Tag Archives: heat transfer

Analytical modelling of mechanical face seals: post #4

Analytical model for full film lubrication

In this post, a first model for full film lubrication is proposed. It will allow to determine the seal faces temperature, the thickness of the film between the faces, the friction torque, etc.

If the distance between the faces is assumed to be equal to the mean film thickness, the dissipated power by viscous friction is:

P=\mu \omega^2 S_f \frac{\left( r_o+r_i\right)^2}{4 h_m}

This power is transferred to the seal rings by conduction. According to post# 1, we have:

E_t \Delta T=\mu \omega^2 S_f \frac{\left( r_o+r_i\right)^2}{4 h_m}

According to post# 3, the film thickness is given by:

h_m=\frac{\beta \Delta R}{4 \left(B_t-0.5 \right)}

The coning angle \beta is due to the faces deformations as explained in post #2:

\beta=N \Delta T+\beta_e

Finally, the fluid viscosity  \mu is a function of the local temperature. By using an exponential law, we have:

\mu \left(\Delta T\right)=\mu_0 \exp \left(-\alpha \Delta T\right)

where \mu_o is the viscosity at the reference temperature and \alpha the thermoviscosity coefficient.

A non linear equation of the seal faces temperature is obtained:

E_t \Delta T=\mu_0 \exp{\left( -\alpha \Delta T\right)} \omega^2 S_f \frac{ \left( r_o+r_i \right)^2 \left( B_t-0.5 \right) }{ \left( N \Delta T+\beta_e \right) \Delta R }

It is convenient to use a dimensionless form of this equation. For that a temperature scale based on the thermoviscosity coefficient is used:

\bar{T}=\Delta T \alpha

Then the previous non linear equation temperature becomes:

\bar{T}=\exp{\left(-\bar{T}\right)}\frac{Se}{\bar{T} + Co}

In this equation Se is the sealing number and is a kind of thermal loading number of the seal face:

Se=\mu_o \pi \omega^2\frac{\left( r_o+r_i \right)^3\left( B_t-0.5 \right) }{E_t N }

The second dimensionless number, Co, is the coning number. It represents an initial coning of the faces due to mechanical loading (fluid pressure) or wear of the faces:

Co=\frac{\beta_e \alpha}{N}

According to governing equation, the seal faces temperature rises with the sealing number, Se. However, the magnitude of this temperature is reduced by the decrease in viscosity with temperature (exponential term) and the increase in film thickness with temperature (denominator). A positive initial coning number, Co , will increase the film thickness and thus reduce temperature whereas a negative value will produce the invert.

The governing equation can be easily solved by using Excel for example. When the temperature of the faces is known, it is then possible to compute the film thickness, the leakage flow, the friction torque, etc. The next figure presents the dimensionless temperature rise as a function of the sealing number for different values of the coning number.

In the case of negative coning number, the temperature can not be lower than -Co to avoid negative coning and film thickness. This situation is not realistic and will lead to faces contact. To analyze

this effect, the minimum film thickness can be expressed in a dimensionless form:

\bar{h}_{min}=Co+\bar{T}

 

The film film thickness is presented as a function of the sealing number; Se, for different values of the coning number Co in the next figure. As expected the film thickness is an increasing function of Se. For positive coning number, the minimum film thickness can not decrease below a threshold avoiding faces contact. For negative or null values of Co, the film thickness can reach zero at low sealing number values. In this case face contact will be experienced. According to my experience, the dimensionless film thickness corresponding to the appearance of contact (three times the r.m.s roughness height), is approximately equal to 0.5. Above this value, the present model is correct. Below this threshold mixed lubrication is expected to occur. This boundary between full film and mixed lubrication regimes has been added on the temperature map (dashed curve):

0.5=Co+\bar{T}

It is now necessary to consider contact between the surfaces of the seal.

References

Brunetière, N. & Apostolescu, A. A Simple Approach to the ThermoElastoHydroDynamic Behavior of Mechanical Face Seals Tribology Transactions, 2009, 52, 243-255

 

 

Analytical modelling of mechanical face seals: post #2

Deformation of the seal faces

The second step of the model concerns deformation of the mechanical seal faces. To be able to accurately determine the behavior of the seal it is mandatory to know the geometrical configuration of the seal faces. Usually, the magnitude of the deformations is a couple of microns (Doust and Parmar, 1986) to be compared to the distance between the faces which is of the order of a micron. The model presented here is axisymetric and thus the deformation considered is an angular deformation leading to a conical shape of the faces. It can be measured by mean of a taper or coning angle as illustrated on the next figure.

Two types of deformation can be identified (Doust and Parmar 1986). The first one is due to thermal gradient in the rings and leads to a coning angle \beta_t. This angle is proportional to the seal face temperature rise \Delta T leading to the following rotation:

 

\beta_t=N \Delta T

where N is the thermal rotation rate. It is important to note that for many seal rings design, the coefficient N is positive if calculated as indicated on the previous figure.

An additional deformation \beta_e is due to the mechanical loading generated by the sealed fluid pressure and the springs, O-rings, etc. Unfortunately, there exists no analytical solution of this problem and these angles must be calculated by FEA. However, these coefficients remain constant as long as the boundary conditions are unchanged. For example, the next figure presents the evolution of b=N/\lambda as a function of \bar{E_t} for a rectangular ring of length e, width \Delta r and radii ratio of 0.88. Here \lambda is the thermal expansion coefficient of the material.

The total coning angle \beta can be expressed in this way:

 

\beta=N \Delta T+\beta_e

Reference

Doust, T. & Parmar, A. An Experimental and Theoretical Study of pressure and thermal Distortions in a Mechanical Seal ASLE Transactions, 1986, 29, 151-159

 

 

 

 

Analytical modelling of mechanical face seals: post #1

Heat transfer in mechanical seals

The first step of the model concerns heat transfer in the mechanical seal rings. As illustrated in the following figure, the mechanism of heat transfer in the vicinity of mechanical seal could be quite complicated.

However it has been shown that the heat generated in the seal interface is mainly transferred by conduction through the rings to the surrounding sealed fluid and then removed by convection. The heat transfer or convection coefficient is h_c. This parameter in mechanical seal can be evaluated using the Becker’s correlation (Becker 1963).

 

The previous figure shows the temperature distribution in the stationary part (part 1) of the seal when submitted to a heat flux q_1. The average resulting temperature rise of the face is \Delta T_1. Let us introduce the thermal efficiency E_{t1} of the ring 1 defined as the ratio of the thermal power P_1 entering the face to the average temperature rise.

E_{t1} = \frac{P_1}{\Delta T_1}= \pi \left( r_o^2-r_i^2\right)\frac{q_1}{\Delta T_1}

where r_o and r_i are respectively the outer and inner radii of the seal interface.

For a given seal design, this coefficient is only dependent on the thermal boundary conditions and can easily be calculated with a FEA software. If the seal width \Delta r=r_o- r_i is very small compared to the ring length e, an analytical expression of E_{t} can be found using the fin theory (Buck, 1989):

 

E_t = 2 \pi r_oe h_c \frac{\tanh m}{m}

where m is a heat transfer parameter including h_c and the thermal conductivity of the ring k :

m = \frac{e}{\Delta r} \sqrt{ \frac{h_c \Delta r }{k} }

A dimensionless version of the thermal efficiency can be expressed in this way:

\bar{E_t}=\frac{E_t}{2 \pi r_oeh_c }

The evolution of the dimensionless thermal efficiency is presented on the next figure as a function of the thermal parameter m (black solid curve). On the same figure, results obtained with FEA are presented when the seal ring length is varied from 1 to 8 and for a radii ratio of 0.88. It can be seen that the analytical solution is a reasonable approximation when the seal length is more than 4 times the seal width.

If the two seal rings are supposed to be at the same temperature \Delta T= \Delta T_1= \Delta T_2, a global thermal efficiency E_t, being the sum of the two individual thermal efficiencies, can be defined. The total thermal power P entering the seal faces is thus:

P=E_t \Delta T= \left(E_{t1}+ E_{t2}\right)\Delta T

References

Becker, K. “Measurement of Convective Heat Transfer from a Horizontal Cylinder Rotating in a Tank of Water,” International Journal of Heat and mass Transfer (6), 1963, pp. 1053-1062.

Buck, G. “Heat Transfer in Mechanical Seals”‘Proceedings of the 6th International Pump Users Symposium’, Houston, Texas, USA, 1989, pp. 9-15.