epdf.pub_production-optimization-using-nodal-analysis-2nd-e[240-418]

Prévia do material em texto

Pressure Traverse Curves 231
LIQUID RATE, STBL/D: 1200
WATER FRACTION: 1
GAS GRAVITY: 0.65
OIL API GRAVITY: 35
WATER SPECIFIC GRAVITY: 1.07
AVERAGE FLOWING TEMP.,F: 150
5652484440
. TUBING SIZE, IN.: 1. 995
PRESSURE, 100 PSIG
20 24 28 32 36161284o O
1
2
3
4
5
6
7
8
" 9..
o
o
~10
o::
!i:ll
'"Q
12
13
14
15
16
17
18
19
20
232 Production Optimiza/ion Using Nadal Analysis
LIQUID RATE, STBL/D: 1200
WATER FRACTION: .5
GAS GRAVITY: 0.65
OIL API GRAVITY: 35
WATER SPECIFIC GRAVITY:. 1.07
AVERAGE FLOWING TEMP.,F: 150
5652484440
TUBING SIZE, IN.: 1. 995
PRESSURE, 100 PSIG
20 24 28 32 36161284o O
1
2
3
4
5
6
7
8
ó< 9..
o
o
~ 10
'"¡;:11.,
e
12
13
14
15
16
17
18
19
20
Pressure Traverse Curves 233
LIQUID RATE, STBL/D: 1200
WATER FRACTION: O
GAS GRAVITY: 0.65
OIL API GRAVITY: 35
WATER SPECIFIC GRAVITY: 1.07
AVERAGE FLOWING TEMP.,F: 150
5652484440
TUBING SIZE, IN.: 1.995
PRESSURE, 100 PSIG
20 24 28 32 36161284O O
1
2
3
4
5
6
7
8
8 9
""o
o
;: 10
'"~11
'""
12
13
14
15
16
17
18
19
20
234 Production Optimization Using Noda/ Ana/ysis
GAS GRAVITY: 0.65
OIL API GRAVITY: 35
WATER SPECIFIC GRAVITY' 1.07
AVERAGE FLOWING TEMP.,F: 150
TUBING SIZE, IN.: 2.441
LIQUID RATE, STBL!D: 100
5652464440
WATER FRACTION: 1
PRESSURE, 100 PSIG
20 24 26 32 36161264o O
1
2
3
4
5
6
7
6
E-< 9
'"o
o
;: 10
,
'"f;;11
'"Q
12
13
14
15
16
17
16
19
20
Pressure Traverse Curves 235
:H-I~Hjl+l¡tljjíttttthHH IIJI-I
GAS GRAVITY: 0.65
OIL API GRAVITY: 35
WATER SPECIFIC GRAVITY, 1.07
AVERAGE FLOWING TEMP.,F: 150
WATER FRACTION: .S
5652484440
TUBING SIZE, IN.: 2.441
LIQUID RATE, STBL/D: 100
PRESSURE, 100 PSIG
20 24 2B 32 36161284o O
1
2
3
4
5
6
7
8
E-< 9..
o
o.
~ 10
"'¡';11.,
Q
12
13
14
15
16
17
18
19
20
236 Production Optimiza/ion Using Nada! Analysis
LIQUID RATE, STBL/D: 100
GAS GRAVITY: 0.65
OIL API GRAVITY: 35
WATER SPECIFIC GRAVITY, 1.07
AVERAGE FLQWING TEMP.,F: 150
5652484440
TUBING SIZE, IN.: 2.441
WATER FRACTION: O
PRESSURE, 100 PSIG
20 24 28 32 36',161284o O
1
2
3
4
5
6
7
8
ó< 9..
o
o
~ 10
'"!i:u
'""
12
13
14
15
16
17
18
19
20
Pressure Traverse Curves 237
GAS GRAVITY: 0.65
OIL API GRAVITY: 35
WATER SPECIFIC GRAVITY:. 1.07
AVERAGE FLOWING TEMP.,F: 150
TUBING SIZE, IN.: 2.441
5652484440
LIQUIO RATE, STBL/O: 200
WATER FRACTION: 1
PRESSURE, 100 PSIG
20 24 28 32 36161284O O
1
2
3
4
5
6
7
8
8 9..
o
o
::: 10
'"t;::11.,
Q
12
13
14
15
16
17
18
19
20
238 Production Optimization Using Nodal Analysis
GAS GRAVITY: 0.65
OIL API GRAVITY: 35
WATER SPECIFIC GRAVITY,. 1.07
AVERAGE FLOWING TEMP.,F: 150
TUBING SIZE, IN.: 2.441
LIQUID RATE, STBL/D: 200
WATER FRACTION: .5
5652484440
PRESSURE, 100 PSIG
20 24 28 32 3616128o O 4
-1
2
3
4
5
6
7
8
".. 9r..
o
o
;: 10
"'!;:11
"''"
12
13
14
15
16
17
18
19
20
Pressure Traverse Curves 239
GAS GRAVITY: 0.65
OIL API GRAVITY: 35
WATER SPECIFIC GRAVITY:. 1.07
AVERAGE FLOWING TEMP.,F: 150
TUBING SIZE, IN.: 2.441
LIQUID RATE, STBL/D: 200
WATER FRACTION: O
5652484440
PRESSURE, 100 PSIG
20 24 28 32 36161284o O
1
2
3
4
5
6
7
8
.. 9..
o
o
~ 10
'"Íi:ll
""
12
13
14
15
16
17
18
19
20
240 Praduction Optimizatian Using Nodal Analysis
56524B4440
TUBING SIZE, IN.: 2.441
LIQUID RATE, STBL!D: 300
WATER FRACTION: 1
GAS GRAVITY: 0.65
OIL API GRAVITY: 35
WATER SPECIFIC GRAVITY:. 1.07
AVERAGE FLOWING TEMP.,F: 150
PRESSURE, 100 PSIG
20 24 2B 32 36161284o O
·1
2
3
4
5
6
7
B
.. 9..
o
o
;: 10
ti:
li:ll.,
'"
12
13
14
15
16
17
lB
19
20
Pressure Traverse Curves 241
GAS GRAVITY: 0.65
OIL API GRAVITY: 35
WATER SPECIFIC GRAVITY,. 1.07
AVERAGE FLOWING TEMP.,F: 150
TUBING SIZE, IN.: 2.441
5652484440
LIQUID RATE, STBL/D: 300
WATER FRACTION: .5
PRESSURE, 100 PSIG
20 24 28 32 36161284-Q O
1
2
3
4
5
6
7
8
,..
9
'"o
o
~ 10
"1;:11
"'Q
12
13
14
15
16
17
18
19
20
242 Production Optimization Using Nadal Analysis
GAS GRAVITY: 0.65
OIL API GRAVITY: 35
WATER SPECIFIC GRAVITY, 1.07
AVERAGE FLOWING TEMP.,F: 150
TUBING SIZE, IN.: 2.441
LIQUID RATE, STBL/D: 300
5652484440
WATER FRACTION: O
PRESSURE, 100 PSIG
20 24 28 32 36161284o O
1
2
3
4
5
6
7
8
E-< 9r..
o
o
~ 10
:x:
!;:11
"'Q
12
13
14
15
16
17
18
19
20
Pressure Traverse Curves 243
GAS GRAVITY: 0.65
OIL API GRAVITY: 35
WATER SPECIFIC GRAVITY,. 1.07
AVERAGE FLOWING TEMP.,F: 150
TUBING SIZE, IN.: 2.441
LIQUID RATE, STBL/D: 400
5652484440
WATER FRACTION: 1
PRESSURE, 100 PSIG
20 24 28 32 3612800. 4
1
2
3
4
5
6
7
8
&< 9..
o
o
;: 10
,
'"i.::ll.,
Q
12
13
14
15
16
17
18
19
20
244 Production Optimiza/ion Using Noda! Analysis
GAS GRAVITY: 0.65
OIL API GRAVITY: 35
WATER SPECIFIC GRAVITY, 1.07
AVERAGE FLOWING TEMP.,F: 150
TUBING SIZE, IN.: 2.441
5652484440
LIQUID RATE, STBL/D: 400
WATER FRACTION: .5
PRESSURE, 100 PSIG
20 24 28 32 36161284o O
1
2
3
4
5
6
7
8
.. 9..
o
o
;: 10
o:
a: 11
'"el
12
13
14
15
16
17
18
19
20
Pressure Traverse Curves 245
GAS GRAVITY: 0.65
OIL API GRAVITY: 35
WATER SPECIFIC GRAVITY, 1.07
AVERAGE FLOWING TEMP.,F: 150
TUBING SIZE, IN.: 2.441
LIQUID RATE, STBL/D: 400
WATER FRACTION: O
5652484440
PRESSURE, 100 PSIG
20 24 28 32 36161284o O
1
2
3
4
5
6
7
8
ó< 9..
o
o
~ 10
o:
~11
"'Q
12
13
14
15
16
17
18
19
20
246 Production Optimization Using Nodal Analysis
GAS GRAVITY: 0.65
OIL API GRAVITY: 35
WATER SPECIFIC GRAVITY: 1.07
AVERAGE FLOWING TEMP.,F: 150
TUBING SIZE, IN.: 2.441
5652484440
LIQUID RATE, STBL/D: 500
WATER FRACTION: 1
PRESSURE, 100 PSIG
16 ·20 24 28 32 361284O O
1
2
3
4
5
6
7
8
8 9..
o
o
;: 10
'"1;:11
'"Q
12
13
14
15
16
17
18
19
20
Pressure Traverse Curves 247
GAS GRAVITY: 0.65
OIL API GRAVITY:·35
WATER SPEC!FIC GRAVITY,. 1.07
AVERAGE FLOWING. TEMP.,F: 150
5652.484440
TUBING SIZE, IN.: 2.441
WATER FRACTION: .5
LIQUIO RATE, STBL/O: 500
PRESSURE, 100 PSIG
20 24 28 32 36161284o O
1
2
3
4
5
6
7
8
¡., 9..
o
o
;: 10
"'¡;:11
'"Q
12
13
14
15
16
17
18
19
20
248 Production Optimization Using Nadal Analysis
LIQUID RATE, STBL/D: 500
WATER FRACTION: O
56524844.40
TUBING SIZE, IN.: 2.441
GAS GRAVITY: 0.65
OIL API GRAVITY: 35
WATER SPECIFIC GRAVITY, 1.07
AVERAGE FLOWING TEMP.,F: 150
PRESSURE, 100 PSIG
20 24 28 32 36161284o O
1
2
3
4
5
6
7
8
E-< 9..
o
o
;: 10
'"1;:11
'""
12
13
14
15
16
17
18
19
20
Pressure Traverse Curves 249
GAS GRAVITY: 0.65
OIL API GRAVITY: 35
WATER SPECIFIC GRAVITY: 1.07
AVERAGE FLOWING TEMP.,F: 150
TUBING SIZE, IN.: 2.441
5652484440
LIQUID RATE, STBL/D: 600
WATER FRACTION: 1
PRESSURE, 100 PSIG
20 24 28 32 36161284O O
1
2
3
4
5
6
7
8
,..
9r..
o
o
~ 10
'"a: 11
'""
12
13
14
15
16
17
18
19
20
250 Production Optimiza/ion Using Nodal Analysis
GAS GRAVITY: 0.65
OIL API GRAVITY: 35
WATER SPECIFIC GRAVITY, 1.07
AVERAGE FLOWING TEMP.,F: 150
5652484440
TUBING SIZE, IN.: 2.441
LIQUID RATE, STBL/D: 600
WATER FRACTION: .5
PRESSURE, 100 PSIG
20 24 28 32 36161284o O
1
2
3
4
5
6
7
8
8 9..
o
o
~ 10
'"!i:11
'"Q
12
13
14
15
16
17
18
19
20
Pressure Traverse Curves 251
GAS GRAVITY: 0.65
OIL API GRAVITY: 35
WATER SPECIFIC GRAVITY, 1.07
AVERAGE FLOWING TEMP.,F: 150
TUBING SIZE, IN.:2.441
5652484440
LIQUID RATE, STBL/D: 600
WATER FRACTION: O
PRESSURE, 100 PSIG
20 24 28 32 3616128o O 4
1
2
3
4
5
6
7
8
.. 9..
o
o
;: 10
'"1;:11
"'Q
12
13
14
15
16
17
18
19
20
252
o
1
2
3
4
5
6
7
8
.. 9..
o
o
~ 10
,
o:
~11
"'Q
12
13
14
15
16
17
18
19
20
4 8 12 16
Production Optimiza/ion Using Nodal Analysis
PRESSURE, 100 PSIG
20 24 28 32 36
TUBING SIZE, IN.: 2.441
LIQUID RATE, STBL/D: 700
WATER FRACTION: 1
GAS GRAVITY: 0.65
OIL API GRAVITY: 35
WATER SPECIFIC GRAVITY: 1.07
AVERAGE FLOWING TEMP.,F: 150
Pressure Traverse Cur,¡es 253
GAS GRAVITY: 0.65
OIL API GRAVITY: 35
WATER SPECIFIC GRAVITY, 1.07
AVERAGE.FLOWING TEMP.,F: 150
TUBING SIZE, IN.:2.441
LIQUIO RATE, STBL!O: 700
WATER FRACTION: .5
5652484440
PRESSURE, 100 PSIG
20 24 28 32 36161284o O
1
2
3
4
5
6
7
8
.. 9..
o
o
~ 10
'"!i:u
'"'"
12
13
14
15
16
17
18
19
20
254 Production Optimization Using Noda! Analysis
5652484440
TUBING SIZE, IN.: 2.441
LIQUID RATE, STBL/D: 700
WATER FRACTIDN: O
GAS GRAVITY: 0.65
DIL API GRAVITY: 35
WATER SPECIFIC GRAVITY, 1.07
AVERAGE FLDWING TEMP.,F: 150
PRESSURE, 100 PSIG
20 24 28 32 36161284O
1
2
3
4
5
6
7
8
E-< 9..
o
o
~ 10
'"!i:11
'"c
12
13
14
15
16
17
18
19
20
Pressure Traverse Curves 255
PRESSURE, 100 PSIG
O
4 8 12 16 20 24 28 32 36 40 44 48 52 56
1
TUBING SIZE, IN. : 2.441
2 LIQUID RATE, STBL/D: 800
WATER FRACTION: 1
3
GAS GRAVITY: 0.65
4 OIL API GRAVITY: 35WATER SPECIFIC GRAVITY: 1. 07
AVERAGE FLOWING TEMP.,F: 150
5
6
7
8
,..
9..
o
o
;: 10
'"!i:ll
'"el
12
13
14
15
16
17
18
19
20 .. - - ..
256 Production Optimization Using Noda/ Analysis
GAS GRAVITY: 0.65
OIL API GRAVITY: 35
WATER SPECIFIC GRAVITY, 1.07
AVERAGE FLOWING TEMP.,F: 150
TUBING SIZE, IN.: 2.441
LIQUID RATE, STBL/D: 800
WATER FRACTION: .5
5652484440
PRESSURE, 100 PSIG
20 24 28 32 361284o
1
2
3
4
5
6
7
8
E-< 9..
o
o
~ 10
:c
!;;11
'""
12
13
14
15
16
17
18
19
20
Pressure Traverse Curves 257
GAS GRAVITY: 0.65
OIL API GRAVITY: 35
WATER SPECIFIC GRAVITY, 1.07
AVERAGE FLOWING TEMP.,F: 150
TUBING SIZE, IN.: 2.441
LIQUID RATE, STBL/D: 800
WATER FRACTION: O
o O
1
2
3
4
5
6
7
8
'" 9..
o
o
~ 10
'"!i:ll
"'el
12
13
14
15
16
17
18
19
20
4 8 12 16
PRESSURE, 100 PSIG
20 24 28 32 36 40 44 48 52 56
258 Production Optimiza/ion Using Nodal Analysis
PRESSURE, 100 PSIG
O
4 8 12 16 20 24 28 32 36 40 44 48 52 56
1
TUBING SIZE, IN. : 2.441
2 LIQUID RATE, STBL/D: 900
WATER FRACTION: 1
3
GAS GRAVITY: 0.65
4
OIL API GRAVITY: 35
WATER SPECIFIC GRAVITY: 1. 07
AVERAGE FLOWING TEMP.,F: 150
5
6
7
8
€o< 9..
o
o
~ 10
a:
!i:ll.,
Q
12
13
14
15
16
17
18
19
20 _. - - -
Pressure Traverse Curves 259
TUBING SIZE, IN.: 2.441
LIQUID RATE, STBL/D: 900
WATER FRACTION: .5
GAS GRAVITY: 0.65
OIL API GRAVITY: 35
WATER SPECIFIC GRAVITY, 1.07
AVERAGE FLOWING TEMP.,F: 150
PRESSURE, 100 PSIG
20. 24 28 32 36161284o O
1
2
3
4
5
6
7
8
ó< 9..
o
o
~ 10
-o:
!;;11
"'el
12
13
14
15
16
17
18
19
20
260 Production Optimization Using Nada! Ana/ysis
5652484440
TUBING SIZE, IN.: 2.441
LIQUID RATE, STBL/D: 900
WATER FRACTION: O
GAS GRAVITY: 0.65
OIL API GRAVITY: 35
WATER SPECIFIC GRAVITY, 1.07
AVERAGE FLOWING TEMP.,F: 150
PRESSURE, 100 PSIG
20 24 28 32 36161284o
1
2
3
4
5
6
7
8
E-< 9
'"o
o
::: 10
'"~11
"'"
12
13
14
15
16
17
18
19
20
Pressure Troverse Curves 261
LIQUID RATE, STBL/D: 1000
WATER FRACTION: 1
GAS GRAVITY: 0.65
OXL API GRAVITY: 35
WATER SPECIFIC GRAVITY, 1.07
AVERAGE FLOWING TEMP.,F: 150
5652484440
TUBING SIZE, IN.: 2.441
PRESSURE, 100 PSIG
20 24 28 32 36161284o O
1
2
3
4
5
6
7
.8
.. 9..
o
o
~ 10
'"¡;;U
"'"
12
13
14
15
16
17
18
19
20
262 Production Optimiza/ion Using Nodal Analysis
GAS GRAVITY: 0.65
OIL API GRAVITY: 35
WATER SPECIFIC GRAVITY: 1.07
.AVERAGE FLOWING TEMP.,F: 150
TUBING SIZE, IN.: 2.441
LIQUID RATE, STBL/D: 1000
WATER FRACTION: .5
5652484440
PRESSURE, 100 PSIG
20 24 28 32 36161284o O
1
2
3
4
5
6
7
8
8 9
'"o
o
~ 10
o:
li:ll
'"Cl
12
13
14
15
16
17
18
19
20
Pressure Traverse Curves 263
5652484440
GAS GRAVITY: 0.65
OIL API GRAVITY: 35 .
WATER SPECIFIC GRAVITY: 1.07
AVERAGE FLOWING TEMP.,F: 150
TUBING SIZE, IN.: 2.441
LIQUID RATE, STBL/D: 1000
WATER FRACTION: O
PRESSURE, 100 PSIG
20 24 28 32 3616128o O 4
1
2
3
4
5
6
7
8
... 9..
o
o
~ 10
"'!;:11
'"e
12
13
14
15
16
17
18
19
20
264 Production Optimization Using Nodal Analysis
TUBING SIZE, IN.: 2.441
40
LIQUID RATE, STBL/D: 1200
WATER FRACTION: 1
,
GAS GRAVITY: 0.65
OIL API GRAVITY: 35
WATER SPECIFIC GRAVITY: 1.07
AVERAGE FLOWING TEMP.,F: 150
PRESSURE, 100 PSIG
20 24 28 32 36161284OO
1
2
3
4
5
6
7
8
« 9..
o
o
~ 10
:e
¡;;11.,
Q
12
13
14
15
16
17
18
19
20
Pressure Traverse Curves 265
56524B4440
WATER FRACTION: .5
GAS GRAVITY: 0.65
OIL API GRAVITY: 35
WATER SPECIFIC GRAVITY, 1.07
AVERAGE FLQWING TEMP.,F: 150
LIQUID RATE, -STBL/D: 1200
TUBING SIZE, IN.: 2.441
PRESSURE, 100 PSIG
20 24 2B 32 361612B4o
1
2
3
4
5
6
7
B
« 9
'"o
o
~ 10
"'¡;;11
"'Q
12
13
14
15
16
17
lB
19
20
266 Production Optimization Using Nadal Analysis
5652484440
GAS GRAVITY: 0.65
OIL API GRAVITY: 35
WATER SPECIFIC GRAVITY, 1.07
AVERAGE FLOWING TEMP.,F: 150
TUBING SIZE, IN.: 2.441
LIQUID RATE, STBL/D: 1200
WATER FRACTION: O
PRESSURE, 100 PSIG
20 24 28 32 36161284o o
1
2
3
4
5
6
7
·8
E-< 9¡.,
o
o
~ 10
'"l;:11
'"Q
12
13
14
15
16
17
18
19
20
Pressure Traverse Curves 267
LIQUID RATE, STBL/O: 1500
WATER FRACTION: 1
5652484440
TUBING SIZE, IN.: 1. 995
GAS GRAVITY: 0.65
OIL API GRAVITY: 35 .
WATER SPECIFIC GRAVITY, 1.07
AVERAGE FLOWING TEMP.,F: 150
PRESSURE, 100 PSIG
20 24 28 32 36161284o O
1
2
3
4
5
6
7
8
E-< 9
'"
""~ 10
:c
!i:1l
'""
12
13
14
15
16
17
18
19
20
268 Production Optirnization Using Nadal Analysis
5652484440
---t.--- -j-
TUBING SIZE, IN.: 1. 995
LIQUID RATE, STBL!D: 1500
WATER FRACTION: .5
GAS GRAVITY: 0.65
OIL API GRAVITY: 35
WATER SPECIFIC GRAVITY, 1.07
AVERAGE FLOWING TEMP.,F: 150
PRESSURE, 100 PSIG
20 24 28 32 36161284o O
1
2
3
4
5
6
7
8
E-< 9..
o
o
;: 10
"'~11
'"Q
12
13
14
15
16
17
18
19
20
Pressure Traverse Curves 269
5652484440
LIQUID RATE, STBL/D: 1500
WATER FRACTION: O
GAS GRAVITY: 0.65
OIL API GRAVITY: 35
WATER SPECIFIC GRAVITY, 1.07
AVERAGE FLOWING TEMP.,F: 150
TUBING SI ZE, IN.: 1. 995
PRESSURE, 100 PSIG
20 24 28 32 36161284o O
1
2
3
4
5
6
7
8
.. 9..
o
o
~ 10
"~ 11
'"Cl
12
13
14
15
16
17
18
19
20
270 Production Optimizatían Using Nodal Ana/ysis
GAS GRAVITY: 0.65
OIL API GRAVITY: 35
WATER SPECIFIC GRAVITY, 1.07
AVERAGE FLOWING TEMP.,F: 150
5652484440
TUBING SIZE, IN.: 2.441
LIQUID RATE, STBL/D: 2000
WATER FRACTION: 1
PRESSURE, 100 PSIG
20 24 28 32 3616128o O 4
1
2
3
4
5
6
7
8
.. 9..
o
o
~10
'"5::11
"Q
12
13
14
15
16
17
18
19
20
Pressure Traverse Curves 271
GAS GRAVITY: 0.65
OIL API GRAVITY: 35
WATER SPECIFIC GRAVITY, 1.07
AVERAGE FLOWING TEMP.,F: 150
TUBING SIZE, IN.: 2.441
LIQUID RATE, STBL/D: 2000
WATER FRACTION: .5
5652484440
PRESSURE, 100 PSIG
20· 24 28 32 36161284o O
1
2
3
4
5
6
7
8
E-< 9..
o
o
;: 10
'"f;:11
'"el
12
13
14
15
16
17
18
19
20
272 Production Optimization Us;ng Nodal Ana(vsis
GAS GRAVITY: 0.65
OIL API GRAVITY: 35
WATER SPECIFIC GRAVITY; 1.07
AVERAGE FLOWING TEMP.,F: 150
TUBING SIZE, IN.: 2.441
LIQUID RATE, STBL/D: 2000
WATER FRACTION: O
5652484440
PRESSURE, 100 PSIG
20 24 28 32 36161284o O
1
2
3
4
5
6
7
8
.. 9..
o
o
~ 10
'"~1l
fil
Cl
12
13
14
15
16
17
18
19
20
Pressure Traverse Curves 273
,
5652484440
LIQUID RATE, STBL/D: 2500
WATER FRACTION: 1
GAS GRAVITY: 0.65
OIL API GRAVITY: 35
WATER SPECIFIC GRAVITY: 1.07
AVERAGE FLOWING TEMP.,F: 150
TUBING SIZE, IN.: 2.441
PRESSURE, 100 PSIG
20 24 28 32 3616128O O 4
1
2
3
4
5
6
7
8
.. 9..
o
o
~ 10
'"~11
'""
12
13
14
15
16
17
18
19
20
274 Production Optimiza/ion Using Nadal Analysis
LIQUID RATE, STBL/D: 2500
WATER FRACTION: .5
GAS GRAVITY: 0.65
OIL API GRAVITY: 35
WATER SPECIFIC GRAVITY,. 1.07
AVERAGE FLOWING TEMP.,F: 150
TUBING SIZE, IN.: 2.441
5652484440
PRESSURE, 100 PSIG
20 24 28 32 36161284O O
·1
2
3
4
5
6
7
8
.. 9
""o
o
~ 10
"'~11
'"Q
12
13
14
15
16
17
18
19
20
Pressure Traverse Curves 275
LIQUID RATE, STBL/D: 2500
WATER FRACTION: O
GAS GRAVITY: 0.65
OIL API GRAVITY: 35
WATER SPECIFIC GRAVITY:_ 1.07
AVERAGE FLOWING TEMP.,F: 150
5652484440
TUBING SIZE, IN.: 2.441
PRESSURE, 100 PSIG
20 24 28 32 36161284o O
1
2
3
4
5
6
7
8
E-< 9..
o
o
;: 10"'!;:11
"'Q
12
13
14
15
16
17
18
19
20
276 Production Optimization Using Noda! Ana/ysis
TUBING SIZE, IN.:2.441
LIQUID RATE, STBL/D: 3000
WATER FRACTION: 1
GAS GRAVITY: 0.65
OIL API GRAVITY: 35
WATER SPECIFIC GRAVITY, 1.07
AVERAGE FLOWING TEMP.,F: 150
PRESSURE, 100 PSIG
20 24 28 32 36161284o O
1
2
3
4
5
6
7
8
.. 9f«
o
o
~ 10
:I:
¡;:11
'"Q
12
13
14
15
16
17
18
19
20
Pressure Traverse Curves 277
LIQUID RATE, STBL/D: 3000
4440
WATER FRACTION: .5
GAS GRAVITY: 0.65
OIL.API GRAVITY: 35
WATER SPECIFIC GRAVITY. 1.07
AVERAGE FLOWING TEMP.,F: 150
TUBING SIZE, IN.: 2.441
PRESSURE, 100 PSIG
20 24 28 32 36161284o
1
2
3
4
5
6
7
8
&< 9
'"
o
o
~ 10
"!i:ll
"'o
12
13
14
15
16
17
18
19
20
278
o
1
2
3
4
5
6
7
8
.. 9..
o
o
~ 10
o:
f;:11
'""
12
13
14
15
16
17
18
19
20
8 12 16
Production Optimization Using Nadal Analysis
PRESSURE, 100 PSIG
20 24 28 32 36
TUBING SIZE, IN.: 2.441
LIQUID RATE, STBL/D: 3000
WATER FRACTION: O
GAS GRAVITY: 0.65
OIL API GRAVITY: 35
WATER SPECIFIC GRAVITY, 1.07
AVERAGE FLOWING TEMP.,F: 150
Pressure Traverse Curves 279
GAS GRAVITY: 0.65
OIL API GRAVITY: 35
WATER SPECIFIC GRAVITY: 1.07
AVERAGE FLOWING TEMP.,F: 150
TUBING SIZE, IN.: 2.992
LIQUID RATE, STBL/D: 300
WATER FRACTION: 1
o O
1
2
3
4
5
6
7
8
.. 9..
o
o
~10
'"Íi:ll
'""
12
13
14
15
16
17
18
19
20
4 8 12 16
PRESSURE, 100 PSIG
20 24 28 32 36 40 44 48 52 56
280 Production Optimiza/ion Using Nadal Analysis
LIQUID RATE, STBL!D: 300
WATER FRACTION: .5
GAS GRAVITY: 0.65
OIL API GRAVITY: 35
WATER SPECIFIC GRAVITY: 1.07
AVERAGE FLOWING TEMP.,F: 150
TUBING SIZE, IN.: 2.992
5652464440
PRESSURE, 100 PSIG
20 24 28 32 36161264o O
1
2
3
4
5
6
7
8
E-< 9...
o
o
~ 10
'"I;:il
'"O
12
13
14
15
16
17
16
19
20
Pressure Traverse Curves 281
TUBING SIZE, IN.: 2.992
LIQUID RATE, STBL!D: 300
WATER FRACTION: O
4440
GAS GRAVITY: 0.65
OIL API GRAVITY: 35
WATER SPECIFIC GRAVITY, 1.07
AVERAGE FLOWING TEMP.,F: 150
PRESSURE, 100 PSIG
20 24 28 32 36161284o O
1
2
3
4
5
6
7
8
E< 9
'"o
o
~ 10
,
'"¡;;11
"''"
12
13
14
15
16
17
18
19
20
282 Production Optimiza/ion Using Nadal Analysis
LIQUID RATE, STBL!D: 500
WATER FRACTION: 1
GAS GRAVITY: 0.65
OIL API GRAVITY: 35
WATER SPECIFIC GRAVITY:. 1.07
AVERAGE FLOWING TEMP.,F: 150
TUBING SIZE, IN.: 2.992
5652484440
PRESSURE, 100 PSIG
20 24 28 32 36161284o O
1
2
3
4
5
6
7
8
... 9".
o
o
~10
'"1;;11
'"el
12
13
14
15
16
17
18
19
20
Pressure Traverse Curves 283
GAS GRAVITY: 0.65
OIL API GRAVITY: 35
WATER SPECIFIC GRAVITY; 1.07
AVERAGE FLOWING TEMP.,F: 150
TUBING SIZE, IN.: 2.992
LIQUID RATE, STBL/D: SOO
WATER FRACTION: .S
o O
1
2
3
4
5
6
7
8
E-< 9..
o
o
::: 10
'"!i:ll
"'a
12
13
14
15
16
17
18
19
20
4 8 12 16
PRESSURE, 100 PSIG
20 24 28 32 36 40 44 48 52 56
284 Produclion Optimiza/ion Using Noda/ Analysis
LIQUID RATE, STBL/D: 500
WATER FRACTION: O
GAS GRAVITY: 0.65
OIL API GRAVITY: 35
WATER SPECIFIC GRAVITY, 1.07
AVERAGE FLOWING TEMP.,F: 150
5652484440
TUBING SIZE, IN.: 2.992
PRESSURE, 100 PSIG
20 24 28 32 36161284o O
1
2
3
4
5
6
7
8
E-< 9..
o
o
~ 10
'"~ll
'"Cl
12
13
14
15
16
17
18
19
20
Pressure Traverse Curves 285
GAS GRAVITY: 0.65
OIL API GRAVITY: 35
WATER SPECIFIC GRAVITY, 1.07
AVERAGE FLOWING TEMP.,F: 150
TUBING SIZE, IN.: 2.992
LIQUID RATE, STBL/D: 7DO
WATER FRACTION: 1
o O
1
2
3
4
5
6
7
8
E-< 9
'"'o
o
~ 10
,
'"f;:11
"'e
12
13
14
15
16
17
18
19
20
4 8 12 16
PRESSURE, 100 PSIG
20 24 28 32 36 40 44 48 52 56
286 Production Optimiza/ion Using Nada! Analysis
LIQUID RATE, STBL/D: 700
WATER FRACTION: .5
GAS GRAVITY: 0.65
OIL API GRAVITY: 35
WATER SPECIFIC GRAVITY,- 1.07
AVERAGE FLOWING TEMP.,F: 150
5652484440
TUBING SIZE, IN.: 2.992
PRESSURE, 100 PSIG
20 24 28 32 36161284o O
1
2
3
4
5
6
7
8
E-< 9..
o
o
~ 10
"'a: 11.,
o
12
13
14
15
16
17
18
19
20
Pressure Troverse Curves 287
GAS GRAVITY: 0.65
DIL API GRAVITY: 35
WATER SPECIFIC GRAVITY,. 1.07
AVERAGE FLDWING TEMP.,F: 150
TUBING SIZE, IN.: 2.992
LIQUID RATE, STBL/D: 700
WATER FRACTIDN: O
5652484440
PRESSURE, 100 PSIG
20 24 28 32 36161284o O
1
2
3
4
5
6
7
8
E-< 9r..
o
o
~ 10
'"~11
'"Q
12
13
14
15
16
17
18
19
20
288 Production Optimization Using Nada! Analysis
GAS GRAVITY: 0.65
OIL API GRAVITY: 35
WATER SPECIFIC GRAVITY: 1.07
AVERAGE FLOWING TEMP.,F: 150
TUBING SIZE, IN.: 2.992
LIQUID RATE, STBL/D: 900
WATER FRACTION: 1
o O
1
2
3
4
5
6
7
8
.. 9..
o
o
~ 10
tI:
!i;1l.,
Q
12
13
14
15
16
17
18
19
20
4 8 12 16
PRESSURE, 100 PSIG
20 24 28 32 36 40 44 48 52 56
Pressure Traverse Curves 289
LIQUID RATE, STBL/D: 900
WATER FRACTION: .5
GAS GRAVITY: 0.65
OIL API GRAVITY: 35
WATER SPECIFIC GRAVITY,. 1.07
AVERAGE FLOWING TEMP.,F: 150
TUBING SIZE, IN.: 2.992
5652484440
PRESSURE, 100 PSIG
20 24 28 32 36161284o O
1
2
3
4
5
6
7
8
8 9..
o
o
~ 10
,
:z:
~11
"'",.
12
13
14
15
16
17
18
19
20
290 Production Optimization Using Nada! Analysis
TUBING SIZE, IN.: 2.992
LIQUID RATE, STBL/D: 900
52 . 56484440
WATER FRACTION: O
GAS GRAVITY: 0.65
OIL API GRAVITY: 35
WATER SPECIFIC GRAVITY:. 1.07
AVERAGE FLOWING TEMP.,F: 150
PRESSURE, 100 PSIG
20 24 28 32 36161284o O
1
2
3
4
5
6
7
8
E-< 9r..
o
o
~ 10
:z:
!l:11
'"e
12
13
14
15
16
17
18
19
20
Pressure Traverse Curves 291
LIQUID RATE, STBL/D: 1000
WATER FRACTION: 1
GAS GRAVITY: 0.65
OIL API GRAVITY: 35
WATER SPECIFIC GRAVITY,. 1.07
AVERAGE FLOWING TEMP.,F: 150
5652464440
TUBING SIZE, IN.: 2.992
PRESSURE, 100 PSIG
20· 24 26 32 36161264o O
1
2
3
4
5
6
7
6
O< 9...
o
o
~ 10
'"¡;:11
'"Q
12
13
14
15
16
17
16
19
20
292 Production Optimization Using Nodal Analysis
GAS GRAVITY: 0.65
OIL API GRAVITY: 35
WATER SPECIFIC GRAVITY:. 1.07
AVERAGE FLOWING TEMP.,F: 150
TUBING .SIZE, IN.: 2.992
LIQUID RATE, STBL/D: 1000
WATER FRACTION: .5
5652484440
PRESSURE, 100 PSIG
20 24 28 32 3616128o O 4
1
2
3
4
5
6
7
8
.. 9
"'o
o
~ 10
"!i:ll
'"Q
12
13
14
15
16
17
18
19
20
Pressure Traverse Curves 293
WATER FRACTION: O
LIQUID RATE, STBL/D: 1000
5652484440
GAS GRAVITY: 0.65
OIL API GRAVITY: 35
WATER SPECIFIC GRAVITY:. 1.07
AVERAGE FLOWING TEMP.,F: 150
TUBING·SIZE, IN.: 2.992
PRESSURE, 100 PSIG
20 24 28 32 36161284o O
·1
2
3
4
5
6
7
8
.. 9..
o
o
~ 10
"'!i:u.,
el
12
13
14
15
16
17
18
19
20
294 Production Optimization Using Noda! Analysis
GAS GRAVITY: 0.65
OIL API GRAVITY: 35
WATER SPECIFIC GRAVITY, 1.07
AVERAGE FLOWING TEMP.,F: 150
TUBING SIZE, IN.: 2.992
LIQUID RATE, STBL/D: 1200
WATER FRACTION: 1
o O
1
2
3
4
5
6
7
8
E-< 9
'"o
o
~ 10
'"¡¡:11
'"e
12
13
14
15
16
17
18
19
20
4 8 12 16
PRESSURE, 100 PSIG
20 24 28 32 36 40 44 48 52 56
Pressure Traverse Curves 295
GAS GRAVITY: 0.65
OIL API GRAVITY: 35
WATER SPECIFIC GRAVITY:. 1.07
AVERAGE FLOWING TEMP.,F: 150
TUBING SIZE, IN.: 2.992
LIQUID RATE, STBL/D: 1200
WATER FRACTIDN: .5
o
1
2
3
4
5
6
7
8
.. 9
'"o
o
~ 10
'"!;;1l
'"Q
12
13
14
15
16
17
18
19
20
4 8 12 16
PRESSURE, 100 PSIG
20 24 28 32 36 40 44 48 52 56
296 Production Optimiza/ion Using Nadal Analysis
LIQUID RATE, STBL/D: 1200
WATER FRACTION: O
5652484440
GAS GRAVITY: 0.65
OIL API GRAVITY: 35
WATER SPECIFIC GRAVITY,. 1.07
AVERAGE FLOWING TEMP.,F: 150
TUBING SIZE, IN.: 2.992
PRESSURE, 100 PSIG
20 24 28 32 3616128O O 4
1
2
3
4
5
6
7
8
E-< 9..
o
o
~ 10
"'!i:ll
'""
12
13
14
15
16
17
18
19
20
Pressure Traverse Curves 297
GAS GRAVITY: 0.65
OIL API GRAVITY: 35
WATER SPECIFIC GRAVITY: 1.07
AVERAGE FLOWING TEMP.,F: 150
TUBING SIZE, IN.: 2.992
LIQUID RATE, STBL/D: 1500
WATER FRACTION: 1
o O
1
2
3
4
5
&
7
8
E-< 9
'"o
o
~ 10
"'1;:11
'""
12
13
14
15
16
17
18
19
20
4 8 12 16
PRESSURE, 100 PSIG
20 24 28 32 36 40 44 48 52 56
298 Production Optimization Using Nadal Ana/ysis
WATER FRACTION: .5
TUBING SIZE, IN.:2.992
LIQUID RATE, STBL/D: 1500
GAS GRAVITY: 0.65
OIL API GRAVITY: 35
WATER SPECIFIC GRAV¡TY:. 1.07
AVERAGE FLOWING TEMP.,F: 150
5652484440
PRESSURE, 100 PSIG
20 24 28 32 36161284o O
1
2
3
4
5
6
7
8
ó< 9'"
o.
o
;: 10
"i;:11.,
"
12
13
14
15
16
17
18
19
20
Pressure Traverse Curves 299
GAS GRAVITY: 0.65
OIL API GRAVITY: 35
WATER SPECIFIC GRAVITY:. 1.07
AVERAGE FLOWING TEMP.,F: 150
TUBING SIZE, IN.: 2.992
LIQUID RATE, STBL/D: 1500
WATER FRACTION: O
5652484440
PRESSURE, 100 PSIG
20 24 28 32 36161284o O
1
2
3
4
5
6
7
8
E-< 9r..
o
o
~10
o:
tu
"'"
12
13
14
15
16
17
18
19
20
300 Production Optimization Using Nodal Ana/ysis
GAS GRAVITY: 0.65
OIL API GRAVITY: 35
WATER SPECIFIC GRAVITY: 1.07
AVERAGE FLOWING TEMP.,F: 150
TUBING SIZE, IN.: 2.992
LIQUID RATE, STBL!D: 2000
WATER FRACTION: 1
5652484440
PRESSURE, 100 PSIG
20 24 28 32 36161284O O
1
2
3
4
5
6
7
8
.. 9..
o
o
~ 10
'"ii:1l
'"e
12
13
14
15
16
17
18
19
20
Pressure Traverse Curves 301
GAS GRAVITY: 0.65
OIL API GRAVITY: 35
WATER SPECIFIC GRAVITY,. 1.07
AVERAGE FLOWING TEMP.,F' 150
TUBING SIZE, IN.: 2.992
LIQUID RATE, STBL/D: 2000
WATER FRACTION: .5
5652484440
PRESSURE, 100 PSIG
20 24 28 32 36161284O O
1
2
3
4
5
6
7
8
E< 9
"'o
o
;: la
"'1;;11
"'e
12
13
14
15
16
17
18
19
20
302 Production Optimization Using Nadal Analysis
GAS GRAVITY: 0.65
OIL API GRAVITY: 35
WATER SPECIFIC GRAVITY, 1.07
AVERAGE FLOWING TEMP.,F: 150
TUBING SIZE, IN.: 2.992
LIQUIO RATE, STBL/O: 2000
WATER FRACTION: O
5652484440
PRESSURE, 100 PSIG
20 24 28 32 36161284o O
1
2
3
4
5
6
7
8
E-< 9[<,
o
o
~ 10
'"~11
'"Q
12
13
14
15
16
17
18
19
20
Pressure Traverse Curves 303
GAS GRAVITY: 0.65
OIL API GRAVITY: 35
WATER SPECIFIC GRAVITY,_ 1.07
AVERAGE.FLOWING TEMP.,F: 150
TUBING SIZE, IN.: 2.992
LIQUID RATE, STBL/D: 3000
WATER FRACTION: 1
5652484440
PRESSURE, 100 PSIG
20 24 28 32 36161284O O
1
2
3
4
5
6
7
8
" 9..
o
o
~ 10
'"a; 11
'"o
12
13
14
15
16
17
18
19
20
304 Production Optimization Using Nadal Analysis
GAS GRAVITY: 0.65
OIL API GRAVITY: 35
WATER SPECIFIC GRAVITY, , 1.07
AVERAGE FLOWING TEMP.,F: 150
TUBING SIZE, IN.: 2.992
LIQUID RATE, STBL/D: 3000
WATER FRACTION: .5
o O
'1
2
3
4
5
6
7
8
8 9r..
o
o
;: 10
'"~11
'"Q
12
13
14
15
16
17
18
19
20
4 8 12 16
PRESSURE, 100 PSIG
20 24 28 32 36 40 44 48 5'2 56
GAS GRAVITY: 0.65
OIL API GRAVITY: 35
WATER SPECIFIC GRAVITY:. 1.07
AVERAGE FLOWING TEMP.,F: 150
TUBING SIZE, IN.: 2.992
LIQUID RATE, STBL/D: 3000
WATER FRACTION: O
Pressure Traverse Curves
O O
1
2
3
4
5
6
7
8
.. 9..
o
o
~ 10
"!i:ll
'""
12
13
14
15
16
17
18
19
20
16
PRESSURE, 100 PSIG
20 24 28 32 36 40 44 48 52 56
305
306 Production Optimization Using Nadal Analysis
GAS GRAVITY: 0.65
OIL API GRAVITY: 35
WATER SPECIFIC GRAVITY,. 1.07
AVERAGE FLOWING TEMP.,F: 150
TUBING SIZE, IN.: 2.992
LIQUID RATE, STBL/D: 4000
WATER FRACTION: 1
5652484440
PRESSURE, 100 PSIG
20 24 28 32 36H1284o O
·1
2
.3
4
5
6
7
8
¡.< 9..
o
o
~ 10
tI:
~ 11
'"a
12
13
14
15
16
17
18
19
20
Pressure Traverse Curves 307
GAS GRAVITY: .0.65
OIL API GRAVITY: 35
WATER SPECIFIC GRAVITY,.1.07
AVERAGE FLOWING TEMP.,F: 150
TUBING SIZE, IN.: 2.992
LIQUID RATE, STBL/D: 4000
WATER FRACTION: .5
1
2
3
4
5
6
7
8
E-< 9..
o
o
~ 10
'"i;::11
'""
12
13
14
15
16
17
18
19
20
4 8 12 16
PRESSURE, 100 PSIG
20 24 28 32 36 40 44 48 52 56
308 Production Optimiza/ion Using Nada! Analysis
O O 4 8 12 16
PRESSURE, 100 PSIG
20 24 28 32 36 40 44 48 52 56
1
mi2
3
4
5
~
6
7 1
8 ti
O< 9..
o
o
~ 10
tI:
~11
'"Q
12
13
14
15
16
17
18
19
20
TUBING SIZE, IN.: 2.992
LIQUID RATE, STBL/D: 4000
WATER FRACTION: O
GAS GRAVITY: 0.65
OIL API GRAVITY: 35
WATER SPECIFIC GRAVITY; 1.07
AVERAGE FLOWING TEMP.,F: 150
-1+
Pressure Traverse Curves 309
GAS GRAVITY: 0.65
OIL API GRAVITY: 35
WATER SPECIFIC GRAVITY,. 1.07
AVERAGE FLOWING TEMP.,F: 150
TUBING SIZE, IN.: 3.958
LIQUID RATE, STBL/D: 500
WATER FRACTION:
565248
1
4440
PRESSURE, 100 PSIG
20 24 28 32 36161284o O
1
2
3
4
5
6
7
8
E-< 9r..
o
o
;: 1~
tI:
¡;;1l.,
"
12
13
14
15
16
17
18
19
20
310 Production Optimization Using Noda/ Analysis
GAS GRAVITY: 0.65
OIL API GRAVITY: 35
WATER SPECIFIC GRAVITY:.l.07
AVERAGE FLOWING TEMP.,F: 150
TUBING SIZE, IN.: 3.958
LIQUID RATE, STBL/D: sao
WATER FRACTION: .5
O O
1
2
3
4
5
6
7
8
¡.. 9..
o
o
~ 10
"'!i: 11
"'Q
12
13
14
15
16
17
18
19
20
4 8 12 16
PRESSURE, 100 PSIG
20 24 28 32 36 40 44 48 . 52 56
Pressure Traverse Curves 311
GAS GRAVITY: 0.65
DIL APIGRAVITY: 35
WATER SPECIFIC GRAVITY:. 1.07
AVERAGE FLOWING TEMP.,F: 150
TUBING SIZE, IN.: 3.958
LIQUID RATE, STBL/D: 500
WATER FRACTION: O
5652484440
P~ESSURE, 100 PSIG
20 24 28 32 36161284o O
1
2
3
4
5
6
7
8
E-< 9..
o
o
~ 10
o:
t;11.,
el
12
13
14
15
16
17
18
19
20
312 Production Optimization Using Nodal Analysis
LIQUID RATE, STBL/D: 800
GAS GRAVITY: 0.65
DIL API GRAVITY: 35
WATER SPECIFIC GRAVITY:. 1.07
AVERAGE FLOWING TEMP.,F: 150
5652484440
TUBING SIZE, IN.: 3.958
WATER FRACTIDN: 1
PRESSURE, 100 PSIG
20 24 28 32 36161284o O
1
2
3
4
5
6
7
8
&< 9..
o
o
~ 10
tI:
~1l
'"Q
12
13
14
15
16
17
18
19
20
Pressure Traverse Curves 313
LIQUID RATE, STBL/D: 800
WATER FRACTION: .5
GAS GRAVITY: 0.65
OIL API GRAVITY: 35
WATER SPECIFIC GRAVITY' 1.07
AVERAGE FLOWING TEMP.,F: 150
5652484440
TUBING SIZE, IN.: 3.958
PRESSURE, 100 PSIG
20 24 28 32 36161284o O
1
2
3
4
5
6
7
8
8 9..
o
o
~ 10
'"~11
"'"
12
13
14
15
16
17
18
19
20
i14 Production Optirnization Using Noda! Analysis
GAS GRAVITY: 0.65
OIL API GRAVITY: 35
WATER SPECIFIC GRAVITY,_ 1.07
AVERAGE FLOWING TEMP"F: 150
TUBING SIZE, IN.: 3.95B
LIQUID RATE, STBL/D: BOa
WATER FRACTION: O
56524840· 44
PRESSURE, 100 PSIG
20 24 28 32 3616128o o 4
1
2
3
4
5
6
7
8
E-< 9..
o
o
~ 10
'"~11
'""
12
13
14
15
16
17
18
19
20
Pressure Traverse Curves 315
48 52 564440
GAS GRAVITY: 0.65
OIL API GRAVITY: 35
WATER SPECIFIC GRAVITY: 1.07
AVERAGE FLOWING TEMP.,F: 150
TUBING SIZE, IN.:3.958
LIQUID RATE, STBL/D: 1000
WATER FRACTION: 1
PRESSURE, 100 PSIG
12 16 20 24 28 32 36B4
201111111111111111111111111 tül1llJ't ¡I 1'11 le-tu L1J" UU l±ti 1I LJ 1I1sIILL I tfi;tl
o O
1
2
3
4
5
6
7
8
E-< 9
'"o
o
;: 10
'"[;;11.,
el
12
13
14
15
16
17
18
19
316 Production Optimiza/ion Using Nodal Analysis
GAS GRAVITY: 0.65
OIL API GRAVITY: 35
WATER SPECIFIC GRAVITY,. 1.07
AVERAGE FLOWING TEMP.,F: 150
TUBING SIZE, IN.:3.9S8
LIQUID RATE, STBL/D: 1000
WATER FRACTION: .5
5652484440
PRESSURE, 100 PSIG
20 24 28 32 36161284o O
1
2
3
4
5
6
7
8
E-< 9..
o
o
~ 10
o:
f;:11
'""
12
13
14
15
16
17
18
19
20
Pressure Traverse Curves 317
GAS GRAVITY: 0.65
OIL API GRAVITY, 35
WATER SPECIFIC GRAVITY: 1.07
AVERAGE FLOWING TEMP.,F: 150
5652484440
TUBING SIZE, IN., 3.958
LIQUID RATE, STBL/D: 1000
WATER FRACTION, O
PRESSURE, 100 PSIG
20 24 28 32 361612840.0
1
2
3
4
5
6
7
8
E-< 9i><
o
o
;: 10
tI:
¡;:11
'""
12
13
14
15
16
17
18
19
20
318 Production Optimization Using Nadal Ana/ysis
GAS GRAVITY: 0.65
OIL API GRAVITY: 35
WATER SPECIFIC GRAVITY: 1.07
AVERAGE FLOWING TEMP.,F: 150
TUBING SIZE, IN.: 3.958
LIQUID RATE, STBL/D:
5652
1500
48
1
4440
WATER FRACTION:
PRESSURE, 100 PSIG
20 24 28 32 36161284o
1
2
3
4
5
6
7
8
'" 9O<
o
o
~ 10
'"Z;:11
'""
12
13
14
15
16
17
18
19
··20·
Pressure Traverse Curves 319
GAS GRAVITY: 0.65
OIL API GRAVITY, 35
WATER SPECIFIC GRAVITY: 1.07
AVERAGE FLOWING TEMP.,F: 150
TUBING SIZE, IN.: 3.958
5652
1500
484440
LIQUID RATE, STBL/D:
WATER FRACTION: .5
PRESSURE, 100 PSIG
20 24 28 32 36161284o O
1
2
3
4
5
6
7
8
« 9..
""
~ 10
'"fi:ll
"'"
12
13
14
15
16
17
18
19
20
320 Produclion Optimiza/ion Using Nada/ Ana/ysis
GAS GRAVITY: 0.65
OIL API GRAVITY: 35
WATER SPECIFIC GRAVITY,1.07
AVERAGE FLOWING TEMP.,F: 150
TUBING SIZE, IN.: 3.958
LIQUID RATE, STBL!D: 1500
WATER FRACTION: O
o O 4
1
2
3
4
5
6
7
6
E-< 9..
o
o
~ 10
'"¡;;11.,
el
12
13
14
15
16
17
16
19
20
6 12 16
PRESSURE, 100 PSIG
20 24 26 32 36 40
-1
44 46 52 56
-1
Pressure Traverse Curves 321
GAS GRAVITY: 0.65
OIL API GRAVITY: 35
WATER SPECIFIC GRAVITY: 1.07
AVERAGE FLOWING TEMP.,F: 150
TUBING SIZE, IN.: 3.958
LIQUID RATE, STBL/D:
5652
2000
48
1
4440
WATER FRACTION:
PRESSURE, 100 PSIG
20 24 28 32 36161284o O
1
2
3
4
5
6
7
8
.. 9
'"o
o
~ 10
'"¡;: 11.,
"
12
13
14
15
16
17
18
19
20
322 Production Optimiza/ion Using Nadal Analysis
TUBING SIZE, IN.: 3.956
LIQUID RATE, STBL/D: 2000
GAS GRAVITY: 0.65
OIL API GRAVITY: 35
WATER SPECIFIC GRAVITY, 1.07
AVERAGE FLOWING TEMP.,F: 150
WATER FRACTION:
o O
1
2
3
4
5
6
7
8
E-< 9..
o
o
~ 10
tI:
!;:11
'""
12
13
14
15
16
17
18
19
20
4
I
8 12 16
PRESSURE, 100 PSIG
20 24 28 32 36 40 44
.5
48 52 56
-t-
Pressure Traverse Curves 323
GAS GRAVITY: 0.65
OIL API GRAVITY: 35
WATER SPECIFIC GRAVITY: 1.07
AVERAGE FLOWING TEMP.,F: 150
TUBING· SIZE, IN.: 3.958
LIQUIO RATE, STBL/O: 2000
WATER FRACTION: O
o O
1
2
3
4
5
6
7
8
.. 9..
o
o
~ 10
'"1;:11
'""
12
13
14
15
16
17
18
19
20
4
I
8 12 16
PRESSURE, 100 PSIG
20 24 28 32 36 40 44 48 52 56
324 Production Optimiza/ion Using Nodal Analysis
GAS GRAVITY: 0.65
OIL API GRAVITY: 35
WATER SPECIFIC GRAVITY: 1.07
AVERAGE FLOWING TEMP.,F: 150
LIQUIO RATE, STBL!O: 3000
WATER FRACTION: 1
TUBING SIZE, IN.: 3.958
56
1-4
52484440
PRESSURE, 100 PSIG
20 24 28 32 36161284o O
1
2
3
4
5
6
7
8
E-< 9..
o
o
~ 10
,
'"!i:ll.,
"
12
13
14
15
16
17
18
19
20
Pressure Traverse Curves 325
I
WATER FRACTION: .5
LIQUID RATE, STBL/D: 3000
GAS GRAVITY: 0.65
OIL API GRAVITY: 35
WATER SPECIFIC GRAVITY: 1.07
AVERAGE FLOWING TEMP.,F: 150
56
.~
52484440
TUBING SIZE, IN.: 3.958
PRESSURE, 100 PSIG
20 24 28 32 36161284o O
1
2
3
4
5
6
7
8
... 9
'"
o
o
;: 10
o:
~1l
'"'"
12
13
14
15
16
17
18
19
20
326 Production Optimization Using Nada! Analysis
LIQUID RATE, STBL/D: 3000
WATER FRACTION: O
GAS GRAVITY: 0.65
OIL API GRAVITY: 35
WATER SPECIFIC GRAVITY, 1.07
AVERAGE FLOWING TEMP.,F: 150
TUBING SIZE, IN.: 3.958
o O
1
2
3
4
5
6
7
8
E-< 9..
o
o
;: 10
:z:
!i:ll
'"Q
12
13
14
15
16
17
18
19
20
4 8 12 16
PRESSURE, 100 PSIG
20 24 28 32 36 40 44 48 52 56
-~
Pressure Traverse Curves 327
WATER FRACTION:
LIQUID RATE, STBL/D: 5000
GAS GRAVITY: 0.65
OIL API GRAVITY: 35
WATER SPECIFIC GRAVITY, 1.07
AVERAGE FLOWING TEMP.,F: 150
5652484440
TUBING SIZE, IN.: 3.958
PRESSURE, 100 PSIG
20 24 28 32 36161284o O
1
2
3
4
5
6
7
8
.. 9..
o
o
;: 10
"'ii:ll
"'"
12
13
14
15
16
17
18
19
20
328 Production Optimization Using Nadal Analysis
GAS GRAVITY: 0.65
OIL API GRAVITY: 35
WATER SPECIFIC GRAVITY, 1.07
AVERAGE FLOWING TEMP.,F: 150
TUBING SIZE, IN.: 3.958
LIQUID RATE, STBL/D: 5000
WATER FRACTION: .5
o O
1
2
3
4
5
6
7
8
.. 9..
o
o
;: 10
'"g;11
'"e
12
13
14
15
16
17
18
19
20
4 8 12 16
PRESSURE, 100 PSIG
20 24 28 32 36 40 44 48 52 56
Pressure Traverse Curves
PRESSURE, 100 PSIG
O O 4 8 12 16 20 24 28 32 36 40 44 48 52 56
+
1
TUBING SIZE, IN.: 3.958
2 LIQUID RATE, STBL/D: 5000
WATER FRACTION: O
3
GAS GRAVITY: 0.65
4
OIL API GRAVITY: 35
WATER SPECIFIC GRAVITY: 1. 07
AVERAGE FLOWING TEMP.,F: 150
5
6
7
8
... 9..
o
o
;: 10
"'1;:11
'""
12
13
14
15
16
17
18
19 m
20
329
>30 Production Optimiza/ion Using Nadal Analysis
GAS GRAVITY: 0.65
OIL API GRAVITY: 35
WATER SPECIFIC GRAVITY: 1.07
AVERAGE FLDWING TEMP.,F: 150
TUBING SIZE, IN.: 3.958
LIQUID RATE, STBL/D: 8000
WATER FRACTION: 1
5652484440
PRESSURE, 100 PS!G
20 24 28 32 3616128
1
2
3
4
5
6
7
8
é< 9....
o
o
~ 10
'"a: 11.,
"
12
13
14
15
16
17
18
19
20
Pressure Traverse Curves 331
LIQUIO RATE, STBL/O: 8000
WATER FRACTION: .5
GAS GRAVITY: 0.65
OIL API GRAVITY: 35
WATER SPECIFIC GRAVITY:. 1.07
AVERAGE FLOWING TEMP.,F: 150
5652464440
TUBING SIZE, IN.: 3.958
PRESSURE, 100 PSIG
20 24 26 32 36161264o O
1
2
3
4
5
6
7
6
O< 9..
o
o
~ 10
'"¡;:11
'""
12
13
14
15
16
17
16
19
20
332 Production Optimization Using Noda! Analysis
TUBING SIZE, IN.: 3.958
LIQUID RATE, STBL/D: 8000
GAS GRAVITY: 0.65
OIL API GRAVITY: 35
WATER SPECIFIC GRAVITY,. 1.07
AVERAGE FLOWING TEMP.,F: 150
WATER FRACTION:
565248
o
4440
PRESSURE, 100 PSIG
20 24 28 32 36161284O O
1
2
3
4
5
6
7
8
'" 9ro..
o
o
~ 10
o:
l;;11
"'Cl
12
13
14
15
16
17
18
19
20
Pressure Traverse Curves 333
WATER FRACTION:
TUBING SIZE, IN.: 3.958
10000LIQUID RATE, STBL/D:
5652484440
GAS GRAVITY: 0.65
OIL API GRAVITY: 35
WATER SPECIFIC GRAVITY: 1.07
AVERAGE FLOWING TEMP.,F: 150
PRESSURE, 100 PSIG
20 24 28 32 36161284
1
2
3
4
5
6
7
8
.. 9..
o
o
~ 10
"'!i::u
'""
12
13
14
15
16
17
18
19
20
334 Production Optimization Using Noda/ Analysis
GAS GRAVITY: 0.65
OIL API GRAVITY: 35
WATER SPECIFIC GRAVITY:. 1.07
AVERAGE FLOWING TEMP.,F: 150
TUBING SIZE, IN.: 3.958
LIQUID RATE, STBL/D: 10000
WATER FRACTIüN: .5
O
1
2
3
4
5
6
7
6
.. 9...
o
o
;: 10
:x:
~11
'"Q
12
13
14
15
16
17
16
19
20
4 6 12 16
PRESSURE, 100 PSIG
20 24 26 32 36 40 44 46 56
Pressure Traverse Curves 335
LIQUID RATE, STBL/D: 10000
WATER FRACTION: O
5652484440
GAS GRAVITY: 0.65
OIL API GRAVITY: 35
WATER SPECIFIC GRAVITY:. 1.07
AVERAGE FLOWING TEMP.,F: 150
TUBING SIZE, IN.: 3.958
PRESSURE, 100 PSIG
20 24 28 32 361612840.0
1
2
3
4
5
6
7
8
... 9f«
o
o
;: 10
'"1;:11
"'"
12
13
14
15
16
17
18
19
20
336 Production Optimization Using Noda! Analysis
PRESSURE, 100 PSIG
O O 2 4 6 8 10 12 14 16 18 20 22 24 26 28
-.·.lHt/WJtWIi:t: H:H+f-FlI=¡~-+t - iIT· .. -. J--L: -1-1+1-1+ t
1 ,-'+ PIPELINE 1.0. , IN. : 2
•ftJ=i • STBL/D:2 +-I...!.· LIQUID RATE, 100
- - - - --
WATER FRACTION: 1
3
GAS GRAVITY: 0.65·
OIL API GRAVITY: 35
4 WATER SPECIFIC GRAVITY: 1. 07
AVERAGE FLOWING TEMP.,F: 100
CORRELATION: BEGGS & BRILL
5 rt-- I • ~ -
6
7
8
.....
o 9
o
o
~
,10
o:...
'" -f¡;jll
H
12
13
14
15
16
17
18
1 --r - - - - --
2
- - - . - T :
Pressure Traverse Curves 337
2826
l. o., 2
20
LIQUID RATE, STBL/D: 100
WATER FRACTION: O
GAS GRAVITY: 0.65·
OIL API GRAVITY: 35
WATER SPECIFIC GRAVITY: 1.07
AVERAGE FLOWING TEMP.,F: 100
CORRELATION: BEGGS & BRILL
PRESSURE, 100 PSIG
10 12 14 16 18864o O 2
1
2
3
4
5
6
7
8
E-<..
o 9
o
o....
10
"'E-<
'"¡:j11
H
12
13
14
15
16
17
18
1
2
338 Production Optirnization Using Noda! Analysis
PRESSURE, 100 PSIG
:1
2 4 6 8 10 12 14 16 18 20 22 24 26 28
-l~itlftrn:ltt~jitt~I:!-Irn'JI1L+_ ,___ _ _ _ _ ___ _ __-> -¡ _. - - -I-f-I+++-I-I:--_ .l._
'-j-f- - PIPELINE I. D. , IN. : 2
-~tr
~
f- -i+
STBL/D:2
.. ( -l-. LIQUID RATE, 200
--
WATER FRACTION: 1
3
GAS GRAVITY: 0.65
OIL API GRAVITY: 35
4 WATER SPECIFIC GRAVITY: 1. 07
AVERAGE FLOWING TEMP.,F: 100
CORRELATION: BEGGS & BRILL
5
ti-
. - I --
6
7
8
E-<..
o 9
o
o....
• 10
"'E-<
" - f~ 11
..:l
12
13
14
15
16
17
18
1
- -r- +-r2 -1
340 Production Optimizalion Using Nodal Analysis
liti1tt:J::l:jt~:1 flFi I H-t+HII:i:t
-i j- - -l:ill:n f-Fr¡:ll-f I1 +H+I-I:r1
-+i-l- PIPELINE 1. D., IN.: 2
:1+$1. LIQUID RATE, STBL/D: 300
WATER FRACTION: 1
GAS GRAVITY': 0.65
OIL API GRAVITY': 35
WATER SPECIFIC GRAVITY': 1.07
AVERAGE FLOWING TEMP.,F: 100
CORRELATION: BEGGS & BRILL
o O
1
2
3
4
2 4 6 8
PRESSURE, 100 PSIG
10 12 14 16 18
-,-
20 22 24 26 28
5
6
-H- --. H- --
7
8
E-< 11..
o 9
o
f
o
.-<
,10
'"E-<el
í;¡ll
..:l
12
13
14
15
16
17
L
18 • r11- • - - - - - -1:20 ,r
Pressure Traverse Curves 341
- 1 ....
---\. - - - .
lT·- ..
2826242220
PIPELINE 1.0., IN.: 2
LIQUIO RATE, STBL/O: 300
WATER FRACTION: O
GAS GRAVITY, 0.65·
OIL API GRAVITY: 35
WATER SPECIFIC GRAVITY: 1.07
AVERAGE FLOWING TEMP.,F: 100
CORRELATION: BEGGS • BRILL
PRESSURE, 100PSIG
10 12 14 16 18864
1
2
3
4
5
6
7
8
O<..
o 9
o
o
~
.10
'"O<
"¡;jll..,
12
13
14
15
16
17
18
1
2
342 Production Optimization Using Nada' Analysis
PIPELINE 1.0., IN.: 2
f-
~- LIQUIO RATE, STBL/O: 400
WATER FRACTION: 1
20
-GAS GRAVITY: 0.65
OIL API GRAVITY: 35
WATER SPECIFIC GRAVITY: 1.07
AVERAGE FLOWING TEMP.,F: 100
CORRELATION: BEGGS & BRILL
PRESSURE, 100 PSIG
10 12 14 16 18864
1
2
3
4
5
6
7
8
€o<..
o 9
o
o....
• 10
'"€o<Cl
¡;jll
H
12
13
14
15
16
17
18
1
2
Pressure Traverse Curves
1
2
3
4
5
6
7
8
....
o 9
o
o...
•10
'"..
"f:jll
..:l
12
13
14
15
16
17
18
1
2
4 6 8
PRESSURE, 100 PSIG
10 12 14 ,16 18
PIPELINE 1.0., IN.: 2
i~ LIQUIO'RATE, STBL!O: 400
WATER FRACTION: O
'GAS GRAVITY: 0.65'
OIL API GRAVITY: 35
WATER SPECIFIC GRAVITY: 1.07
AVERAGE FLOWING TEMP.,F: 100
CORRELATION: BEGGS & BRILL
343
344 Production Optimization Using Nodal Analysis
WATER FRACTION: 1
1- f-·
+- LIQUID RATE, STBL/D: sao
28262420
PIPELINE 1. D., IN.: 2
--GAS GRAVITY: 0.65-
OIL API GRAVITY: 35
WATER SPECIFIC GRAVITY: 1.07
AVERAGE FLOWING TEMP.,F: 100
CORRELATION: BEGGS & BRILL
PRESSURE, 100 PSIG
10 12 14 16 18864
1
2
3
4
5
6
7
8
E-<..
o 9
o
o
~
,lO
'"E-<
'"f:111..,
12
13
14
15
16
17
18
1
~
2
Pressure Traverse Curves 345
WATER FRACTION: O
28262420
PIPELINE I.D., IN.: 2
LIQUID RATE, STBL/D: 500
""GAS GRAVITY: 0.65"
OIL API GRAVITY: 35
WATER SPECIFIC GRAVITY: 1.07
AVERAGE FLOWING TEMP.,F: 100
CORRELATION: BEGGS & BRILL
1- - -f
-'-o-r-r
PRESSURE, 100 PSIG
10 12 14 16 18864
1
2
3
4
5
6
7
8....
o 9
o
o
~
,10
"'..
"~11
él
12
13
14
15
16
17
18
1
20
146 Production Optimization Using Noda! Ana/ysis
PIPELINE LO., IN.: 2
WATER FRACTION: 1
20
-GAS GRAVITY: 0.65-
OIL API GRAVITY: 35
WATER SPECIFIC GRAVITY: 1.07
AVERAGE FLOWING TEMP.,F: 100
ORRELATION: BEGGS & BRILL
1- - -1-
~- LIQUIO RATE, STBL/o: 700
PRESSURE, 100 PSIG
10 12 14 16 18864
1
2
3
4
5
6
7
8
8..
e 9
e
e
~
,la
'"8
'"tí 11
,..;¡
12
13
14
15
16
17
18
1
~
2
Pressure Traverse Curves. - 347
PIPELINE I.D., IN.: 2
1-
~" LIQUIDRATE, STBL!D: 700
2420
WATER FRACTION: O
"GAS GRAVITY: 0.65
OIL API GRAVITY: 35
WATER SPECIFIC GRAVITY: 1.07
AVERAGE FLOWING TEMP.,F: 100
CORRELATION: BEGGS & BRILL
PRESSURE, 100 PSIG
10 12 14 16 18864
1
2
3
4
5
6
7
8..
'"o 9
o
o....
•10
tI:..
"&1 11..,
12
13
14
15
16
17
18
1
--/
2
348 Production Optimiza/ion Using Nadal Analysis
WATER FRACTION: 1
f- - +-
~. LIQUID RATE, STBL/D: 900
28262420
PIPELINE LD., IN.: 2
GAS GRAVITY: 0.65
OIL APr GRAVITY: 35
WATER SPECIFIC GRAVITY: 1.07
AVERAGE FLOWING TEMP.,F: 100
CORRELATION: BEGGS & BRrLL
PRESSURE, 100 PSIG
10 12 14 16 18864
1
2
3
4
5
6
7
8....
o 9
o
o...
,10
'"E<
"f;Jll
H
12
13
14
15
16
17
18
1
2
Pressure Traverse Curves 349
LIQUID RATE, STBL/D: 900
WATER FRACTION: O
- GAS GRAVITY: 0.65-
OIL API GRAVITY: 35
WATER SPECIFIC GRAVITY: 1.07
AVERAGE FLOWING TEMP.,F: 100
CORRELATION: BEGGS & BRILL
PIPELINE 1. D., IN.: 2
28262420 22
.1.
f
+- - +
-'--
PRESSURE, 100 PSIG
10 12 14 16 18864
1
2
3
4
5
6
7
8....
o 9
o
o
~
.10
"'..
"~1l..,
12
13
14
15
16
17
18
1
. -j,
2
350 Production Optimization Using Nodal Analysis
PIPELINE I.O., IN.: 2
+-'-. LIQUIO RATE, STBL/o: 1200
WATER FRACTION: 1
20
GAS GRAVITY: 0.65·
OIL API GRAVITY: 35
WATER SPECIFIC GRAVITY: 1.07
VERAGE FLOWING TEMP.,F: 100
C RELATION: BEGGS & BRILL
PRESSURE, 100 PSIG
10 12 14 16 1886
1
2
3
4
5
6
7
8....
o 9
o
o....
•10
'"..
'"~11..,
12
13
14
15
16
17
18
1
2
Pressure Traverse Curves 351
PIPELINE I.D., IN.: 2
PRESSURE, 100 PSIG
10 12 14 16 18 20
GAS GRAVITY: 0.65·
OIL API GRAVITY: 35
WATER SPECIFIC GRAVITY: 1.07
AVERAGE FLOWING TEMP.,F: 100
ORRELATION: BEGGS & BRILL
-1-
-'-. LIQUID· RATE, STBL/D: 1200·
WATER FRACTION: O
+-
864
1
2
3
4
5
6
7
8
..
'"o 9
o
o...
•10
'"..'-'
~ 11..,
12
13
14
15
16
17
18
1
- ~
2
352 Production Optimiza/ion Using Nada! Analysis
WATER FRACTION: 1
GA RAVITY: 0.65
OIL A GRAVITY: 35
WATER S CIFIC GRAVITY: 1.07
AVERAGE F WING TEMP.,F: 100
CORRELATION. BEGGS • BRILL
282624
I.D. ,
20
LIQUID RATE, STBL/D: 1500
PRESSURE, 100 PSIG
10 12 14 16 1886
1
2
3
4
5
6
7
8....
o 9
o
o...
,la ,
'" -1-..<.!J
f:íll
H
12
13
14
15
16
17
18
1
2
Pressure Traverse Curves 353
GRAVITY: 0.65-
OIL PI GRAVITY: 35
WATER PECIFIC GRAVITY: 1.07
AVERAG LOWING TEMP.,F: 100
CORRELAT BEGGS & BRILL
LIQUID RATE, STBL/D: 1500
28262420
WATER FRACTION: o
PIPELINE I.D., IN.: 2
-,
PRESSURE, 100 PSIG
10 12 14 16 18
.1.. +
86
, '
:,,- - ,
"
1
2
3
4
5
6
7
8..
r..
o 9
o
o
.-<
,la
:c..
"f:í 11,..,
12
13
14
15
16
17
18
1
2
354 Production Optimiza/ion Using Nada! Analysis
WATER FRACTION: 1
LIQUID RATE, STBL/D: 2000
2826242220
~- r
,
GRAVITY: 0.65-
I GRAVITY: 35
ECIFIC GRAVITY: 1.07
AVERAGE OWING TEMP.,F: 100
ORRELATIO : BEGGS & BRrLL
PRESSURE, 100 PSIG
10 12 14 16 1886
1
2
3
4
5
6
7
8....
o 9
o
o....
•10 ,
'" .+..
"i:íll
..:1
12
13
14
15
16
17
18
1
----.__ .
-- +2
Pressure Traverse Curves 355
PRESSURE, 100 PSIG
2 4 6 8 10 12 14 .16 18 20 22 24 26 28
- i
1
PIPELINE l. o. , IN. : 2
-~.. - -1
2
--'- LIQUID RATE, STBL/D: 2000
WATER FRACTION: O
3
AS GRAVITY: 0.65·
O API GRAVITY: 35
~ 4 WA SPECIFIC GRAVITY: 1. 07. AVERA FLOWING TEMP.,F: 100
CORRELK ON: BEGGS & BRILL
5
6
7
8.... - - -
o 9
o
o....
,lO
"'..
el
~¡;jll
>-1
12
13
14
15
16
17
18
- - - -
1
- - - -1 ... - . - -
-1 - -2
356 Production Optimization Using Nodaf Analysis
PIPELINE I.O., IN.: 3
WATER FRACTION:
28262420
LIQUIO RATE, STBL/o: 500
GAS GRAVITY: 0.65·
OIL API GRAVITY: 35
WATER SPECIFIC GRAVITY: 1.07
AVERAGE FLOWING TEMP.,F: 100
CORRELATION: BEGGS & BRILL
~
¡.
-'-.
PRESSURE, 100 PSIG
10 12 14 16 1886
1
2
3
4
5
6
7
B
E-<..
o 9
o
o
.-<
.10
'"E-<
'"¡;'jll
>'l
12
13
14
15
16
17
18
1
.2
Pressure Traverse Curves 357
28262420
LIQUID RATE, STBL/D: 500
WATER FRACTION: O
GAS GRAVITY: 0.65'
OIL API GRAVITY: 35
WATER SPECIFIC GRAVITY: 1.07
AVERAGE FLOWING TEMP.,F: 100
CORRELATION: BEGGS & BRILL
r
PRESSURE, 100 PSIG
10 12 14 16 18864
0 0 2
1
2
3
4
5
6
7
8
.,..
o 9
o
o
.-<
.10
"'.,
"¡;jll
'"
12
13
14
15
16
17
18
1
2
358 Production Optimization Using Nodal Anolysis
WATER FRACTION: 1
GAS GRAVITY: 0.65-
OIL API GRAVITY: 35
WATER SPECIFIC GRAVITY: 1.07
AVERAGE FLOWING TEMP.,F: 100
CORRELATION: BEGGS & BRILL
,r
2826242220
PIPELINE I.D., IN.: 3
, f-
~- LIQUID RATE, STBL/D: BOa
PRESSURE, 100 PSIG
10 12 14 16 18864
1
2
3
4
5
6
7
8....
o 9
o
o....
,ID
o:..
<.!J
f:¡11..,
12
13
14
15
16
17
18
1
2
Pressure Traverse Curves 359
PIPELINE I.D., IN.: 3
LIQUIDRATE, STBL/D: 800
WATER FRACTION: o
GAS GRAVITY: 0.65'
OIL API GRAVITY: 35
WATER SPECIFIC GRAVITY: 1.07
AVERAGE FLOWING TEMP.,F: 100
CORRELATION: BEGGS & BRILL
1
2
3
4
5
6
7
8
E-<..
o 9
o
o
~
,la
o::
E-<
<.O
f:111
H
12
13
14
15
16
17
18
1
20
4 6 8
PRESSURE, 100 PSIG
10 12 14 16 18
++- - 1-·
-'-o
20 22 24 26 28
360 Produc(ion Optimization Ur;ing Nada! Analysis
GAS GRAVITY: 0.65·
OIL API GRAVITY: 35
WATER SPECIFIC GRAVITY: 1.07
AVERAGE FLOWING TEMP.,F: 100
CORRELATION: BEGGS & BRILL
LIQUID RATE, STBL/O: 1000
28262420
PIPELINE I.D., IN.: 3
WATER FRACTION: 1
+-
r
PRESSURE, 100 PSIG
10 12 14 16 18
~ .1
~- --
864
1
2
3
4
5
6
7
8
E-<..
o 9
o
o..-.
.10
"'E-<<!J
f:jll..,
12
13
14
15
16
17
18
1
2
Pressure Traverse Curves 361
1-
GAS GRAVITY: 0.65-
OIL API GRAVITY: 35
WATER SPECIFIC GRAVITY: 1.07
AVERAGE FLOWING TEMP.,F: 100
CORRELATION: BEGGS & BRILL
28262420
PIPELINE 1.0., IN.: 3
WATER FRACTION: O
LIQUID RATE, STBL/D: 1000
-r -
_ ...L. ' •.
PRESSURE, 100 PSIG
10 12 14 16 18864
1
2
3
4
5
6
7
8
ó<..
o 9
o
o
n
.10
"'ó<'-'
¡;jll
H
12
13
14
15
16
17
18
1
2
362 Production Optimization Using Nodal Analysis
WATER FRACTION: 1
LIQUIO RATE, STBL/O:1500
2826242220
PIPELINE 1.0., IN.: 3
GAS GRAVITY: 0.65·
OIL API GRAVITY: 35
WATER SPECIFIC GRAVITY: 1.07
AVERAGE FLOWING TEMP •• F: 100
CORRELATION: BEGGS & BRILL
r·
PRESSURE. 100 PSIG
10 12 14 16 18864
1
2
3
4
'"
.~ 5
6
7
8
....
o 9
o
o.,
,10
'"..
'"f:íll
..:l
12
13
14
15
16
17
18
1
20
Pressure Traverse CUrles 363
PIPELINE I.D., IN.: 3
LIQUID RATE, STBL/D: 1500
GAS GRAVITY: 0.65
OIL API GRAVITY: 35
WATER SPECIFIC GRAVITY: 1.07
AVERAGE FLOWING TEMP.,F: 100
CORRELATION: BEGGS & BRILL
o
2220
WATER FRACTION:
- - -1.. '
PRESSURE, 100 PSIG
10 12 14 '16 18864
1
2
3
4
5
6
7
8..
'"o 9
o
o....
,la
'"..
"¡;¡11..,
12
13
14
15
16
17
18
1
2
364 Production Optimization Using Nodal Analysis
GAS GRAVITY: 0.65-
OIL API GRAVITY: 35
WATER SPECIFIC GRAVITY: 1.07
AVERAGE FLOWING TEMP.,F: 100
ORRELATION: BEGGS & BRILL
2826242220
LIQUID RATE, STBL/D: 2000
WATER FRACTION: 1
PRESSURE, 100 PSIG
10 12 14 16 18864
,
+
:1
-c
1
2
3
4
5
6
7
8....
o 9
o
o
~
,la
'"..t!J
¡:¡ 11
"'
12
13
14
15
16
17
18
1
2
Pressure Traverse Curves 365
PRESSURE, 100 PSIG
2 4 6 8 10 12 14 16 18 20 24 26 28
1 3PIPELINE l. D. , IN. :
¡. -~+ 2000
2
-'.- LIQUID RATE, STBL/D:,
-- -
WATER FRACTION: O
3
GAS GRAVIT'l: 0.65-
OIL API GRAVIT'l: 35
4 WATER SPECIFIC GRAVIT'l: 1. 07
AVERAGE FLOWING TEMP.,F: 100
CORRELATION: BEGGS & 8RILL
5
6
7
8
O<..
o 9
o
o
~
,lO
"'O<
"¡;jll
H
12
13
14
15
16
17
18
-c
1
,
2 -1 " r
366 Production Optimizarion Using Nada! Analysis
GAS GRAVITY: 0.65-
OIL API GRAVITY: 35
WATER SPECIFIC GRAVITY: 1.07
AVERAGE FLOWING TEMP.,F: 100
CORRELATION: BEGGS & BRILL
¡-
28262420
LIQUID RATE, STBL/D: 3000-
WATER FRACTION: 1
PIPELINE I.D., IN.: 3
-1
~-
PRESSURE, 100 PSIG
10 12 14 16 18864
-+
-1-
1
2
3
4
5
6
7
8
...
'"o 9
o
o
.-<
.10
'"...'-'
f;'jll
,..:¡
12
13
14
15
16
17
18
1
2
Pressure Traverse Curves 367
··GAS GRAVITY: 0.65·
OIL API GRAVITY: 35
WATER SPECIFIC GRAVITY: 1.07
AVERAGE FLOWING TEMP.,F: 100
CORRELATION: BEGGS & BRILL
WATER FRACTION: O
28262420
PIPELINE I.D., IN.: 3
LIQUID RATE, STBL/D: 3000
PRESSURE, 100 PSIG
10 12 14 16 18864
1
2
3
4
5
6
7
8
"'..
o 9
o
o....
,lO
'""''-'¡;jll,..,
12
13
14
15
16
17
18
1
2
368 Production Optimiza/ion Using Nada! Analysis
S GRAVITY: 0.65-
01 API GRAVITY: 35
WAT SPECIFIC GRAVITY: 1.07
AVERAG FLOWING TEMP.,F: 100
CQRRELA ON: BEGGS & BRILL
PIPELINE 1.0., IN.: 3
28262420
WATER FRACTION: 1
LIQUID RATE, STBL!D: 4000
-,
1- - -l·
"1 -l..
PRESSURE, 100 PSIG
10 12 14 16 1886
- '
"'-,
1
2
3
4
5
6
7
8
E-<
r..
o 9
o
o
~
,lO
:c
E-<
e>¡;¡ 11..,
12
13
14
15
16
17
18
1
2
Pressure Traverse Curves 369
GAS GRAVITY: 0.65
~
API GRAVITY: 35
WA ER SPECIFIC GRAVITY: 1.07
AVE GE FLOWING TEMP.,F: 100
. CORRE TION: BEGGS • BRILL
1Ilr.-1-
r
2826242220
-,~- - --I-f- .-
WATER FRACTION: o
PIPELINE I.D., IN.: 3
1+ ~
-=t: q:: 1:. LIQUID RATE, STBL/D: 4000
PRESSURE, 100 PSIG
10 12 14 16 1886:. 4
2
3
4
5
6
7
8
E-<
Ó<
o 9
o
o
~
,la
o:
E-<
"~ 11
H
12
13
14
15
16
17
18
1
:1- - .
-
- - ~:~
2
370 Production Optimization Using Nodal Analysis
PRESSURE, 100 PSIG
2 4 6 8 10 12 14 16 18 20 24 26 28
1
PIPELINE l. o. , IN. : 3
;- - 1-
2 -'o LIQUID RATE, STBL/D: 5000
WATER FRACTION: 1
3
GAS GRAVITY: 0.65'
OIL API GRAVITY: 35
4 TER SPECIFIC GRAVITY: 1. 07
AGE FLOWING TEMP.,F: 100
LATION: BEGGS & BRILL
5
6
7
8.....
o 9
o
o....
,la
"'E-<
'"f;¡11..,
12
13
14
15
16
17
18
1
- :1·
"2 r
Pressure Traverse Curves 371
PIPELINE I.D., IN.: 3
WATER FRACTION: O
26242220
LIQUIO RATE, STBL/O: 5000
GAS GRAVITY: 0.65
OIL API GRAVITY: 35
WATER SPECIFIC GRAVITY: 1.07
VERAGE FLOWING TEMP.,F: 100
RRELATION: BEGGS & BRILL
e-
1- - f·
'1 .J..
PRESSURE, 100 PSIG
10 12 14 16 lB86
1
2
3
4
5
6
7
8....
o 9
o
o
~
,lO
c::..
'"f:jll
..:l
12
13
14
15
16
17
18
1
-1
2
372 Production Optimization Using Noda! Analysis
2826242220
PRESSURE, 100 PSIG
10 12 14 16 188
1
2 6000
FRACTION: 1
3
4
5
6
7
8
.....
o 9
o
o....
,lO
I::: •.¡....
"f:jll
H
12
13
14
15
16
17
18
1
. ·1
"2
Pressure Traverse Curves 373
PIPELINE I.D., IN.: 3
LIQUID RATE, STBL/D: 6000
WATER FRACTION: O
28262420
S GRAVITY: 0.65
OI PI GRAVITY: 35
WATE PECIFIC GRAVITY: 1.07
AVERAG FLOWING TEMP.,F: 100
CORRELAT N: BEGGS • BRILL
->
-f
_1 -l-_
PRESSURE, 100 PSIG
10 12 14 16 188
,
.+
1
2
3
4
5
6
7
8
....
o 9
o
o....
,10
'"..
'"f:jll
H
12
13
14
15
16
17
18
1
2
374 Production Oprimi=ation Using Nada! Analysis
WATER FRACTION: 1
1- -~~
+, LIQUID RATE, STBL/D: 1000
2826
4
2420
PIPELINE
"- + -1
+-r f
GAS GRAVITY: 0.65
OIL API GRAVITY: 35
WATER SPECIFIC GRAVITY: 1.07
AVERAGE FLOWING TEMP.,F: 100
CORRELATION: BEGGS & BRILL
PRESSURE, 100 PSIG
10' 12 14 1618864
1
2
3
4
5
6
7
8
8..
o 9
o
o
~
.10
'"8
'"&111
'"
12
13
14
15
16
17
18
1
2
Pressure Traverse Curves 375
WATER FRACTIDN: O
++
2826242220
GAS GRAVITY: 0.65-
OIL API GRAVITY: 35
WATER SPECIFIC GRAVITY: 1.07
AVERAGE FLOWING TEMP.,F: 100
CORRELATION: BEGGS & BRILL
'. PIPELINE I. D., IN.: 4
" ::t: :t: LIQUID RATE, STBL/D: 1000-
PRESSURE, 1.00 PSIG
10 12 14 16 18864
1
2
3
4
5
6
7
8
E<..
o 9
o
o
n
,10
'"E<
'"¡;jll
,.:¡
12
13
14
15
16
17
18
1
2
376 Production Optimization Using Nodal Analysis
GAS GRAVITY: 0.65'
OIL API GRAVITY: 35
WATER SPECIFIC GRAVITY: 1.07
AVERAGE FLOWING TEMP.,F: 100
CORRELATION: BEGGS & BRILL
282620
PIPELINE I.O., 4
LIQUIO RATE, STBL/O: 1500
WATER FRACTION: 1
, ,
-- _.>-
PRESSURE, 100 PSIG
10 12 14 16 18
-1" ~_.I "-.-.L __
±
4 6 8
1
2
3
4
5
6
7
8
....
o 9
o
o
'""',lO
'"..
el
~11
H
12
13
14
15
16
17
18
1
2
PresslIre Traverse Curves 377
LIQUID RATE, STBL/D: 1500
WATER FRACTION: O
GAS GRAVITY: 0.65·
OIL API GRAVITY: 35
WATER SPECIFIC GRAVITY: 1.07
AVERAGE FLOWING TEMP.,F: 100
CORRELATION: BEGGS & BRILL
282624
I. D. ,
20
PRESSURE, 100 PSIG
10 12 14 16 18864
1
2
3
4
5
6
7
8
..
O<
o 9
o
o
~
.10
"'..
<!)
~11
>.:l
12
13
14
15
16
17
18
1
2
378 Prodllction Optimiza/ion Using Noda! Analysis
o O 2 4 6 8
PRESSURE, 100 PSIG
10 12 14 16 18
-++
20 22 24 26 28
2
3
4
5
6
,-¡-I--
-1+il-~n::¡-I
- I ...1-.
1-
PIPELINE I.D., IN.: 4
LIQUID RATE, STBL/D: 2000
WATER FRACTION: 1
GAS GRAVITY: 0.65-
OIL API GRAVITY: 35
WATER SPECIFIC GRAVITY: 1.07
AVERAGE FLOWING TEMP.,F: 100
CORRELATION: BEGGS & BRILL
-'-j-- - -
. rT --
7
8 I8..
o 9
o
o
~
,lO
o:
8
t!1
¡;j1l
H
~1tM
12
13
14
15
16
17
18 • t19 i J~ -mi-o: ..
2 ,
~-r
Pressure Traverse Curves 379
+-r
28262420
4
LIQUID RATE, STBL/D: 2000
WATER FRACTION: O
GAS GRAVITY: 0.65·
OIL API GRAVITY: 35
WATER SPECIFIC GRAVITY: 1.07
AVERAGE FLOWING TEMP.,F: 100
CORRELATION: BEGGS & BRILL
PRESSURE, 100 PSIG
1012 14 16 18864
1
2
3
4
5
6
7
8....
o 9
o
o....
,lO
"'..eJ
í;jll...,
12
13
14
15
16
17
18
1
2
380 Production Optimization Using Nodal Analysis
GAS GRAVITY: 0.65
OIL API GRAVITY: 35
WATER SPECIFIC GRAVITY: 1.07
AVERAGE FLDWING TEMP.,F: 100
CORRELATIDN: BEGGS & BRILL
,r
. r+
2826242220
PIPELINEI.D., IN.: 4
LIQUID RATE, STBL/D: 3000
WATER FRACTION: 1
++ ---1+ ~.
PRESSURE, 100 PSIG
10 12 14 16 188642o O
1
2
3
4
5
6
7
8
.....
o 9
o
o....
•10
'"...lO¡;¡ 11
H
12
13
14
15
16
17
18
1
2
·1~itj:j+t+Hm~l:UiftH+H-Ht¡i
- il-~U_-U tltJítttul-H-I+HFI+
'++ PIPELINE LO .• IN.: 4
::t,+
.. :r:l: - LIQUIO RATE. STBL/o: 3000
WATER FRACTION: o
GAS GRAVITY: 0.65-
OIL API GRAVITY: 35
WATER SPECIFIC GRAVITY: 1.07
AVERAGE FLOWING TEMP •• F: 100
CORRELATION: BEGGS & BRILL
Pressure Traverse Curves
o O 2
1
2
3
ft\\1\
4 I
5
6
7
8
E-<..
o 9
o
o
~
,la
'"E-<
"i;'jll
H
12
13
14
15
16
17
18
1
- -ro
2
4 6 8
PRESSURE. 100 PSIG
10 12 14 16 18 20 22 24 26 28
381
382 Production Optimiza/ion Using Nadal Analysis
2826242220
GRAVITY, 0.65-
API GRAVITY: 35
SPECIFIC GRAVITY: 1.07
AVERA FLOWING TEMP.,F: 100
CORRELA ION: BEGGS& BRILL
PIPELINE I.D., IN.: 4
-1-
~- LIQUIDRATE, STBL/D: 5DOO-
WATER FRACTION: 1
PRESSURE, 100 PSIG
10 12 14 16 18864
1
2
3
4
5
6
7
8
E-<
r.
o 9
o
o....
•10
tI:
E-<
<él
f:lll
.:l
12
13
14
15
16
17
18
1
- - --1-
"-
2
Pressure Traverse Curves 383
PRESSURE, 100 PSIG
2 4 6 8 10 12 14 16 18 20 22 24 26 28
1
'-1 PIPELINE l. D. I IN. : 4
1- --i+
STBL/D:2 , -'-. LIQUID RATE, 5000
WATER FRACTION: O
3
GAS GRAVITY: 0.65·
IL API GRAVITY: 35
4 W ER SPECIFIC GRAVITY: 1. 07
AVE GE FLOWING TEMP.,F: 100
CORR ATION: BEGGS & BRILL
5
6
7
8.....
o 9
o
o
",10
o:..
el
511..,
12
13
14
15
16
17
18
1
- - ·1
20
.. ._¡ 1-,
384 Production Optimization Using Nodal Analysis
"
- -1
2826
IN.: 4
20
PIPELINE
LIQUID RATE, STBL/D: 8000
WATER FRACTION: 1
GRAVITY: 0.65-
API GRAVITY: 35
R SPEClfIC GRAVITY: 1.07
AVE GE FLOWING TEMP.,F: 100
CORRE TION: BEGGS & BRILL
PRESSURE, 100 PSIG
10 12 14 16 1886
1
2
3
4
5
6
7
8
.,
'"o 9
o
o
~
.10
o: :1..,
lO
~11
H
12
13
14
15
16
17
18
1
- - - :j
-1
- -r
2
Pressure Traverse Curves 385
WATER FRACTION: o
LIQUID RATE, STBL/D: 8000
28262420
GAS GRAVITY: 0.65
OIL API GRAVITY: 35
ATER SPECIFIC GRAVITY: 1.07
A RAGE FLOWING TEMP.,F: 100
CO ELATION: BEGGS & BRILL
PRESSURE, 100 PSIG
10 12 14 16 18864
1
2
3
4
5
6
7
8....
o 9
o
o....
,la
"' -+..C9
1311
H
12
13
14
15
16
17
18
1 .. -j
~ ~ ~ -1- ~
2
~I~
386 Production Optimization U'iing Noda! Ana~vsis
282620
PRESSURE, 100 PSIG
10 12 14 16 1886
1
2 LIQUID RATE,
STBL/D: 10000
WATER FRACTION: 1
3 GAS GRAVITY: 0.65'
OIL API GRAVITY: 35
4
WATER SPECIFIC GRAVITY: 1. 07
VERAGE FLOWING TEMP.,F: 100
RELATION: BEGGS & BRILL
5
6
7
8....
o 9
O>
O>
~
,lO ,
"' 1..
l?
&i 11
H
12
13
14
15
16
17
\
18 ". r -
- - - -
1
--j -]
"
- -
2D -1-
,
Pressure Traverse Curves 387
PRESSURE, 100 PSIG
2 4 6 8 10 12 14 16 18 20 24 26 28
1
PIPELINE I.O. , IN. : 4+" - f- STBL/D:2 -'-- LIQUID RATE, 10000
--
WATER FRACTION: a
3
-- - - - GAS GRAVITY: 0.65-
OIL API GRAVITY: 35
4
WATER SPECIFIC GRAVITY: 1. 07
AVERAGE FLOWING TEMP.,F: 100
CORRELATION: BEGGS & BRILL
5
6
7
8
E-<..
o 9
o
o....
,la ,
'" ~J.E-<
"f;'jll
>-1
12
13
14
15
16
17
18
1
- -: -1
- -r--
2 -1- ,r
388 Production Optimiza/ion Using Noda! Analysis
f-
WATER FRACTION: 1
2826242220
GAS GRAVITY: 0.65-
OIL API GRAVITY: 35
WATER SPECIFIC GRAVITY: 1.07
AVERAGE FLOWING TEMP.,F: 100
CORRELATION: BEGGS & BRILL
'ti PIPELINE LO., IN.: 5
ti-'
1- . -;-f--
~I- --'-,-'-- LIQUID RATE, STBL/D: 2000
PRESSURE, 100 PSIG
10 12 14 16 18864
1
2
3
4
5
6
7
8
&<
O<
o 9
o
o
~
10
'"&<
"f;'jll
H
12
13
14
15
16
17
18
1
2
Pressure Traverse Curves 389
GAS GRAVITY: 0.65
OIL API GRAVITY: 35
WATER SPECIFIC GRAVITY: 1.07
AVERAGE FLOWING TEMP.,F: 100
CORRELATION: BEGGS & BRILL
2826242220
LIQUID RATE, STBL/D: 2000
PIPELINE 1. D., IN.: 5
WATER FRACTION: O
PRESSURE, 100 PSIG
10 12 14 16 18
I _.1 .l..
( .. +Ullittlli±±±:l±Uill±l±±J±J:±j
864
1
2
3
4
5
6
7
8....
o 9
o
o
~
,lO
'"..
'"¡;jll
"'
12
13
14
15
16
17
18
1
2
390 Production Optimi=atiQn Using Noda! rlna(l-'sis
LIQUID RATE, STBL/D: 3000
GAS GRAVITY: 0.65·
DIL API GRAVITY: 35
WATER SPECIFIC GRAVITY: 1.07
AVERAGE FLDWING TEMP.,F: 100
CORRELATION: BEGGS & BRILL
2826242220
.. --·-i···._-_.----
"
. - j-
PIPELINE 1. D., IN.: S
WATER FRACTION: 1
f
l- - - f··
~
--¡
PRESSURE, 100 PSIG
10 12 14 16 18864
1
2
3
4
5
6
7
8....
o 9
o
o
~
,lO
'"..'-'&]11
0-1
12
13
14
15
16
17
18
1
2
Pressure Traverse Curves 391
¡.. ~ +
~. LIQUIO RATE, STBL/O: 3000
GAS GRAVITY: 0.65
OIL API GRAVITY: 35
WATER SPECIFIC GRAVITY: 1.07
AVERAGE FLOWING TEMP.,F: 100
CORRELATION: BEGGS & BRILL
28262422
-1-
20
WATER FRACTION: O
-1 ..
j- -
PIPELINE 1. D., IN.: 5
PRESSURE, 100 P5IG
10 12 14 16 18864
1
2
3
4
5
6
7
8
E-<..
o 9
o
o
",10
'"E-<
"'¡¡¡ll
'"
12
13
14
15
16
17
18
1
2
392 Prodllction Optimi=ation U'iing Nodal AJ1ulysis
GAS GRAVITY: 0.65-
OIL API GRAVITY: 35
WATER SPECIFIC GRAVITY: 1.07
AVERAGE FLOWING TEMP.,F: 100
CORRELATION: BEGGS & BRILL
,r
282624
l. D.,
20
LIQUID RATE, STBL/D: SOOO
WATER FRACTION: 1
.+
PRESSURE, 100 PSIG
10 12 14 16 18864
1
2
3
4
5
6
7
8....
o 9
o
o
~
,lO
'"..
'"íJll
H
12
13
14
15
16
17
lB
1
·c
2
Pressure Traverse Curves
1
2
3
4
·5
6
7
8
...
'"o 9
o
o
'",ID
'"...
'"~ 11
>-1
12
13
14
15
16
17
18
1
~
20
4 6 8
PRESSURE, 100 PSIG
10 12 14 16 18
PIPELINE 1. O., IN.: 5
. - _ - 1- -W=f·
-¡ ~r -+ : -'-. LIQUID RATE, STBL!D: 5000
WATER FRACTION: O
GAS GRAVITY: 0.65·
OIL API GRAVITY: 35
WATER SPECIFIC GRAVITY: 1.07
AVERAGE FLOWING TEMP.,F: 100
CORRELATION: BEGGS & BRILL
393
394 Production Optimization Using Noda! Ana(vsis
28262420
LIQUID RATE, STBL/D: 8000
WATER FRACTION: 1
PIPELINE 1. D., IN.: S
GAS GRAVITY: 0.65'
OIL API GRAVITY: 35
WATER SPECIFIC GRAVITY: 1.07
ERAGE FLOWING TEMP.,F: 100
CO RELATION: BEGGS & BRILL
+
>- +
h , ~._. L
-t'
PRESSURE, 100 PSIG
10 12 14 16 18864
1
2
3
4
5
6
7
8
E-<...
o 9
o
o
.-<
10
"'E-<<!J
¡;jll
H
12
13
14
15
16
17
18
1
2
Pressure Traverse Curves 395
GAS GRAVITY: 0.65
OIL API GRAVITY: 35
WATER SPECIFIC GRAVITY: 1.07
AVERAGE FLOWING TEMP.,F: 100
RRELATION: BEGGS & BRILL
2826242220
PIPELINE I. D., IN.: 5
LIQUID' RATE, STBL/D: 8000·
WATER FRACTION: O
r
__ .i-
i-
PRESSURE, 100 PSIG
10 12 14 16 1886
1
2
3
4
5
6
7
8
....
o 9
o
o....
,lO
'"..
'-'
¡;jll..,
12
13
14
15
16
17
18
1
20
396 Production Optimi:::a/ion Using Noda! AnQ!ysis
PIPELINE I. D., IN.: 5
r
26242220
LIQUID RATE, STBL/D: 10000
WATER FRACTION: 1
GAS GRAVITY: 0.65-
OIL API GRAVITY: 35
WATER SPECIFIC GRAVITY: 1.07
AVERAGE FLOWING TEMP.,F: 100
CORRELATION: BEGGS & BRILL
-e-
->-
-'--
PRESSURE, 100 PSIG
10 12 14 16 18864
1
2
3
4
5
6
7
8
é<..
o 9
o
o
~
,lO
:r:
é<
'"¡;jll
H
12
13
14
15
16
17
18
1
-1
20
Pressure Traverse Curves 397
PRESSURE, 100 PSIG
2 4 6 8 10 12 14 16 18 20 22 24 26 28
-L
1
PIPELINE 5l. D. , IN. :
I , ++
2 'o. LIQUID RATE, STBL!D: 10000
-,
WATER FRACTION: O
3
0.65"GAS GRAVITY:
OIL API GRAVITY: 35
4 WATER SPECIFIC GRAVITY: 1. 07
AVERAGE FLOWING TEMP.,F: 100
CORRELATION: BEGGS • BRILL
5
6
7
8
E-<..
o 9
o
o...
,10
'"E-<
el
fJll
H
12
13
14
lS
16
17
18
1
" j'
2 ++
398 Production Optimization Using Noda/ Analysis
PIPELINE 1.0., IN.: 5
GAS GRAVITY: 0.65
OIL API GRAVITY: 35
WATER SPECIFIC GRAVITY: 1.07
AVERAGE FLOWING TEMP.,F: 100
CORRELATION: BEGGS & BRILL
26262420
WATER FRACTION: 1
LIQUID RATE, STBL/D: 12000,
. l
1- - +
-'-.
PRESSURE, 100 PSIG
10 12 14 16 1666
1
2
3
4
5
6
7
6
....
o 9
o
o
~
.10
"'..
'"f;jll,..,
12
13
14
15
16
17
16
1
-+
2
Pressure Traverse Curves 399
PRESSURE, 100 PSIG
10 12 14 16 18
1-
-,.
~- LIQUID RATE, STBL/D: 12000
WATER FRACTION: o
PIPELINE
20 22 24 26 28
+L~.~
I.D., IN.: 5
GAS GRAVITY: 0.65-
OIL API GRAVITY: 35
WATER SPECIFIC GRAVITY: 1.07
AVERAGE FLOWING TEMP.,F: 100
CORRELATION: BEGGS • ERILL
¡..
-+
8642
1
2
3
4
5
6
7
8
E-<..
o 9
o
o....
,la
'"E-<
"í:j11
o-l
12
13
14
15
16
17
18
¡-
1 + ·1
20
Abandonment conditions. 18
Abscissa correlating group, 110
Absolute
permeability, 14, 15,26
pressure, 124
temperature, 124
Acceleration, 84,86,87,93,97,191,194
component,67, 83, 84
term, 84
Acidizing, 49, 139
Actual
density, 195
downstream pressure, 125
drawdown, 26
gas velocity, 65, 66
¡íquid holdup, 66, 85
Iiquid velocity, 65. 66
producing capacity, 139
volumetric flow rates, 76
wellhead pressure, 100
Algorithms, 68, 78
for coupling pressure and heat loss calcula-
rians, 81
heat transfer calculation. 73
incremellting on length, 68
incrementing on pressure, 68
Altered zone penneability, 48, 52
effects of. 14
Altered radius
etTects of, 14
zane, 48, 52, 53
Alves flow pattero, 108
American Gas Association, 109, 110
Analysis. 150, 152
artificiallift wells, 155
components ofsystem, 185
OST, PVT, 144
forces acting on variousareas of valve,
165
gravel-packed completions, 174
laboratory, 72
Index
multiwell systems, 151
outtlow, 155
pressure-volume-temperature, 72
single wells, 151
Angle, choke opening, 126
Angle of indination, (13
Annular, 67, l09
area, 158
flow,90
prediction capability, 90
tests, 86
mist partero, 87
Annulus, 83, 90, 180,260
AOF, 43, 44, 45, 46
API,97
equation, 127
grav;ly, 75, 78, 80, 95
Application
curves, 98
total system analysis, 151
Vogel Method-Non-Zero Skin Factor
(Standing Modification), 26
Vogel Method-Zero Skin factor, 23, 24
Aquifer, 18, 19
Artificiallift, 4, 7, 24, 40, 136, 137, 141, 148,
150,151,153
analysis, 155
design, 155
methods, 155, 177, 183
gas lift, 155
hydraulic pumping, 155
submersible pumping, 155
sucker rod or beam pumping, 155
weHs, 146, 155, 178
Average flowing temperature, 97, 98
Average pressure, la, 113, 143
Average reservoir pressure, 2, 9,12,20,21,
22
Average system pressure, 88
Average temperature, 113
Aziz flow regimes, 88
Aziz, Govier and Fogarasi Methoct, 87
Back Pressure
equation,43
Baker flow partero map, 108, 109
Basic pressure gradient equation, 58
Beam pumping, 155, 177
unit, 178
Bean diameter, 127
Beggs and Brin
correlation, 117, 118
data, lI4,lI5
flow partero map, 108
method, 88, 89, 90, 98, 108, lll, ll2, lI4,
lI8, 192, 194
Bellows pressure, 166
Bemoulli equation, 123
Beta ratio, 127
BHP, flowing, static, 163
Bit size, 36
Borehole,9
size,51
Bortomhole, 136
chokes, 123
flowing pressure, 5, 9, 13, 14,98, -lOO,
lI4,177
pressure, 5, 43, 84, 140, 147, 155, 182
pressure gage. 31
temperature, 81
Brill and Beggs equation. 78
(modified by Standing), 78
Brine viscosity, 80
Bubble regime, 67
Bubble-flow partero, 86, 87
Bubble·rise velocity, 87
Bubblepoint, 75
pressure, 15, 18, 20, 24. 36, 37, 5l, 79,
148
Buildup test, 45
Calculated [iquid holdup values, [14
401
402 Produclion Optimiza/ion Using Noda! Ana(vsis
Calculator application, ll2
Carnco methad, 163
Capacitance
probe, 65
devices, 83
Casing, 83.160,162,180
annulus, 177
diameler, 174
gas pressure, 160
inside diameter, [82
pressure, 163, [66, 168, 177
reduction, 163
lraverse, 162
valves, 165
size, 135, 174
tied into tlowine, 180
Casinghead
flowline, 175
gas, 174, 175
Centrifugal separator, t74
Ceramic choke disk operatían, 126
Chierici, Ciucci and Sclocchi Method, 88
Choke. 123, 126
at wellhead,
capacity, 173, 176, 177
constants, 124, 126
control, 153
diameter, 124, 126, 127, 128
discharge coefficient, 126
[ocated at separator, 141, 142, 143
located at wellhead, t 41,142, L43
loeatian, 143
setting, 126
size, 123, 124. 125, 143, 163
Circular drainage, 31
area, 12, 14
Clausis inequality, 59
Clay swelling, 14
Coefficients, 123
Colcbrook equation, 61, 62
Combination drive, 19
reservoir, 19
Commingled
rate, 153
well,38
Commíngling, 153
flow streams, 152
point, 153
point pressure, 153
well streams, 152
Compacted
permeability, 51, 52
zone, 48, 50, 5[,52,53, 144
permeability, 51
radius, 51, 52
thlekness, 53
Compaction,47
Comparison studies, 92
Completion, 143
configurations design, 146
effect, 143
efficieney, 45, -1:6, 47, 48
¡ength,45
methods, 47, 143
pressure drop, 143
zonc,4S
Completions,
gravel pack, 143
open hole, 143
perforated. 143
Components, 47, 48,57,86.108,11 J, 133,
174
acceleration, 67.69
changes, 57
charaeteristics. 57
downstream. 2
elevation, 69
friction, 69
laminar
grave! pack, 48
perforation,47
reservoir, 47
turbulel1{
gravel pack, 48
perforation, 48
reservoir, 48
upstream, 2, 3, 9
Compressible, 10
flow, 64
Compressibility, 9, 79
factor, 123
Compressor, 146, 150, 152
pressures, J46
Computer application, 86, 98, 112
calculation, 68, 150
program, MONA, 90
subroutíne, 108, 111
Condensate, 72, 97, 122
Conductive heat 105s, 71
resistance,
Continuous flow gas lift, 155
system design, 155
well,60
Convection lenn. Rf 7l
Convective
acceleracion, 63
heat !oss, 10
heal: transfer, 71
resistanee, 71
Conventional
flow·afier·flow test, 31
test
pressure diagrams, 32
producing rute, 32
Convergence, 72, 85, 123,125,182
Core,49
data, 38
Comish Method, 91
Correlating parameters, 66
Correlations
for holdup factor, 85
forRs ' 78
for secondary correction factor. 85
for viscosity number coefficíent, 85
for pipeline flow prediction. lO8
Corrosion,61
Cricondenthenn, 20
Critical
flow {sanie), 123. 124, 125, 141, 142, 153
gas saturation. [8
pressure drop, 143
pressure ratío, 124. 125
ratio of downstream to upstream pressure,
124
regime, 124
temperature, 20
Crude oil, 66,72
viscosity, 66
Crushed zone. 50
permeability. 5)
damage,48
Cul1ender and Smith method, 97
Cumulntive oil production, 150. 151
data, 150
increment, 150
recovery, 18
Damaged well, 20
Damaged-zone penneability, 51
Darey flow, 35,48
Darcy's
equatíon, 30
equation for radial gas flow, 43
law,9, ID, 11, 14,21
Darcy-Wiesbach thction factor, 60
Daca banlc, 114
Dead ni1 interfaciai tension, 81
Declining production rate, 95
Deep welIs, J60
Deganee aod Atherton f10w pattern, 108
Degree
of scatter, 92
of s\ippage, 66
Deliverability, 1, 150, l63
Density, 5, 57, 64, 65, 67, 73, 75, 87, 96, 100,
176,180,182,191
air, 87
calcu1ating, 66
changes,65
definition, 65
gas/liquid mixture, 66
oil,75
tenn, 66,111
two-phase, 65
water, 15, 87
Depletion, 40, 46, 54, 55, 61,148,155
depletíon parameters
gas/oil ratio, 148
gaslliquid ratio, 148
water cut, 148
type field, 93
Depth axis, 100
Design
gradient, 168, 169
method, t63
liquid rate, 162
rnethods, 98
procedure, 174
safety factors, 165
surface pressure, tubing load. 169
Designing
t1owtines, 1 04
long distance pipelines, 104
Determining
maximum tubing size, 96
producing cap3clry, 151
Development planning, ! SO
Deviated wells, 90
Dewpoint pressure. 15,20
Diameter, 51
Dimensional analysis. 61. l11
lndex
Dimensionless
flow rate, 21
groups,
Reynolds number, 7 \
Grashof number, 71
Prandtl number, 71
IPR. 21, 22
curves, 21, 26
numbers, 66, 85, 86, 97,109,19[,192
pressure, 21
ratio, 22
slip velocity, 86
Direction of flow, 68
Directional well, 90, 93, 98, 104
Directionally drilled wel1s, 90, 97, 174
Discharge
coefficiem, 123, 124, 127
pressures, 175
Dispersions, 95
Dissolved gas, 80, 175
drive, 18
drive mechanism, 18
drive performance, 18
Dissolved or solution gas calculation, 77
Dissolved solids, 80
Dividíng well into short increments, 96
Division point (node), 2
Dome pressure, 165, 166, 169
Downhill flow, lIS
Downhole, 165
Downstream, 153
components, 2, 133
conditions. 125
gas density, 124
pressure, 123, 125, 126, 127, 128, 141,
142,143,153,172
Downward
flow, 64, 68, 69, 89
incUnation, 109
mavement, 87
Drainage
area, 19, 150
radius, 12, 14
Drawdown, 9,14,17,20,21, 24,34,54
actual, 26
effect, gas wells, 54
ideal, 26
rate, 19
test, 45
Drew, Koo and McAdams equation, 60, 61,62
OríU stem test, 36, 144
Orive mechanism, 9, J7
Dry gas, 97
reservo ir, 21, 47
wells,82
DST analysis, 144
Oukter, et al., Method, 109, 110
Dukler
correlatian, ¡ 17
frictíon factor cOrTelatíon, ! 12
liquíd holdup correlation, 112
method,111
Dukler-Eaton
correlation, 1[4
method, 114
Duns and Ros method, 86, 87, 98
Eatan correlation, 114
for fríction factor and liquid holdup, 109,
111
Eaton, et al., Method, 109, ¡ 10
Eaton liquid holdup correlation, 1[1
Economic evaluarion, 150
Effect of
compressor pressures, 146
depletion, 20, 148
on pressure profile, 21
on [PR,21
downhole separator, 176
final outlet pressure, 152
flow rate, 116
flowlines on well performance, 118
flowline sizes, 146
gas injection rote, 146, 157
gaslliquid ratio, 94, 116
gas rate, 94
gravity, on liquid, 67
injection depth, 157
injeccian rate, line diameter, 117
negative skio, 20
perforating density, 144
pipeline angle 00 flow partern, 109
positive skin, 20
stimulation, 139, 140
tubing size, 96, 135, 146
on minimum production rate, 96
on injection rate,
turbulence,43
upper string size, 137
variables on pipeline performance, 116
viscosity, 95
water cut on required flowing pressure,
94,95
Effective
mixture viscosity, ¡ 17
permeability, 15,47
stimulation, 140
viscosity, 65
Efficiency factor, 113,117
Ekofisk field, North Sea, 90
Electric submersible pumps (ESP), 153, 174
Elevation
change, 63, 65
component, 66, 116
component, 83, 91,98, 108, 112
Emperícal
correlation, 65, 66, 68, 83, 84, 91,114,191
fluid property correlation, 73, 76
enthalpy correlation, 72
methods,73
Emulsioos, 95, 117
Energy balance, 58
equation, 59, 69
Energy loss, 60, 84
Energy of expansion or compression, 58
Engineering eguation of state for a gas, 75
English system ofunits, 123
Enthalpy, 59
change, 8Z
gradient, 69
specific, 69
Entropy,59
Equation for calculacing gas in solution in
Water, 79
403
Equation for estimating minimum gas produc-
ing rate, 97
Equivalent length concept, 128
Erosion, 61. 129
Erosional
flow rate, 129
velocity, 129
velocity eguation, 129
ESP, 176
ESlimating flowing temperature, 82
Evaluatíng
completion etTects, 143
correlations, 91
usiog field data, 91
pipe flow correlations, ¡ 14
EvalualÍon srudies, 93
Expansion factor, 127
Fanning equation, 60
Fetkovich
equation, 34, 40
method, 30, 37, 42, 142
present and future IPRs, 42, 43
Field data, 91, 92, 93, 98, 114, 115, 116
Field producing capacity, 151
Final autlet pressure, 152
Finding optimum rubing size, 5
Fitting
type, 128, 129
size, 128
Flanigan
efficiency factor, 113
equation, 113
method, 111,112,118
Flow
capacity, 3, 122, 135, 140
characteristics,
laminar, 71
transitían, 71
turbulent, 71
coefficient e, 42
conditions, 83
conduit,67
critical, 123
direction of, 68
diversion, 122
efficiency, 26, 29, 47,140, 141
gas,
two-phase, 123
geometry, 11, 60, 83
in casing, 176
in directional wells, 97
in gas wells, in pipelines, 108
inclined downward, 67
inclined upward, 67
non-steady, 71
of gases, 82
parameters, 90
panem, 65, 66, 67, 7[, 72, 83, 84, 85, 86,
87,88.90,97,108,109,114,117,192,
193,194,195
bubble regime, 66
descríptions for vertical air/water flow,
67
descriptions for horizontal air/water
flow, 67
map, 84,86, 108
404 Produclion Optimization Using Nada/ Ana/ysis
mist,67
existing, 67
expected, 67
horizontal tlow, predicting,
vertical f1ow, predicting, 67
period, <1-3
rate, 2,3,7,9,13,21,24,43,49,65,73,
75,82,83,84,85,88,91, IDO, [04,
[16,ln,123,124,126,12~133,137,
141, 143, 144, 145, 167, 194
through choke, 124
total in-situ, 66
in-situ,76
standard, 76
regirr:e,9
resistance, ¡44
splitting problem, 122
steam, 64, 65
stream, 109, 152
subcritícal, 123
tests, 31
after·flow, 30, 31. 32, 33. 34, 43
Flowing
bottom.hole pressure, 24, 94, 100, 102, 104,
162,163,174,183
Quid, to, 14,69,70
temperature, 165
viscosity, 66
gasllit¡uid mixture, S
density, 65
gradient, 163, 168
load fluid gradient curve, 1fi3
performance, 93
pressure, 31
pressure traverses, production wel1s, 146
temperature gradient, t67
temperature in pipelines, 82
temperature in wells. 82
temperamre profile, 81
temperatures, 81
test, 102
tubing prcssure, 160, 163
tubing pressure traverse, 163, 173
wellbore pressure, 9, 24, 21, 31, 98, 155
weUs, 141, t55, 15R
F1owline, 104, 114, 123, 136, 141, 142, t43,
156,114,178
diameter, 139
pressure drop, 137, l56
calculations, 174
requirements, 158
size, 14, 1I8, L37, 139, 146, 158
size effect, 136, 137
too large, 136, 137
too small, 136, 137
Fluctuating tlow, 65
Fluid
co1urnn, 1RO
density, 72, 73, 75, 83, 129
tlow equations, 58
gradient traverse, 163
[evel, [60, 179, 180
mixture, 180
operated va[ves, 165
phase, 65
superficial velocity, 65
physical properties, 81,125
properties,9, 15,41,57,64,67,68,69,78,
84,98, 192
t:valualion, 127
oil grav\ty, 66
gas gravity, 66
dissoLved gas, 66
calculations, 72
correlalion, 81, 88,194
data,
PVT properties, 75
5ample, 36, 98
analysis, 4 t
~aturation, 9
lemperature, 70, 81, 175
ve[ocity, 4, 5, 9, 64, 72, 76, 93, 100
viscosiry value, 80
Folds of inerease, 26
Force balance, 60
Formation, 162
damage,9,14,17,30,48,49,54,55,lJ5
clay swelting, 14
gas welIs, 14
pore plugging, 14
gaslliquid ratio, GLR, 156, 158, 162, 168,
172, 174
stimulation, 9
thickness, 45, 51
volurne factor, 76,79, 125, t76
brine in contact with gas, 79
Fraction of oil flowing, 125, 175
Fracüon ofwater tlowing, 125
Fmcturing, 139
Free gas, 15, 18, 37, 57, 94,175,176
flow rate, j6
saturation, 19
Friction, 59, 60. 104, 112, 116, 156, ¡58
component, 67, 83, 94,112
factor, 60,.61, 62, 64, 67, 72, 83. 84, 86.
90,91,95,108,109,110,117,191,195
comparison study, 114
correlatian, 67, 84, 85, \09,114
equation, 90
for pipe flow, 61,62,128
prediction, 114
two~phase, 67,89
loss, 5, 37, 59, 60, 63, 65, 68, 80, 83, 93,
98,113,116,128,135,156
component, 64
in annulus, t58
methods, 113
pressure drop, 95,117,139,143,180
component, [14
tenn, 84,93, 104, 117
pressure 10s$ in pipelines, t08
Future gas well performance, 150
Future IPRs, 41
Gagc pressures, 22,43
Gas bubble 180
velocity, 87
Gas cap, 19
drive, 18
perfonnance, 18
reservoir,18
Gas
compressibiliry, 127
factor, 45, 76, 77,129, 158
eompression, ¡58
conCensate pipeline, 1t2
coning,37
density, SO, 81, 124, 125
deviation factor, 97
equatlOD
of state, 96
to express density, 129
flow, JI, 12, D, 123. 127
equation,47,123
rate, 76, 88, l22. 12.7, t29
fOnTI;ltion volume factor, 76, 79
calcuation, 79
gravity,78, 79. 80,82,97,98,127,129
correction cquation, 78
holdup,65
in-situ
t10w rate, 65
velocity, 76
injection, 19,94,147, J56
pressure, 155
rate, 5, 6, [48, 156, l57, 158, 16S, 169
surface pressure, 160
wells, 146
¡ift,94, 102, \ 53, 155, 158, 173
valve, 155, 160, 162, 163, 165, 167
design, 165
dome pressure, 1 71
performance, 165
well, 116, 137, 155, 156
analysis, 157
schematic, \56
Une pressure drop, 117
tiquid
flow, 117, 124
mixture density, 66
viseosity, 95
ratio (GLR), 38, 83, 85, 93, 94, 96, 116,
117,122, 124, 148, 149, 152, 155,
174
mass flow rate, (24
oil
eontact, 19
interfacial tension, 81
mixture, 81
viscosity,9S
oiVwater viseosity, 95
ratio, 93, [48,150,158
phase, 64, 66, 86, 87, 9 t
pipeline equations, 117
pressure, 160, 162. 172
productivity index, 13
properties, 65, 124
rate, 88,109,112.115,123.137,149,180
relative penneability. 15
reservQir, 15,46
equ3tions. 14<1-
Reynotds number. 122
saturation, 15,20,30,37, 39,40,-l1, 47,54
separation, 174
single·phasc tlow, 57
specific gravity, \0, 75, I~J. 125
splitting, 122, 123
storage
operations, 147
reservoirs. 146
superficial velocities, 87
lndex
veiocity, 85, 90, lDS, 112, 113, 117
superficial, 76
viscosity, 47, 80,122,191
yoid fmetion, 65
cOrTelatían, 90
vo!ume, 157, 173
water interfacial tcosian, 81
weight, 162, 182
well, 49, 54, 81, 82, 83, 96,97,149
backpressure equatían. 146
predicting future IPRs, 43, 47
Gas·free viscosity, 80
Gas-liquid
ratio, 126
wells, 129
separatían, 174
Gas-oiL relative penneability data, L7
Gas-producing rates, 76
Gas~well testing, 31
Gas/liquid mixture, 72
Gathering
Iines, 104
system, 122
General energy eguatían, 58
General equation for flow through restne-
tioos, 123
General eguatían for frietían factor, 114
General inflow equations, 47
General pressure gradient equation, 96, 97,
108
General pressure traverse curves, 104
Generalized curves, 98
Generating LPR, 155
Geometry for linear flow, 11
system, la
Geothermal gradient, 82, 167
Gilbert's "5" curve, 180
GLR, 84, 97, 98,100,102,104, !l8, 140,153,
163,172,176,177
curve, 100
maximum value. 98
Gradient curves, 98, 168
Graphical solution for valve spacing, 162
Grashof number, 71
Gravel pack, 9, 53, 54, 144, 145
analysis,
producing capacity, 144
system pressure drop, 144
completion, 11,53,47, 143
equations, 53
resistance, 144
gravel penneability, 53,144
wells,53
Gravitational separation, 65
Gravity.
effect of. 67
of stock tank oil, 81
Gray method, 97
Gregory, et aL, correlations, 114, ¡ 16
Griffith correlation, 86
Hagedom and Brown. 86
correlation, 93, 98
method, 85, 93, 98, 191
lbe study, 93
Hagen-Poiseuille equarian for laminar flow,
60
Hand calculations, 68
Handheld, prograrnmable calculators, 89
Hasan and Kabir method, 90, 98
Head gain, 176, 177
Heat
balance equation, 69
energy, 58
loss, 57,81,82
conductive 71
convective, 70
gradient, 70
transfer, 65
calculation algorithm, 73
calculations,