently, a new generation of working fluids with significantly lower Global Warming Potential (GWP) has been developed. However, operating experience with this novel fluids is rare, especially concerning existing systems designed for older generation fluids. Therefore, the applicability of two modern fluids as drop-in replacements for the currently widespread fluid R245fa is experimentally investigated. It can be concluded that both novel fluids R1233zd(E) and R1224yd(Z) are generally suitable as a drop-in replacement for R245fa in ORC systems. The highest thermal efficiency is reached with R1233zd(E), while the highest power output is still obtained with the high-GWP fluid R245fa. The concept of regenerative preheating is investigated in literature by numerical studies and its thermodynamic and economic performance is predominantly evaluated positively. However, regenerative preheating has not yet been realized in experimental ORC test rigs or commercial products. For this purpose, a novel ORC test rig is designed, constructed and commissioned in the course of this thesis. For evaluation purposes, the regenerative preheating concept is compared to a standard ORC configuration. As a result, a 9.9% higher net thermal efficiency is achieved with regenerative preheating, while the net power output is equal to the one achieved with the standard configuration. This result is particularly important for combined heat and power (CHP) generation due to the reduced cooling of the heat source. In order to evaluate this concept for CHP applications, a novel ORC-CHP architecture based on regenerative preheating is experimentally compared to three state of the art ORC-CHP concepts. Moreover, three different supply and return temperatures of the district heating system (DHS) are considered. The results reveal that the novel architecture, in combination with low- and medium-temperature DHS, leads to an increased part-load performance and a wider operating range. This enables an up to 9.4% higher annual net electricity production, which accounts for additional revenues of 4.56 million e in the case of a typical geothermal project. Thus, it can be concluded that this novel ORC-CHP architecture is beneficial from a technical perspective and promising in terms of economics.
Article
This paper presents the identification of slug/stratified-wavy, stratified-wavy and annular regimes for horizontal flow (in the range of mass fluxes 40 – 150 kg m⁻² s⁻¹), and slug, churn, and annular flow regimes for vertical upward flow (in the range 65 – 115 kg m⁻² s⁻¹) for R134a flow through 7 mm ID tube. Flow regimes are characterized based on time plot of normalized capacitive signals, kernel density estimation (KDE), power spectral density (PSD), and visualization results from a high-speed camera. Sensors with different axial lengths (D, 2D/3, and D/2) are also tested to study the adequacy of shorter sensors for the characterization of flow regimes. Results show that all three sensors have a similar capability of characterizing flow regimes, justifying the use of the shorter sensors in many applications with limited space.
Article
Full-text available
In this paper we analyse the situation for the dielectric properties of the refrigerants, from the experimental and theoretical point of view, based on more than one decade of research of our group. Examples of the predictive power of simple models will illustrate the existing tools for electrical permittivity and dipole moment prediction and correlation. The relation of Báron and Buep was analysed and extended to include the effects of pressure variation. Analogies between the Vedam equation and rough hard-sphere theory of transport properties were encountered and discussed.
Article
Electrical properties of refrigerants are of importance as soon as bushings are surrounded by a refrigerant. This is the case e. g. for hermetic sealed motor compressors as well as for some control devices such as liquid level control units or capacity controls for compressors. This paper presents a survey of existing data for HFC refrigerants and presents new measurements for those HFC blends that have been identified as long term replacements for CFCs and HCFCs. The data collection includes permittivity, electrical conductivity and breakdown voltage. Values are given for the HFC blends R404A, R407C, R410A and R507 as well as for R134a.RésuméIl est important de prendre en compte les propriétés électriques des frigorigènes lorsque les composants métalliques sont entourés d'un frigorigène. On rencontre cette situation dans le cas des compresseurs hermétiques et des appareils de commande tels que les appareils utilisés pour réguler le niveau du liquide ou, dans le cas des compresseurs, les systèmes de réglage de la puissance. Cette communication présente une enquête des données sur les frigorigènes HFC ainsi que de nouvelles mesures effectuées sur les mélanges de HFC destinés à remplacer les CFC et les HCFC dans le long terme. Les données présentées comprennent : la constante diélectrique, la conductivité électrique et la tension de claquage.
Article
This paper presents measurements of the dielectric constant of HFC 134a and HCFC 142b, as a function of pressure and temperature, in the temperature range from 200 to 300 K and pressures up to 20 MPa, using a direct capacitance method. The samples used had a stated purity of 99.8 and 99.9%, respectively. The values of the dielectric constant have a precision of 0.01% and an accuracy of 0.1%. The data obtained were correlated as a function of density and pressure. The theory developed by Vedam et al., based on the Eulerian strain, and the Kirkwood equation for the variation of modified molar polarization with temperature and density were applied to analyze the data and to obtain the dipole moment of both refrigerants in the liquid state.
Article
Dielectric measurements were performed on liquid and solid (CF4)1−x (CMF3)x with M=H, Cl, and Br. The dielectric behavior of the polar molecules in the liquid state is well described by an Onsager equation. At the melting point, pure hydrogenated and brominated fluoromethanes condense into dipolar rigid phases, while pure tetrafluoromethane forms a plastic crystal. CClF3 exhibits dipolar relaxational phenomena in the solid state. The data indicate that near the melting point this compound is close to a transition into a plastic phase. Mixtures of CF4 with CHF3 and CBrF3 exhibit monotectic phase diagrams with a limited solubility in the liquid state and complete immiscibility in the solid state. However, formation of mixed crystals is found in (CF4)1−x (CClF3)x which exhibits a eutectic phase diagram.
Article
The static relative permittivity (dielectric constant) and the resistivity of HFC-236ea (CF3–CHF–CHF2) and HFC-245fa (CF3–CH2–CHF2) in the liquid phase were studied at temperatures from 293 to 343 K and pressures from 0.1 to 50 MPa. The relative permittivity was measured by a concentric-cylinder-type capacitance cell with an LCR meter with an uncertainty of less than 0.1%. The resistivity was measured by a high resistance meter using plane-parallel platinum electrodes installed in a borosilicate glass syringe. It was found that the relative permittivities and the resistivities of liquid HFC-236ea and HFC-245fa at 303 K and 0.101325 MPa are about 5.13 and 6.54 and 1.5×1010 and 0.2×1010 O·cm, respectively. The relative permittivity and the resistivity increase monotonically with increasing pressure and decreasing temperature.
Article
In this study, a method of using a capacitance sensor was investigated as a means to measure the mass fraction of a type of PAG oil flowing with CO2 in a transcritical cycle. The test facility equipped with the capacitance sensor was fabricated to establish and maintain a known oil mass fraction and to measure the capacitance of the CO2/oil mixture. By using this facility, the relationship among three parameters (reduced CO2 density (CO2 density divided by the critical density of CO2), oil mass fraction, and relative dielectric constant of the CO2/PAG oil mixture) was developed. For the range of oil mass fraction 0–0.07, the error of new measurement method was within 0.005 for a wide range of pressures and temperatures tested. This study established the method of measuring the oil mass fraction continuously in the transcritical CO2 cycle without affecting the cycle performance. Through this method, the effect of oil mass fraction on the characteristics of the oil circulation behavior and the performance of the transcritical CO2 cycle can be investigated.
Article
In this paper the authors report measurements of the dielectric constant of 1,1,1,2-tetrafluoroethane, HFC-134a, an environmentally acceptable refrigerant, under consideration as an alternative replacement of the chlorofluorocarbons, CFCs. The dipole moment in the gaseous phase was found to be (1.91 {+-} 0.19) D, and in the liquid phase (3.54 {+-} 0.01) D. The authors present values of the first three dielectric virial coefficients in the gaseous phase.
Article
Experimental data of the dielectric constant of HCFC 123 and HFC 152a as a function of pressure and temperature in the temperature range from 200 to 300 K and pressures up to 18 MPa were correlated as a function of pressure and temperature, with an uncertainty of ±0.01 for HCFC 123 and ±0.12 for the HFC 152a, and as a function of density and temperature with an uncertainty of ±0.005 for HCFC 123 and ±0.034 for HFC 152a. The uncertainty of the results obtained for the dielectric constant was estimated at a 95% confidence level to be ±7.27×10−3 for HCFC 123 and ±3.26×10−2 for HFC 152a. The theory developed by Vedam and Chen [K. Vedam, C. Chen, Importance of using eulerian representation of strain in high pressure studies on liquids, J. Chem. Phys., Vol. 77, 1982, pp. 1461–1463] and adapted by Diguet [R. Diguet, Density dependence of refractive index and static dielectric constant, Physica, 139 and 140B, 1986, pp. 126–130] and the Kirkwood modification of the Onsager equation for the variation of the modified molar polarization with temperature and density were applied to analyse the data and to obtain the dipole moment of both refrigerants in the liquid state. These were found to be 2.13 D for HCFC 123 and 3.69 D for HFC 152a.
Oil mass fraction measurement of CO 2 /PAG mixture Electrical properties of CFC-and HCFC-substitutes
  • Froid
  • Que Seint-Hyacinthe
  • Y Hwang
  • R Radermacher
  • T Hirata
Froid, 18th Seint-Hyacinthe, Que, vol. 2, pp. 398e402. Hwang, Y., Radermacher, R., Hirata, T., 2008. Oil mass fraction measurement of CO 2 /PAG mixture. Int. J. Refrigeration 31, 256e261. Meurer, C., Pietsch, G., Haacke, M., 2001. Electrical properties of CFC-and HCFC-substitutes. Int. J. Refrigeration 24, 171e175. Pä tz, G., Hä ntzschel, H., Neubert, J., 1968. Messung elektrischer Eigenschaften von Kä ltemaschinenö len. Fachbericht Nr. 97/ 68. ILK Dresden.
Electrical characterization of alternate refrigerants
  • B R Fellows
  • R G Richard
  • I R Shankland
Fellows, B.R., Richard, R.G., Shankland, I.R., 1991. Electrical characterization of alternate refrigerants. In: Actes Congr. Int. Froid, 18th Seint-Hyacinthe, Que, vol. 2, pp. 398e402.