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12-1 Given d m a x = 1.000 in and b m i n = 1.0015 i n , the mini mum radial clearance is
Also
Eq. (12-7):
Fig. 12-16:
Fig. 12-19:
Fig. 12-18:
Fig. 12-20:
cmin
b mi n d n 1 .0015 1 .000
2 2
l/d = 1
r = 1.000/2 = 0.500
r/c = 0.500/0.00075 = 667
N = 1100/60 = 18.33 rev/s
P = W/(ld) = 250 /[( 1)( 1)] = 250 psi
8(10- 6
)(18.33) '
0.000 75 in
S (6672
)250
h00/c
Q/(rcNl)
fr/c
Qs / Q
0. 261
0.595
3.98
5.8
0.5
f 0.0087
h0 = 0.595(0.00075) = 0.000466 in Ans.
5.8 5.8- ^
r/c 667
The power loss in Btu/s is
2:TfWrN 2n (0.0087)(250)(0.5)(18.33)H778(12)778(12)
= 0.0134 Btu/s Ans.
Q = 3.98rcNl = 3.98(0.5)(0.000 75)(18.33)(1) = 0.0274 in 3/s
Qs = 0.5(0.0274) = 0.0137 in3
/s Ans.
_ _ _
_ _
_
_
_ _
bmin - dmax 1.252 - 1.250
c m i n = 2 = 2 = 0.001 in
r =.
1 .25/2 = 0.625 in
r/c = 0.625/0.001 = 625
N = 1150/60 = 19.167 rev/s
400
P = = 128 psi1 .25(2.5)
l/d = 2.5/1.25 = 2
(6252
)(10)(10- 6
)(19.167)S = = 0.585
128
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313
The interpolation formula of Eq. (12-16) w i l l have to be used. From Figs. 12-16, 12-21,
and 12-19
For //d = oo, ho/e = 0.96, PI p m a x = 0.84,
//d = 1, ho/e = 0.77, P /pmax = 0.52,
1
l/d = , ho/e = 0.54, P /p m a x = 0.42,2
1l/d = , ho/e = 0.31, P / p m a x = 0.28,
Q
reNl
Q
reNlQ
reNl
Q
3.09
3.6
4.4
5.254 rcNl
Equation (12-16) is easily programmed by code or by using a spreadsheet. The results are:
l/d yiy
1 / 2 y 1 / 4
ho/e 2 0.96 0.77 0.54 0.31 0.88
pP/pPmax 2 0.84 0.52 0.42 0.28 0.64
Q / reNl 2 3.09 3.60 4.40 5.25 3.28
ho = 0.88(0.001) = 0.000 88 in Ans.
128p
max0.64
200 psi Ans.
Q = 3.28(0.625)(0.001)(19.167)(2.5) = 0.098 in3/s Ans.
12-3
e
min
bmin - dmax 3.005 - 3.000
2 2
r =. 3.000/2 = 1 .500 in
l/d = 1 .5/3 = 0.5
r/e = 1 .5/0.0025 = 600
N = 600/60 = 10 rev/s
800
0.0025 in
P1 . 5(3)
Fig. 12-12: SAE 10, ' = 1.75 /zreyn
S = (6002
)
177.78 psi
1.75(10 - 6 )(10)
177.780.0354
Figs. 12-16 and 12-21: ho/e = 0.11, P /p m a x = 0.21
ho = 0.11(0.0025) = 0.000 275 in Ans.
pmax = 177.78/0.21 = 847 psi Ans.
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Fig. 12-12: SA E 40, = 4.5 reyn
( 4.5 \) = 0.09101 .75ho/e = 0.19, P /p m a x = 0.275
ho = 0.19(0.0025) = 0.000475 in Ans.
pmax = 177.78/0.275 = 646 psi Ans.
12-4bmin - dmax 3.006 - 3.000
e m i n = 2 = 2 = 0.003
r = . 3.000/2 = 1 . 5 in
l/d = 1
r/e = 1 .5/0.003 = 500
N = 750/60 = 12.5rev/s
600
P = = 66.7 psi3(3)
Fig. 12-14: SAE 10W, = 2.1 reyn
'2 .1(10- 6
) (12.5)S = (500 2)
66.70.0984
From Figs. 12-16 and 12-21:
ho/e = 0.34, P /pm a x
= 0.395
ho = 0.34(0.003) = 0.001 020 in Ans.
66.7
p m a x = = 169 psi Ans.0.395
Fig. 12-14: SAE 20W-40, = 5.05 reyn
' 5.05(10- 6 ) (12.5)
S = (500 2)66.7
0.237
From Figs. 12-16 and 12-21:
ho/e = 0.57, P/pmax = 0.47
ho = 0.57(0.003) = 0.001 71 in Ans.
66.7
pm a x = = 142 psi Ans.
0.47
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1 2 - 5
bmin - dmax 2.0024 - 2c m i n = = = 0.0012 in
2 2
d 2r = = - = 1in , l/d = 1/2 = 0.50
2 2
r/c =1/0.0012 =833
N =800/60 = 13.33 rev/s
600P = = 300 psi
2(1)
Fig. 12-12: SAE 20, =3.75 reyn
' 3.75(10- 6
)(13.3)S = (8332
)300
0.115
From Figs. 12-16, 12-18 and 12-19:
ho/c = 0.23, rf/c = 3.8, Q/(rcNl) =5.3
ho = 0.23(0.0012) = 0.000 276 in Ans.
3.8
f = = 0.00456
833
The powerloss due to friction is
2:TfWrN 2n (0.004 56)(600)( 1) (13.33)
H = =778(12) 778(12)
= 0.0245 Btu/s Ans.
Q = 5.3rcNl
= 5.3(1)(0.0012)(13.33)(1)
= 0.0848 in3
/s Ans.
12-6_ bmin - dmax _ 25.04 - 25
c min _
2 2
r ' d/2 = 25/2 = 12.5 mm,
r/c = 12.5/0.02 = 625
N = 1200/60 = 20 rev/s
= 0.02 mm
l/d = 1
1250P =
l o r = 50 MPa s, S
252
(6252
)
2 M Pa
50(10- 3
) (20)2(10
6
)0.195
From Figs. 12-16, 12-18 and 12-20:
ho/c = 0.52, fr/c = 4.5, Qs/Q = 0.57
ho = 0.52(0.02) = 0.0104 mm Ans.
f=
T =
4. 5
6250.0072
fWr = 0.0072(1.25)(12.5) = 0.1125 N m
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The power loss due to friction is
H = 2nTN = 2n(0.1125)(20) = 14.14 W Ans.
Qs = 0.57 Q The side flow is 57% of Q Ans.
12-7bmin - dmax 30.05 - 30.00
c m i n = = = 0.025 mm
d 30r = 15 mm
2 2
r 15- = = 600c 0.025
1120N = = 18.67 rev/s
60
2750
P = = 1.833 MPa30(50)
2 ' 60(10- 3 )(18.67)
S = (600 2)1 . 833(10
6)0.22
l 50= = 1.67d 30
This //d requires use of the interpolation of Raimondi and Boyd, Eq. (12-16).
From Fig. 12-16, the ho/c values are:
y1/4 = 0.18, y i / 2 = 0.34, y i = 0.54, y ^ = 0.89
hoSubstituting into Eq. (12-16), = 0.659
c
From Fig. 12-18, the fr/c values are:
y 1 / 4 = 7.4, y 1 / 2 = 6.0, y 1 = 5.0, yoo = 4.0
fr
Substituting into Eq. (12-16), = 4.59c
From Fig. 12-19, the Q/(rcNl) values are:
y 1 / 4=
5.65, y 1 / 2=
5.05, y 1=
4.05,=
2.95Q
Substituting into Eq. (12-16), = 3.605
rcNl
ho = 0.659(0.025) = 0.0165 mm Ans.
f = 4.59/600 = 0.007 65 Ans.
Q = 3.605(15)(0.025)(18.67)(50) = 1263 mm3
/s Ans.
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1 2 - 8 bmin - dmax 75.10 - 75c m i n = = = 0.05 mm
2 2
l/d = 36/75 = 0.5 (close enough)
r = d/2 = 75/2 = 37.5 mm
r/c = 37.5/0.05 = 750
N = 720/60 = 12 rev/s
2000
P = = 0.741 MPa75(36)
Fig. 12-13: SAE 20, 1 = 18.5MPa s
18.5(10- 3
)(12)S = (750 2)
0.741(106)0.169
From Figures 12-16, 12-18 and 12-21:
ho/c = 0.29, fr/c = 5.1, P /pmax = 0.315
ho = 0.29(0.05) = 0.0145 mm Ans.
f = 5.1/750 = 0.0068
T = fWr = 0.0068(2)(37.5) = 0.51 N m
The heat loss rate equals the rate ofworkon the film
//loss = 2:rTN = 2n (0.51)(12) = 38.5W Ans.
p m a x = 0.741/0.315 = 2.35 MPa Ans.
Fig. 12-13: SAE 40, 1 = 37 MPa s
S = 0.169(37)/18.5 = 0.338
From Figures 12-16, 12-18 and 12-21:
ho/c = 0.42, fr/c = 8.5, P/pmax = 0.38
ho = 0.42(0.05) = 0.021 mm Ans.
f = 8.5/750 = 0.0113
T = fWr = 0.0113(2)(37.5) = 0.85 N m
H l o s s = 2n TN = 2n (0.85)(12) = 64 W Ans.
pmax = 0.741 /0.38 = 1 .95 MPa Ans.
_
bmin - dmax 50.05 - 50
c m i n = = = 0.025 mm2 2
r = d/2 = 50/2 = 25 mm
r/c = 25/0.025 = 1000
l/d = 25/50 = 0.5, N = 840/60 = 14 rev/s
2000
P = = 1.6MPa25(50)
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Fig. 12-13: SAE 30, X = 34 MPa s
2 r34(10- 3 ) (14)
S = (1000 )1.6(10
6
)
From Figures 12-16, 12-18, 12-19 and 12-20:
0.2975
ho/c = 0.40, fr/c = 7.8, Qs / Q = 0.74, Q/(rcNl) = 4.9
ho = 0.40(0.025) = 0.010 mm Ans.
f= 7.8/1000 = 0.0078
T = fWr = 0.0078(2)(25) = 0.39 N m
H = 2n TN = 2n (0.39)(14) = 34.3W Ans.
Q = 4.9rcNl = 4.9(25 )(0.025 )(14)(2 5) = 1072 mm2
/s
Qs = 0.74(1072) = 793 mm3
/s Ans.
12-10 Consider the bearings as specified by
minimum f:
maximum W:
and differing only in dand d'.
Preliminaries:
b+tb
b
- 0
Fig. 12-16:
minimum f:
maximum W:
Fig. 12-12:
Eq. (12-7):
Forminimum f:
IJLN / P =
l/d = 1
P = 700/(1.252
) = 448 psi
N = 3600/60 = 60 rev/s
S = 0.08
S = 0.20
1.38(10- 6
)reyn
1.38(10- 6
)(60/448) = 0.185(10- 6
)
r
c
S
XN / P
0.08658
0 .185(10- 6
)
c = 0.625/658 = 0.000 950 = 0.001 in
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I f this iS C m i n ,
b d = 2(0.001) = 0.002 in
The median clearance is
, td + tb , td + tb
c = c m i n + 2 = 0.001 + 2
and the clearance range forthis bearing is
. td + tbAc =
2
which is a function only of the tolerances.
Formaximum W:
r / 0.2
- = J ^ = 1040
c \ 0
I f this is c m i n
c y 0.185(106 )
c = 0.625/1040 = 0.000 600 = 0.0005 in
b d' = 2c m i n = 2(0.0005) = 0.001 in
, td + tb n^nr- .t
d +t
b
c = c m i n + 2 = 0.0005 + 2
. td +t
bAc =
2
The difference (mean) in clearance between the two clearance ranges, c r a n g e , is
c r a n g e = 0.001 + 2 I 0.0005 + 2 I
= 0.0005 in
For the minimum f bearing
b d = 0.002 in
or
d = b 0.002 in
For the maximum Wbearing
d' = b 0.001 in
For the same b, tb and td, we need to change the journal diameter by 0.001 in .
d' d = b 0.001 (b 0.002)
= 0.001 in
Increasing dof the minimum friction bearing by 0.001 i n, defines d'of the maximum load
bearing. Thus, the clearance range provides for bearing dimensions which are attainable
in manufacturing. Ans.
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12-11 Given: SAE 30, N = 8rev/s, Ts = 60C, l/d = 1, d = 80 mm, b = 80.08 mm,
W = 3000N
bmin - dmax 80.08 80
c m i n = = = 0.04 mm2 2
r = d/2 = 80/2 = 40 mm
r 40
- = = 1000c 0.04
3000P = = 0.469 MPa
80(80)
Trial #1: From Figure 12-13 forT = 81C, \x = 12 MPa s
AT = 2(81C 60C) = 42C
12(10- 3
) (8)
S = (1000
2
)
From Fig. 12-24,
0.120AT
0.469(106) 0.2047
0.349 + 6.009(0.2047) + 0.0475(0.2047)2
= 1.58P
(0.469\I = 6.2C0.120 /Discrepancy = 42C 6.2C = 35.8C
Trial #2: From Figure 12-13 for T = 68C, \ = 20 MPa s,
AT = 2(68C 60C) = 16C
(2 0 \ I = 0.34112From Fig. 12-24,
0.120AT0.349 + 6.009(0.341) + 0.0475(0.341)
2
= 2.4P
(
0.469\I = 9.4C
0.120 /
Discrepancy = 16C 9.4C = 6.6C
Trial #3: \ = 21 MPa s, T = 65C
AT = 2(65C 60C) = 10C
(21 \ I = 0.35812
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From Fig. 12-24,
0.120 AT0.349 + 6.009(0.358) + 0.0475(0.358)
2
= 2.5P
(
0.469\I = 9.8C
0.120 /
Discrepancy = 10C 9.8C = 0.2C O.K.
Tav = 65C Ans.
T1 = Tav AT/2 = 65C (10C/2) = 60C
T 2 = Tav + AT/2 = 65C + (10C/2) = 70C
S = 0.358
From Figures 12-16, 12-18, 12-19 and 12-20:
ho Q Qs = 0.68, fr/c = 7.5, = 3.8, = 0.44c rcN l Q
ho = 0.68(0.04) = 0.0272 mm Ans.
7.5f = = 0.0075
1000
T = fWr = 0.0075(3)(40) = 0 . 9 N m
H = 2n TN = 2n (0.9)(8) = 4 5 . 2 W Ans.
Q = 3.8(40)(0.04)(8)(80) = 3891 mm 3/s
Qs = 0.44(3891) = 1712mm3
/s Ans.
12-12 Given: d = 2.5 in , b = 2.504 i n , c m i n = 0.002 in, W = 1200 lb f ,SAE = 20 , Ts = 110F,
N = 1120 rev/min, and l = 2 .5 in .
For a trial film temperature Tf = 150F
Tf S A T (From Fig. 12-24)
150 2.421 0.0921 18.5
AT 18.5FTav = Ts + = 110F + = 119.3F2 2
Tf Tav = 150F 119.3F
which is not 0.1 orless, therefore try averaging
150F + 119.3F(Tf ) n e w = = 134.6F
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Proceed with additional trials
Trial Ne w
Tf l-i' S AT Tf
150.0 2.421 0.0921 18.5 119.3 134.6
134.6 3.453 0.1310 23.1 121.5 128.1
128.1 4.070 0.1550 25.8 122.9 125.5
125.5 4.255 0.1650 27.0 123.5 124.5
124.5 4.471 0.1700 27.5 123.8 124.1
124.1 4.515 0.1710 27.7 123.9 124.0
124.0 4.532 0.1720 27.8 123.7 123.9
Note that the convergence begins rapidly. There are ways to speed this, but at this point
they would only add complexity. Depending where you stop, you can enterthe analysis.
(a) \jt! = 4.541(10 6 ) , S = 0.1724
hoFrom Fig. 12-16: = 0.482, ho = 0.482(0.002) = 0.000 964 in
c
From Fig. 12-17: 0 = 56 Ans.
(b) e = c ho = 0.002 0.000 964 = 0.001 04 in Ans.
fr(c) From Fig. 12-18: = 4.10, f = 4.10(0.002/1.25) = 0.006 56 Ans.
c
(d) T = fWr = 0.006 56(1200)(1.25) = 9.84 lbf in
2n TN 2n (9.84)(1120/60)H = = = 0.124 Btu/s Ans.
778(12) 778(12)
Q 1120(e) From Fig. 12-19: = 4.16, Q = 4.16(1.25)(0.002M I (2.5)
rcNl 60
= 0.485 in 3/s Ans.
Qs 3From Fig. 12-20: = 0.6, Qs = 0.6(0.485) = 0.291 in
3/s Ans.Q
P 1200
(f) From Fig. 12-21: = 0.45, pmax =
2 = 427 psi Ans.pmax 2. 5
2(0.45)
0p = 16 Ans.
(g)
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12-13 Given: d = 1.250 in , ta = O.OOlin, b = 1.252in, tb = 0.003i n, / = 1.25in, W = 250lbf,
N = 1750 rev/min, SA E 10 lubricant , sump temperature Ts = 120F.
Below is a partial tabular summary for comparison purposes.
c
mi n cc
max0.001 in 0.002 in 0.003 in
Tf 132.2 125.8 124.0
AT 24.3 11.5 7.96
Tmax 144.3 131.5 128.0
n' 2.587 3.014 3.150
S 0.184 0.053 7 0.0249
e 0.499 0.775 0 0.873
fr
c4.317 1.881 1.243
QrcNjl
4.129 4.572 4.691
Qs
Q0.582 0.824 0.903
ho
c0.501 0.225 0.127
f 0.006 9 0.006 0.005 9
Q 0.0941 0.208 0.321
Qs 0.0548 0.172 0.290
ho 0.000 501 0.000 495 0.000 382
Note the variations on each line. There is not a bearing, but an ensemble of many bear-
ings, due to the random assembly of toleranced bushings and journals. Fortunately the
distribution is bounded; the extreme cases, c m i n and c m a x , coupled with c provide the
charactistic description for the designer. A l l assemblies must be satisfactory.
The designer does not specify a journal-bushing bearing, but an ensemble of bearings.
12-14 Computer programs w i l l varyFortran based, M A T L A B , spreadsheet, etc.
12-15 In a step-by-step fashion, we are building a skill for natural circulation bearings.
Giv en the average film temperature, establish the bearing properties.
Giv en a sump temperature, find the average film temperature, then establish the bearing
properties.
No w we acknowledge the envi ronmental temperature's role in establishing the sump
temperature. Sec. 12-9 and Ex. 12-5 address this problem.
The task is to iteratively find the average film temperature, Tf, which makes Hgen and
H l o s s equal. The steps for determining c m i n are provided within Trial #1 through Trial #3
on the following page.
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Trial #1:
Choose a value of Tf.
Find the corresponding viscosity.
Find the Sommerfeld number.
Find fr/c, then
2545Hgen = WNc
1050
Find Q/(rcNl) and Qs/ Q. From Eq. (12-15)
0.103P(fr/c)AT = J '
(1 0.5 Qs /Q )[Q/(rcNjl)]
hcR A( Tf Too)H l o s s = \ '
1 + a
Display Tf, S, H g e n , H l o s s
Trial #2: Choose another Tf, repeating above drill.
Trial #3:
Plot the results of the first tw o trials.
Choose (Tf)3 from plot. Repeat the drill. Plot the results ofTrial #3 on the above graph.
I f you are not within 0.1F, iterate again. Otherwise, stop, and find all the properties of
the bearing for the first clearance, c m i n . See i f Trumpler conditions are satisfied, and i f so,
analyze c and c m a x .
The bearing ensemble in the current prob lem statement meets Trumpler's criteria
(fornd = 2).
This adequacy assessment pro tocol can be used as a design tool by giving the students
additional possible bushing sizes.
b (in) tb (in)
2.254 0.004
2.004 0.004
1.753 0.003
Otherwise, the design option includes reducing l/d to save on the cost of journal machin
ing and vender-supplied bushings.
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12-16 Continue to build a skill with pressure-fed bearings, that of finding the average tempera
ture of the fluid film. First examine the case forc = c m i n
Trial #1 :
Choose an initial Tf.
Find the viscosity.
Find the Sommerfeld number.
Find fr/c, ho/c, and e.
From Eq. (12-24), find AT.
ATTav = Ts +
2
Display Tf, S, AT, and Tav.
Trial #2:
Choose anotherTf. Repeat the drill, and display the second set of values for Tf,
S, A T, and Tav. Plot Tav vs Tf :
i
i
1
\if>2 Uf)3 U f)l
Trial #3:
Pickthe third Tf from the plot and repeat the procedure. I f(Tf ) 3 and ( Ta v ) 3 differ by more
than 0 . l F , plot the results forTrials #2 and #3 and try again. I fthey are within 0 . l F ,de -
termine the bearing parameters, check the Trumple r cri teria, and compare / / l o s s with the
lubricant's cooling capacity.
Repeat the entire procedure forc = c m a x to assess the cooling capacity for the maxi
mum radial clearance. Finally, examine c = Cto characterize the ensemble of bearings.
12-17 A n adequacy assessment associated with a design task is required. Trumpler 's criteria
w i l l do.
d = 50.00+0 05 mm, b = 50.084+ ' 0 1 0 mm
SAE 30, N = 2880 rev/min or 48 rev/s, W = 10 k N
bmin - dmax 50.084 - 50c m i n = = = 0.042 mm
2 2
r = d/2 = 50/2 = 25 mm
r/c = 25/0.042 = 595.
1l - (55 5) = 25 mm
2
l'/d = 25/50 = 0.5
W 10(106
)p = = = 4000 kPa
4r l ' 4(0.25)(0.25)
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Trial #1: Choose (Tf ) 1 = 79C. From Fig. 12-13, JZ = 13 MPa s.
13(10 3 )(48) 'S = (595
2
)
From Figs. 12-18 and 12-16:
From Eq. (12-25), AT =
0.0554000(10
3
)
fr = 2.3, e = 0.85.
c
978(106
) (f r / c ) SW 2
1 + 1.5e2 psr
4
978(106
) 2.3(0.055)(102
)
200(25)41 + 1 . 5(0.85)2
= 76.0C
Tav = Ts + AT/2 = 55C + (76C/2) = 93C
Trial #2: Choose (Tf ) 2 = 100C. From Fig. 12-13, JI= 7MPa s.
S = 0.055 ( 13(7 \
13 0.0296
frFrom Figs. 12-18 and 12-16: = 1.6, e = 0.90
AT978(10
6
)
1 + 1 .5(0.9)2
1.6(0.0296)(102
)
200(25)4
26.8C
26.8CTav = 55C + z = 68.4C2
100
90
80
70
(79C, 93C)
(79C, 79C)
> 85 C
L V_ | 1 L
(100C, 100C)
60 70 80 90 100 f
(100C, 68.4C)
Trial #3: Thus, the plot gives (Tf ) 3 = 85C. From Fig. 12-13, JX = 10.8MPa s.
(10.8 \I = 0.045713fr
From Figs. 12-18 and 12-16: = 2.2, e = 0.875
AT978(10
6
)
1 + 1 .5(0.8752
)
2.2(0.0457)(102
)
200(25)4
58.6C
58.6CTav = 55C + = 84.3C
2
85C + 84.3CResult is close. Choose Tf = = 84.7C
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Fig. 12-13: = 10.8MPa s
(10.8\I =13 / 0.0457fr ho = 2.23, e = 0.874, = 0.13
c c
AT978(10
6
)
1 + 1.5(0.8742
)
59.5CTav = 55C + = 84.7C
2
2.23(0.0457)(102
)
200(254
)
O.K.
59.5C
From Eq. (12-22)
Qs = (1 + 1.5e2
)n psrc
3
3l'
n (200)(0.0423
)(25)
3(10)(106
)(25)
Trumpler:
= [1 + 1.5(0.874 2)]
= 3334 mm3
/s
ho = 0.13(0.042) = 0.005 46 mm or 0.000 215 in
ho 0.0002 + 0.000 04(50/25.4)
= 0.000 279 in Not O.K.
T m a x = Ts + AT = 55C + 63.7C = 118.7C or 245.7F O.K.
Pst = 4000 kPa or 581 psi Not O.K.
n = 1, as done Not O.K.
There is no point in proceeding further.
12-18 So far, we've performed elements of the design task. Now let's do it more completely.
First, rememberour viewpoint.
The values of the unilateral tolerances, tb and td, reflect the routine capabilities of the
bushing vendor and the in-house capabilities. Whi le the designer has to live with these,
his approach should not depend on them. They can be incorporated later.
First we shall find the minimum size of the journa l whi ch satisfies Trumpler's con
straint of Pst < 300psi.
W
2dV< 300
W
2d 2 1 ' /d < 300 == d >
W
600(l '/ d)
d
m i n
900
2(300)(0.5)1.73 in
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In this problem we w i l l take journal diameter as the nomina l value and the bushing bore
as a variable. In the next pro blem, we w i l l take the bushing bore as nominal and the jour
nal diameter as free.
To determine where the constraints are, we w i l l set tb = td = 0, and thereby shrink
the design window to a point.
We set d = 2.000 in
b = d + 2 c m i n = d + 2c
nd = 2 (This makes Trumpler's nd < 2 tight)
and construct a table.
d Tma x ho Pst Tmax n fom
0.0010 2.0020 2 215.50 312.0 XS X
-5 .74
0.0011 2.0022 2 206.75 293.0 X -6 .06
0.0012 2.0024 2 198.50 277.0 X -6 .37
0.0013 2.0026 2 191.40 262.8X
-6 .660.0014 2.0028 2 185.23 250.4 X -6 .94
0.0015 2.0030 2 179.80 239.6 X -7 .20
0.0016 2.0032 2 175.00 230.1 X -7 .45
0.0017 2.0034 2 171.13 220.3 X -7 .65
0.0018 2.0036 2 166.92 213.9
f- 7 . 9 1
0.0019 2.0038 2 163.50 206.9 -8 .12
0.0020 2.0040 2 160.40 200.6
s s s s-8 .32
*Sample cal cula tion for the first entry of this colum n.
Iteration yields: Tf = 215.5F
With Tf = 215.5F, from Table 12-1
X = 0.0136(10 - 6 )exp[12 71.6/(2 15.5 + 95)] = 0 .8 17 (1 0 - 6 ) r eyn
900N = 3000/60 = 50 rev/s, P = = 225 psi
4
S1
0.001
0.817(10 - 6 ) (50)0.182
From Figs. 12-16 and 12-18:
Eq. (12-24):
ATf =
225
e = 0.7, fr/c =
0.0123(5.5)(0.182)(9002
)
5.5
191 .6F[1 + 1.5(0.7 2 )](30)(1 4)
215.8F = 215.5F191 .6F
Tav = 120F + =2
For the nominal 2-in bearing, the various clearances show that we have been in contact
with the recurving of( ^ 0 ) m i n . The figure of merit (the parasitic friction torque plus the
pumping torque negated) is best at c = 0.0018 in . For the nomina l 2-in bearing, we w i l l
place the top of the design window at c m i n = 0.002 i n, and b = d + 2(0.002) = 2.004 in.
A t this poin t, add the b and dunilateral tolerances:
d 2.000+0 of)0 in, b = 2.004+0'00 in
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Now we can check the performance at c m i n , c, and c m a x . Of immediate interest is the fom
of the median clearance assembly, 9.82, as compared to any other satisfactory bearing
ensemble.
I f a nominal 1.875 in bearing is possible, construct another table with tb = 0 and
td = 0.
c b d Tmax ho Pst Tmax fos fom
0.0020 1.879 1.875 157.2 194.30 X S S S 7.36
0.0030 1.881 1.875 138.6 157.10 S S S S 8.64
0.0035 1.882 1.875 133.5 147.10 S S S S 9.05
0.0040 1.883 1.875 130.0 140.10 S S S S 9.32
0.0050 1.885 1.875 125.7 131.45 S S S S 9.59
0.0055 1.886 1.875 124.4 128.80 S S S S 9.63
0.0060 1.887 1.875 123.4 126.80 X S S S 9.64
The range of clearance is 0.0030 < c < 0.0055 in. That is enough room to fit in our de
sign window.
d = 1.875+0 o0i in, b = 1.881+ 0 '[ 00 in
The ensemble median assembly has fom =9.31 .
We just had room to fit in a design window based upon the ( h o ) m i n constraint. Further
reduction in no mina l diameterw i l l preclude any smaller bearings. A table constructed for a
d = 1.750 in journal w i l l prove this.
We choose the nominal 1.875-in bearing ensemble because it has the largest figure
of merit. Ans.
12-19 This is the same as Prob. 12-18 but uses design variables of nominal bushing bore b andradial clearance c.
The approach is similarto that of Prob. 12-18 and the tables w i l l change slightly. In the
table for a nominal b = 1.875 in , note that at c = 0.003 the constraints are "loose." Set
b = 1.875 in
d = 1.875 2(0.003) = 1.869 in
For the ensemble
b = 1.875+00 0? , d = 1.869+o0 00
Analyze at c m i n = 0.003, c = 0.004 in and c m a x = 0.005 in
At c m i n = 0.003 in: Tf = 138.4, \' = 3.160, S = 0.0297, H l o s s = 1035 Btu/h and the
Trumplerconditions are met.
At c = 0.004 in : Tf = 130F, \' = 3.872, S = 0.0205, H l o s s = 1106 Btu/h, fo m =
9.246 and the Trumpler conditions are O.K.
At c m a x = 0.005 in: Tf = 125.68F, \' = 4.325 /zreyn, S = 0.01466, H l o s s =
1129 Btu/h and the Trumpler conditions are O.K.
The ensemble figure of merit is slightly better; this bearing is slightly smaller. The lubri
cant cooler has sufficient capacity.
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12-20 From Table 1 2-1 , Seireg and Dandage, 0 = 0.0141(106)reyn and b = 1360.0
(reyn) = 0.0141 exp[1360/(T + 95)] ( T in F)
= 0.0141 exp[1 360/( 1.8C + 127)] (C in C)
( M P a s) = 6.89(0.0141) exp [13 60/ (1. 8C + 127)] (C in C)
For SA E 30 at 79C
= 6.89(0.0141) exp{1360/[1.8(79) + 127]}
= 15.2MPa s Ans.
12-21 Originally
d = 2.000+0 001 in , b = 2.005+0'00 in
Doubled,
d = 4.000+0 00 0 in, b = 4.010+0'00o
The rad ial load quadrupled to 3000 lbfwhen the analyses for parts (a) and (b) were carried
out. Some of the results are:
Trumpler
Part c S fr/c Qs ho/c H l o s s ho ho f
(a) 0.007 3.416 0.0310 135.1 0.1612 6.56 0.1032 0.897 9898 0.000 722 0.000 360 0.005 67
(b) 0.0035 3.416 0.0310 135.1 0.1612 0.870 0.1032 0.897 1237 0.000 361 0.000 280 0.005 67
The side flow Qs differs because there is a c3 term and consequently an 8-fold increase.
H l o s s is related by a 9898/1237 or an 8-fold increase. The existing ho is related by a 2-fold
increase. Trumpler's ( h o ) m i n is related by a 1.286-fold increase
fom = 82.37 for double size 1} an 8-fold increase for double-size
fo m = 10.297 fororiginal size
12-22 From Table 12-8: K = 0.6(10 ) i n min/(lbf ft h). P = 500/[(1)(1)] = 500 psi,
V = nDN/12 = n(1)(200)/12 = 52.4 ft/min
Tables 12-10 and 12-11: f1 = 1 .8, f2 = 1
Table 12-12: PVmax = 46 700 psi ft/min, Pmax = 3560 psi, Vmax = 100 ft/min
4 F 4(500)P m a x = = = 637 psi < 3560 psi O.K.
n DL n
F
P = = 500 psi V = 52.4 ft/minDL
PV = 500(5 2.4) = 26 200 psi ft/min < 46 700 ps i ft/min O.K.
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Solving Eq. (12-32) fort
n DLw n(1)(1)(0.005)t = = = 1388 h = 83 270 mi n
4/1 f2 KVF 4(1.8)(1)(0.6)(101 0)(52.4)(500)
Cycles = Nt = 200(83 270) = 16.7rev Ans.
12-23 Estimate bushing length with f1 = f2 = 1, and K = 0.6(101 0 ) i n 3 min/(lbf ft h)
1(1)(0.6)(10 _ 1 0)(2)(100)(400)(1000)Eq. (12-32): L = = 0.80in
3(0.002)
From Eq. (12-38), with fs = 0.03 from Table 12-9 applying nd = 2 to F
and hcR= 2.7 Btu/(h f t 2 F)720(0.03)(2)(100)(400)
L = = 3.58 in
778(2.7)(300 70)0.80 < L < 3.58 in
Trial 1 : Le t L = 1in , D = 1 in
4(2)(100)
P m a x = = 255 psi < 3560 psi O.K.
2(100)P = = 200 psi
1(1)
n (1)(400)V = = 104.7ft/min > 100 ft/min Not O.K.
12
Trial 2: Tr y D = 7 / 8 i n , L = 1 in
4(2)(100)P m a x = = 291 psi < 3560 psi O.K.
n(7/8)(1)
2(100)P = = 229 psi
7/8(1)
n(7/8)(400)V = = 91.6ft/min < 100 ft/min O.K.
12
PV = 229(91.6) = 20 976 psi ft/min < 46700 psi ft/min O.K.
V / 1
33 1.3
91.6
100 1.8(91.6 3 3 \J = 1.74100 33
L = 0.80(1.74) = 1.39 in
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Trial 3: Try D = 7/8 in, L = 1.5 in
4(2)(100)
P m a x = = 194 psi < 3560 psi O.K.n(7/8)(1.5)2(100)
P = = 152 psi, V = 91.6 ft/min7/8(1 .5)
PV = 152(91.6) = 13 923 psi ft/min < 46700 psi ft/mi n O.K.
D = 7 /8 in , L = 1.5 in is acceptable Ans.
Suggestion: Try smaller sizes.