Lyons W.C. (ed.). Standard handbook of petroleum and natural gas engineering.2001- Volume 1
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Table
4-38
(continued)
I
I
w
5
a
Mud
Pumps
637
Table
4-38
(continued)
140
TO
12
111
85
IO
Q,
w
00
5
a
E
-
MOOEL
x
UANUFACNREBCONTINEL
-
EMSCOiTMPLm
I
WAX
MAX
STRDKE LINER SIZE
(IN)
in
P
s
P
M
LENGTH
5
5-112
6
6-112
I
125a
120
12
,%?@
k2
=
1,
3645
5135
28(w
31
37
14
52
60
F:
a
640
Drilling and Well Completions
Mud
Pumps
641
642
Drilling and Well Completions
Table
4-40
Pump Output
vs.
Annular
Velocity
[18]
12
3
4
6 0
1
8
9
10
11
12
1s
14
16
16
17
4%
;#
7
6%
1%
6
6%
*%
6U
7%
1%
8%
8%
8%
876
9
0%
10%
11
uu
UY
I1
17%
M
:a
:#
8%
8%
1%
1%
:#
:a
8
IO
11
9
10
10
11
14
19
16
10
17
84
M
24
¶I
26
21
10
a4
OI
26
xa
ti
a2
ao
n
a8
a4
16
41
89
a7
68
11
40
U
#s
n
86
69
84
?4
117
111
Lwl
188
168
n
I4
I2
I9
16
11
I6
IO
21
22
n
n
11
41
84
4'7
41
49
42
61
U
40
62
46
42
60
46
68
60
66
'76
?I
CT
78
74
101
98
n
1w
184
110
118
I69
148
Ml
2s
211
616
6n
SI8
aa
in
in
I8
82
41
I(
a9
41
44
64
76
82
81
68
94
81
M
86
IO1
81
81
106
92
84
0s
01
I26
118
110
161
I41
186
le4
I67
148
111
104
171
w
269
fl7
184
810
rn
487
46a
in
nr
4m
41
81
n
41
64
6s
U
62
*6
I1
111
91
in
102
I41
181
147
In
I18
168
I21
167
118
124
14s
In
109
178
1-
811
M
247
UI
118
MI
ret
280
418
86L
601
411
441
7M
671
641
m
ns
rm
a89
48
41
11
71
64
W
n
n
17
OS
181
1M
141
110
IS6
1U
171
I40
117
166
141
tu4
161
141
174
180
107
101
I68
111
U6
tu
tu
167
841
10I
u1
464
416
686
U8
617
817
768
?49
ni
na
ni
4n
1W
n
118
1M
1u
118
I*
It4
MI
170
ul
w
1L(
u1
m
m
nr
m
Ma
m
w
281
n8
147
826
101
*If
194
462
481
01
Iu
661
cw
4lI
ma
781
118
ut
019
118
1.m
ma
ni
n*
1.m
1.m
lI*
I1
IO8
116
I84
181
188
in
m
in
ffl
m4
a88
XM
111
MI
XU
Ma
811
UI
m
au
ni
n4
168
82s
*U
406
470
444
-6
612
1n
1N
808
171
111
1.W
958
a
1-
1.281
IJU
410
49)
m
184
108
IH
I16
I14
I41
in
in
cu
M
ffl
m
m
ns
m
UT
118
U8
ma
841
m
n8
681
410
MI
267
491
488
4aI
M4
100
481
m
UI
ea1
lu
896
I?O
au
771
1.086
1.-
981
1417
m
YA
Mud
Pumps
643
lam
1.~4
1IOI
1.914
1.718
1-0
171
142
108
144
174
I86
IS7
246
u7
86s
801
426
M6
441
468
no
868
411
414
us
411
UI
UI
484
aa
w
w
140
w
H(
w
SI6
Ma
784
I**
1.066
1.m
1.410
1.814
LII
Lon
1.9Z.l
na
a81
nr
:%
181
150
100
104
196
to1
168
166
?.04
196
8x4
449
M7
465
408
481
420
M8
499
UT
471
484
WI
&Ea
Ul
718
UL
781
744
1bS
ma
400
ai
'E
E:
929
828
1.8-
I.lt6
1.M
1.610
1.4M
htI7
1,140
l,U4
191
168
114
181
I94
206
219
m
109
408
841
471
407
4w
424
601
ux
4011
698
460
411
486
UT
0,
We
166
117
a74
m
7M
741
WD
1.w
S78
tu)
nc
rei
:%
1.¶96
1.186
1m1
1.669
1.478
ut4
LIS1
1141
tM
1u
m
181
ma
216
214
mi
88s
8%
4I6
w
496
614
4u
484
MI
Ilt
442
In
Qo
uf
nl
616
lu
768
1-
w
In
1.111
1.W
1.m
SlO
1.446
1.406
1.861
1.Y4
1.7M
1,us
1.661
4n
ua
4n
na
2%
a.lu
110
I74
m
Ill
w
m
l41
me0
411
840
447
876
620
448
689
467
668
486
448
677
4U
640
MI
w4
U1
w
m
7m
74s
SO4
m
815
I.IU
LIU
1.W6
S68
1.616
1.478
1.us
1.m
moI
;I
198
z88
127
us
268
nr
840
40
886
608
421
690
509
611
uo
u4
6KZ
804
666
VI4
U6
ue
a71
1Sl
140
UI
U6
w
ne
m
na
1.m
E
1.11
I,-¶
Lfll
1.820
1,481
%I)
LIT8
1.847
1,wa
1M6
I.)tl
%*I7
8.084
LlI6
1.m
zms
x.m
M
214
g.
UI
162
ns
296
861
6011
417
S48
460
660
661
M5
$6
6U
7w
Ma
w
us
117
U1
?e,
741
LMI
nu
Slb
1.IM
1.-
1.-
1.486
1.170
1S60
1m
1.70
1.6Y
2.U6
L14S
1,996
ea8
675
1.m
i.no
267
UI
s4
aoo
ni
2m
aoa
a81
4
ea
624
S69
477
661
570
68s
LM
710
618
WI
786
648
639
694
040
Ma
M
768
I.-
t.004
944
1.161
1.007
1.-
1.a
1- 1.868
1.118
1.874
1.814
1.668
P.8P
¶.a6
1.m
a.w9
n7
m
111
168
m
an
as4
648
448
689
494
688
690
710
616
UI
684
761
U6
610
?%*
w
014
8n
l96
1.084
1.w
m
1.191
1.186
1.W4
IJn
1.4m
1.418
1.lM
1.007
lJIl
151s
1.718
2.4m
2101
t.148
:.tu
8.104
?as
8.m
Used
by
permission
of
the American Petroleum Institute, Production Department.
644
Drilling and Well Completions
(text
continued
from
page
631)
The required pump working pressure PWP (psi) can be calculated as
PWP
=
APs
+
APd
+
APa
+
AP,,
(4-35)
where
APs
=
pressure loss through surface equipment in psi
APd
=
pressure
loss
through the inside of the drill string in psi