Vehicle thermal Management Systems Conference and Exhibition (VTMS10) -  IMechE

Vehicle thermal Management Systems Conference and Exhibition (VTMS10) (eBook)

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2011 | 1. Auflage
676 Seiten
Elsevier Science (Verlag)
978-0-85709-505-3 (ISBN)
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This book contains the papers presented at the IMechE and SAE International, Vehicle Thermal Management Systems Conference (VTMS10), held at the Heritage Motor Centre, Gaydon, Warwickshire, 15-19th May 2011. VTMS10 is an international conference organised by the Automobile Division and the Combustion Engines and Fuels Group of the IMechE and SAE International. The event is aimed at anyone involved with vehicle heat transfer, members of the OEM, tier one suppliers, component and software suppliers, consultants, and academics interested in all areas of thermal energy management in vehicles. This vibrant conference, the tenth VTMS, addresses the latest analytical and development tools and techniques, with sessions on: alternative powertrain, emissions, engines, heat exchange/manufacture, heating, A/C, comfort, underhood, and external/internal component flows. It covers the latest in research and technological advances in the field of heat transfer, energy management, comfort and the efficient management of all thermal systems within the vehicle. - Aimed at anyone working in or involved with vehicle heat transfer - Covers research and technological advances in heat transfer, energy management, comfort and efficient management of thermal systems within the vehicle

The Institution of Mechanical Engineers (IMechE) is one of the leading professional engineering institutions in the world.
This book contains the papers presented at the IMechE and SAE International, Vehicle Thermal Management Systems Conference (VTMS10), held at the Heritage Motor Centre, Gaydon, Warwickshire, 15-19th May 2011. VTMS10 is an international conference organised by the Automobile Division and the Combustion Engines and Fuels Group of the IMechE and SAE International. The event is aimed at anyone involved with vehicle heat transfer, members of the OEM, tier one suppliers, component and software suppliers, consultants, and academics interested in all areas of thermal energy management in vehicles. This vibrant conference, the tenth VTMS, addresses the latest analytical and development tools and techniques, with sessions on: alternative powertrain, emissions, engines, heat exchange/manufacture, heating, A/C, comfort, underhood, and external/internal component flows. It covers the latest in research and technological advances in the field of heat transfer, energy management, comfort and the efficient management of all thermal systems within the vehicle. - Aimed at anyone working in or involved with vehicle heat transfer- Covers research and technological advances in heat transfer, energy management, comfort and efficient management of thermal systems within the vehicle

A practical approach to R-1234yf thermophysical property calculation and A/C system cycle analysis


M.R. Jones,     MIRA Ltd, UK

ABSTRACT


The new refrigerant R-1234yf is on the verge of widespread acceptance as the preferred alternative fluid for use in automotive air conditioning systems. In view of this, much work has recently been conducted in the fundamental thermophysical analysis of the refrigerant, as well as in its practical application in automotive air conditioning systems.Much of the property analysis work published to date has been directed at establishing accurate coefficients for use in well-known relationships such as the Martin Hou and Peng-Robinson equations of state. This enables the computation of a range of useful properties based on, for example, temperature and pressure conditions, and aids refrigerant cycle analysis and simulation. However, these equations of state and their corollaries can be complex, and generally require the use of iterative numerical techniques in their solution. Various proprietary tools are available to enable these computations, but they are not generally applied in the domain of the practicing automotive climate control engineer.This paper draws together much of the published thermophysical data relating to R-1234yf and reduces it to a set of discrete equations, presented with coefficients, which enable direct calculation of all relevant properties. This facilitates relatively easy analysis of A/C cycles within a spreadsheet environment, as demonstrated in the paper by application to a system incorporating an internal heat exchanger.

1 INTRODUCTION


R-1234yf is confirmed as the preferred replacement automotive refrigerant in all markets where R134a is now unacceptable on the grounds of environmental impact. All vehicle manufacturers selling new models into the European market from 2011 onwards have to comply with the Global Warming Potential (GWP) upper limit of 150 laid down in the legislation (1); R-1234yf achieves this comfortably, with a published GWP value of 4 (2).

However, although the GWP of R-1234yf is clearly acceptable, other thermodynamic properties of the fluid are inferior as compared with R134a. Most notably, enthalpy of vaporisation at typical evaporating pressures is around 18% lower for R-1234yf as compared with R134a, although this is offset to some extent by the higher gas densities of R-1234yf (3). In view of these differences, the automotive community has been, and continues to be, active in A/C system performance development using the new fluid.

This paper will briefly discuss some of the measures which are being adopted in order to claw back the potential performance degradation relating to the new fluid, but the main objective of the paper is to present a set of thermodynamic property relationships which enable the practicing engineer to analyse the R-1234yf A/C loop. Whilst evaporator air-side observations and calculations are useful in assessing the ultimate performance of the new refrigerant, detailed analysis of the refrigerant loop is also essential in the development of any new system. Vehicle development engineers conducting whole-vehicle refrigerant charge determination tests, typically in the Climatic Wind Tunnel (CWT), need to be able to calculate condenser subcool and evaporator superheat accurately. Similarly, laboratory-based A/C studies, which generally seek to develop a more fundamental understanding of the refrigerant cycle, also need accurate saturation data, as well as comprehensive refrigerant enthalpy information. Some of the data required has been published recently, with discrete laboratory-based measurements of refrigerant properties and extended tables of data derived from complex equations of state (4, 5, 6, 7). However, the data presented is not sufficiently detailed for use in analysis of A/C cycles, and the mathematical relationships and coefficients given generally require the use of relatively complex iterative numerical solutions.

This paper gathers together property data which has been published for R-1234yf, and condenses the information into a set of highly useable curve fits which can be implemented by the practicing automotive engineer in everyday simulation and analysis environments. The logarithmic and 2D and 3D polynomial relationships presented enable direct calculation of refrigerant saturation properties and enthalpy over the normal operating range of the fluid in an automotive A/C system, and generally recover properties to an accuracy of within 0.2% as compared with the published data.

2 DEVELOPMENT OF THERMOPHYSICAL RELATIONSHIPS


The relationships developed here are generally of relatively simple polynomial form, and they are presented along with their respective coefficients. As some of the relationships extend to sixth order terms care needs to be taken with respect to the accuracy of coefficients used; these are quoted to 12 significant figures where appropriate, which was found to give acceptable accuracy and stability.

2.1 Vapour pressure relationship


Leck (7) presents a vapour pressure relationship derived from the Martin-Hou equation of state as follows (Note − pressure, P in kPa and temperature T in K in Eq1a only):

(1a from Leck)

Calculation of the saturation curve using this equation and fitting the resulting data by means of a 3rd order logarithmic polynomial leads to the following relationship which enables calculation of saturation temperature based on absolute pressure:

(1b)

where t is saturation temperature in C, P is absolute pressure in bar and c0-3 are the polynomial coefficients, which are given for all relationships in Table 1.

Table 1

Coefficients for use in equations 1-4

A plot of the ‘raw’ R-1234yf data, R-1234yf data recovered from the log fit, and the R134a curve is shown in Fig 1. It can be seen that the log fit recovers saturation temperature to an accuracy of within around 0.05C across the entire range, and is typically within 0.02C, which is more than adequate for automotive A/C system analysis.

Fig 1 R-1234yf & R134a saturation temperature vs pressure plot

2.2 Saturation enthalpy relationships


Saturated liquid and vapour enthalpy data has been made available in separate publications by Leck and Akasaka up to the critical point of 94.7C, 33.8bar (7, 4); data presented in the publications correlate well within the normal saturation range of interest in automotive applications (ie around -10C to 90C). The data reported by Akasaka has been used to derive relationships for the saturated liquid and vapour enthalpies as a function of temperature, and taking the arithmetic difference in the two values leads directly to the enthalpy of vapourisation.

The following 6th order 2D polynomial was found to represent each of the saturated enthalpies within an acceptable level of accuracy up to a temperature of 90C (ie. within around 0.1% at worst):

(2a(liq), 2b(vap))

where hsat can be either saturated liquid or vapour enthalpy in kJ/kgK, t is temperature in C, and c0-6 are the coefficients presented in Table 1.

Detailed saturated enthalpy data between 90C and the critical temperature of 94.7C was not available, but as this corresponds with system operation at pressures in excess of 30.9 bar this is not considered to be an issue in the work reported here.

2.3 Subcooled liquid enthalpy relationship


Approximate subcooled liquid enthalpy calculations can be made on the assumption that enthalpy of any subcooled liquid is equal to the saturation enthalpy at the same temperature. Observation of the p-h diagrams published for R-1234yf shows that this is a reasonable assumption at liquid temperatures between around 0 and 50C. However, a more rigorous approach yielding better accuracy across the complete temperature range necessitates the calculation of subcooled liquid enthalpy as a function of both pressure and temperature. In view of this, a 3D surface fit is required, and it was found that a full cubic 3D polynomial of the form shown below works well:

(3)

where hliq is enthalpy of subcooled liquid in kJ/kg as a function of P (pressure in bar abs), and t (temperature in C). Again, coefficients c0 to c9 are presented in Table 1, and recovery of subcooled liquid enthalpies from the fit given above generates data accurate to within around 0.2% of published values across a the entire range of temperature and pressure of interest. This corresponds with a correlation coefficient, R2, of 0.99993.

2.4 Superheated vapour enthalpy relationship


Derivatives of the Martin-Hou equation of state enable the direct calculation of ideal gas heat capacity, but this is of limited use in the analysis of the superheated region of automotive refrigerant cycles. Non-ideal gas behaviour in the vicinity of the saturated vapour line can result in considerable inaccuracies in calculations of vapour enthalpy. Clearly superheated vapour enthalpy is a function of both pressure and temperature, and again...

Erscheint lt. Verlag 5.5.2011
Sprache englisch
Themenwelt Naturwissenschaften Physik / Astronomie Thermodynamik
Technik Bauwesen
Technik Maschinenbau
ISBN-10 0-85709-505-6 / 0857095056
ISBN-13 978-0-85709-505-3 / 9780857095053
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