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Chapter 6 Long Hydrodynamic Journal Bearing
6.1 Introduction
6.2 Reynolds Equation for a Journal Bearing
6.3 Journal Bearing with Rotating Sleeve
6.4 Combined Rolling and Sliding
6.5 Pressure Wave in a Long Journal Bearing
6.6 Sommerfeld Solution of the Pressure Wave
6.7 Journal Bearing Load Capacity
6.8 Load Capacity Based on Sommerfeld Conditions
6.9 Friction in a Long Journal Bearing
6.10 Power Loss on Viscous Friction
6.11 Sommerfeld Number
6.12 Practical Pressure Boundary Conditions
Chapter 7 Short Journal Bearings
7.1 Introduction
7.2 Short-Bearing Analysis
7.3 Flow in the Axial Direction
7.4 Sommerfeld Number of a Short Bearing
7.5 Viscous Friction
7.6 Journal Bearing Stiffness
Chapter 8 Design Charts for Finite-Length Journal Bearings
8.1 Introduction
8.2 Design Procedure
8.3 Minimum Film Thickness
8.4 Raimondi and Boyd Charts and Tables
8.5 Fluid Film Temperature
8.6 Peak Temperature in Large, Heavily Loaded Bearings
8.7 Design Based on Experimental Curves
Chapter 9 Practical Applications of Journal Bearings
9.1 Introduction
9.2 Hydrodynamic Bearing Whirl
9.3 Elliptical Bearings
9.4 Three-Lobe Bearings
Copyright 2003 by Marcel Dekker, Inc. All Rights Reserved.
particularly in a high-speed journal bearing. Therefore, for proper design, the
bearing must operate at eccentricity ratios well below 1, to allow adequate
minimum film thickness to separate the sliding surfaces. Most journal bearings
operate under steady conditions in the range from e ¼ 0:6 to e ¼ 0:8. However,
the most important design consideration is to make sure the minimum film
thickness, hn, will be much higher than the size of surface asperities or the level
of journal vibrations during operation.
6.2 REYNOLDS EQUATION FOR A JOURNAL
BEARING
In Chapter 4, the hydrodynamic equations of a long journal bearing were derived
from first principles. In this chapter, the hydrodynamic equations are derived from
the Reynolds equation. The advantage of the present approach is that it can apply
to a wider range of problems, such as bearings under dynamic conditions.
Let us recall that the general Reynolds equation for a Newtonian incom-
pressible thin fluid film is
@
@x
h3
m
@p
@x
 
þ
@
@z
h3
m
@p
@z
 
¼ 6ðU1 À U2Þ
@h
@x
þ 12ðV2 À V1Þ ð6-5Þ
Here, U1 and U2 are velocity components, in the x direction, of the lower and
upper sliding surfaces, respectively (fluid film boundaries), while the velocities
components V1 and V2 are of the lower and upper boundaries, respectively, in the
y direction (see Fig. 5-2). The difference in normal velocity ðV1 À V2Þ is of
relative motion (squeeze-film action) of the surfaces toward each other.
For most journal bearings, only the journal is rotating and the sleeve is
stationary, U1 ¼ 0; V1 ¼ 0 (as shown in Fig. 6-1). The second fluid film boundary
is at the journal surface that has a velocity U ¼ oR. However, the velocity U is
not parallel to the x direction (the x direction is along the bearing surface).
FIG. 6-2 Velocity components of the fluid film boundaries.
Copyright 2003 by Marcel Dekker, Inc. All Rights Reserved.
Therefore, it has two components (as shown in Fig. 6-2), U2 and V2, in the x and y
directions, respectively:
U2 ¼ U cos a
V2 ¼ ÀU sin a
ð6-6Þ
Here, the slope a is between the bearing and journal surfaces. In a journal
bearing, the slope a is very small; therefore, the following approximations can be
applied:
U2 ¼ U cos a % U
V2 ¼ ÀU sin a % ÀU tan a
ð6-7Þ
The slope a can be expressed in terms of the function of the clearance, h:
tan a ¼ À
@h
@x
ð6-8Þ
The normal component V2 becomes
V2 % U
@h
@x
ð6-9Þ
After substituting Eqs. (6.7) and (6.9) into the right-hand side of the Reynolds
equation, it becomes
6ðU1 À U2Þ
@h
@x
þ 12ðV2 À V1Þ ¼ 6ð0 À UÞ
@h
@x
þ 12U
@h
@x
¼ 6U
@h
@x
ð6-10Þ
The Reynolds equation for a Newtonian incompressible fluid reduces to the
following final equation:
@
@x
h3
m
@p
@x
 
þ
@
@z
h3
m
@p
@z
 
¼ 6U
@h
@x
ð6-11Þ
For an infinitely long bearing, @p=@z ffi 0; therefore, the second term on the left-
hand side of Eq. (6-11) can be omitted, and the Reynolds equation reduces to the
following simplified one-dimensional equation:
@
@x
h3
m
@p
@x
 
¼ 6U
@h
@x
ð6-12Þ
6.3 JOURNAL BEARING WITH ROTATING
SLEEVE
There are many practical applications where the sleeve is rotating as well as the
journal. In that case, the right-hand side of the Reynolds equation is not the same
as for a common stationary bearing. Let us consider an example, as shown in Fig.
Copyright 2003 by Marcel Dekker, Inc. All Rights Reserved.

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  • 1.
  • 2. Chapter 6 Long Hydrodynamic Journal Bearing 6.1 Introduction 6.2 Reynolds Equation for a Journal Bearing 6.3 Journal Bearing with Rotating Sleeve 6.4 Combined Rolling and Sliding 6.5 Pressure Wave in a Long Journal Bearing 6.6 Sommerfeld Solution of the Pressure Wave 6.7 Journal Bearing Load Capacity 6.8 Load Capacity Based on Sommerfeld Conditions 6.9 Friction in a Long Journal Bearing 6.10 Power Loss on Viscous Friction 6.11 Sommerfeld Number 6.12 Practical Pressure Boundary Conditions Chapter 7 Short Journal Bearings 7.1 Introduction 7.2 Short-Bearing Analysis 7.3 Flow in the Axial Direction 7.4 Sommerfeld Number of a Short Bearing 7.5 Viscous Friction 7.6 Journal Bearing Stiffness Chapter 8 Design Charts for Finite-Length Journal Bearings 8.1 Introduction 8.2 Design Procedure 8.3 Minimum Film Thickness 8.4 Raimondi and Boyd Charts and Tables 8.5 Fluid Film Temperature 8.6 Peak Temperature in Large, Heavily Loaded Bearings 8.7 Design Based on Experimental Curves Chapter 9 Practical Applications of Journal Bearings 9.1 Introduction 9.2 Hydrodynamic Bearing Whirl 9.3 Elliptical Bearings 9.4 Three-Lobe Bearings Copyright 2003 by Marcel Dekker, Inc. All Rights Reserved.
  • 3. particularly in a high-speed journal bearing. Therefore, for proper design, the bearing must operate at eccentricity ratios well below 1, to allow adequate minimum film thickness to separate the sliding surfaces. Most journal bearings operate under steady conditions in the range from e ¼ 0:6 to e ¼ 0:8. However, the most important design consideration is to make sure the minimum film thickness, hn, will be much higher than the size of surface asperities or the level of journal vibrations during operation. 6.2 REYNOLDS EQUATION FOR A JOURNAL BEARING In Chapter 4, the hydrodynamic equations of a long journal bearing were derived from first principles. In this chapter, the hydrodynamic equations are derived from the Reynolds equation. The advantage of the present approach is that it can apply to a wider range of problems, such as bearings under dynamic conditions. Let us recall that the general Reynolds equation for a Newtonian incom- pressible thin fluid film is @ @x h3 m @p @x þ @ @z h3 m @p @z ¼ 6ðU1 À U2Þ @h @x þ 12ðV2 À V1Þ ð6-5Þ Here, U1 and U2 are velocity components, in the x direction, of the lower and upper sliding surfaces, respectively (fluid film boundaries), while the velocities components V1 and V2 are of the lower and upper boundaries, respectively, in the y direction (see Fig. 5-2). The difference in normal velocity ðV1 À V2Þ is of relative motion (squeeze-film action) of the surfaces toward each other. For most journal bearings, only the journal is rotating and the sleeve is stationary, U1 ¼ 0; V1 ¼ 0 (as shown in Fig. 6-1). The second fluid film boundary is at the journal surface that has a velocity U ¼ oR. However, the velocity U is not parallel to the x direction (the x direction is along the bearing surface). FIG. 6-2 Velocity components of the fluid film boundaries. Copyright 2003 by Marcel Dekker, Inc. All Rights Reserved.
  • 4. Therefore, it has two components (as shown in Fig. 6-2), U2 and V2, in the x and y directions, respectively: U2 ¼ U cos a V2 ¼ ÀU sin a ð6-6Þ Here, the slope a is between the bearing and journal surfaces. In a journal bearing, the slope a is very small; therefore, the following approximations can be applied: U2 ¼ U cos a % U V2 ¼ ÀU sin a % ÀU tan a ð6-7Þ The slope a can be expressed in terms of the function of the clearance, h: tan a ¼ À @h @x ð6-8Þ The normal component V2 becomes V2 % U @h @x ð6-9Þ After substituting Eqs. (6.7) and (6.9) into the right-hand side of the Reynolds equation, it becomes 6ðU1 À U2Þ @h @x þ 12ðV2 À V1Þ ¼ 6ð0 À UÞ @h @x þ 12U @h @x ¼ 6U @h @x ð6-10Þ The Reynolds equation for a Newtonian incompressible fluid reduces to the following final equation: @ @x h3 m @p @x þ @ @z h3 m @p @z ¼ 6U @h @x ð6-11Þ For an infinitely long bearing, @p=@z ffi 0; therefore, the second term on the left- hand side of Eq. (6-11) can be omitted, and the Reynolds equation reduces to the following simplified one-dimensional equation: @ @x h3 m @p @x ¼ 6U @h @x ð6-12Þ 6.3 JOURNAL BEARING WITH ROTATING SLEEVE There are many practical applications where the sleeve is rotating as well as the journal. In that case, the right-hand side of the Reynolds equation is not the same as for a common stationary bearing. Let us consider an example, as shown in Fig. Copyright 2003 by Marcel Dekker, Inc. All Rights Reserved.