- 1 b
L
2
- 3 b
L
3
- 1 b
L
4
- 1 b
L
5
L
Fakto F =
f Tingg
Static
Veloc Press
-W
s
=
Efisie Tenag
Maka
11. Pomp
buah gate va = 1 x 13 x
buah elbow = 3 x 30 x
buah sharp e = 1 x 32 x
buah sharp e = 1 x 65 x
L = L
1
+ L
2
= 80 ft + 4 = 133,86 f
or gesekan, f × v
2
×
∑
L 2 g
C
×D gi pemompa
c head
, ∆z
g g
city head,
∆ 2
ure head
, ∆
= ∆z
g g
c
+ ∆
2 = 10 + 0 +
= 346,61 ensi pompa
a pompa, P a dipilih pom
pa Diffuser
alve fully op 0,31 ft = 4,
standar 90
o
0,31 ft = 28 edge entran
0,31 ft = 3, edge exit K
0,31 ft = 17 + L
3
+ L
4
+ 4,14 ft + 28
ft
L =
0,0045 2 3
aan, z = 1
g g
c
= 10 ft.lb ∆v
2
2 g
c
= 0 ∆P
ρ =
2850 ∆v
2
2 g
c
+ ∆P
ρ +
+ 336,03+ 0 ft.lbflbm
= 80
= -W
s
×Q 550 ×0
mpa dengan
Washer J
pen LD=1 14 ft
o
C LD = 3 8,68 ft
nce K=0,5 ; 50 ft
K=1 ; LD = 7,52 ft
+ L
5
,68 ft + 3,5
5× 2,51
2
×1 32,174 ×0,
10 ft bflbm
01,92 -2.116 78,52
F 0,58
× ρ
0,8 =
346, n tenaga 12,
J-201
13
30
; LD = 32
= 65
50 ft + 17,5
33,86 ,31
= 0,
6,23 = 336
,61 × 0,20 × 550 ×0,8
37 hp ≈ 12,
52 ft
58 ft.lbflb
6,03 ft.lbflb
× 78,52 8
= 1 5 hp
bm
bm
Peters et.al 2,37 hp
l., 2004
Universitas Sumatera Utara
Fungs
Jenis Jumlah
Bahan Kondi
- Laj - De
- Vi
- Laj
- Te
- Te
Perhit Asum
Peren Asum
Diam De
Digun Ukura
Sched
Diam Diam
Inside
kecep V = Q
N
Re
= =
= Asum
i
h n kontruksi
isi operasi: aju alir mass
ensitas camp skositas cam
aju alir volum ekanan masu
ekanan kelua
tungan: msi aliran tur
ncanaan pom msi N
Re
21 meter pipa ek
= 3,9 Q = 7,07 in
nakan pipa d an nominal
dule number
meter Dalam meter Luar O
e sectional a
patan rata-ra QA
i
= 1,13 =
VD = 63,91 .3,5
= 276922,59 msi N
Re
21 : memomp
Blow Tan
:
Positive d
: 4 unit :
Commerc
sa puran umpa
mpuran metrik Q
uk P
1
ar P
2
rbulen, mak mpa
100, aliran tu konomis, De
0,36
ρ
0,18
dengan spes : 8 in
r
: 80 ID
OD
area
A : 0 ata, V:
ft
3
s 0,317
57. 0,6350 9 aliran turb
100 sudah b pa
Unbleach nk
V-202
displacemen
cial Steel
= 1183 an =
1023 = 0,78
= F
ρ = 30,5
= 47,8
ka diameter
urbulen e:
sifikasi :
: 7,625 : 8,625
0,3171 ft
2
71 ft
2
= 3,5
0,00052 bulen
enar.
hed Pulp
da
nt Rotary P
327 kgjam 3,78 kgm
3
8 cp ρ
52 psi 83 psi
pipa pompa
5 in = 0,635 5 in = 0,718
7 fts ari
Diffuser
Pump
= 72,4
= 63,9
= 0,00 = 1,13
= 4394 = 6887
a :
Walas, 19
Geankoplis
5 ft = 0,193 8 ft = 0,218
Washer
V
46 lbms 91 lbmft
3
0051 lbmft. 3 ft
3
s = 0,03 4,88 lbfft
2
7,52 lbfft
2
990
s,1997
m m
V-201 ke
.s 32 m
3
s
Universitas Sumatera Utara
Untuk Pada N
dipero Instal
- Pa
- 1 b
L
2
- 3 b
L
3
- 1 b
L
4
- 1 b
L
5
L = =
= Fakto
F = f
Tingg
Static Veloc
Press
-W
s
=
Efisie Tenag
k pipa
Comm
N
Re
= 27692 oleh harga f
asi pipa Fo anjang pipa
buah gate va = 1 x 13 x
buah elbow = 3 x 30 x
buah sharp e = 1 x 32 x
buah sharp e = 1 x 65 x
L
1
+ L
2
+ L 50 ft + 8,26
177,04 ft or gesekan,
f × v
2
×
∑
L 2 g
C
×D gi pemompa
c head, ∆z g
city head, ∆
ure head
, ∆
= ∆z
g g
c
+ ∆
2 = 10 + 0 +
= 49,26 ft ensi pompa
a pompa, P
mercial Stee
22,59 dan ε
faktor
fanni
oust,1980 : lurus, L
1
= alve fully op
0,635 ft = 8 standar 90
o
0,635 ft = 5 edge entran
0,635 ft = 2 edge exit K
0,635 ft = 4 L
3
+ L
4
+ L
5
6 ft + 57,15
L =
0,0048 2 3
aan, z = 1
g g
c
ft. ∆v
g
c
∆P ρ
= 6887
∆v
2
2 g
c
+ ∆P
ρ +
+ 39 + 0,26 ft.lbflbm
= 80
= -W
s
×Q 550 ×0
el
, harga ε =
εD = 0,0000
ing,
f = 0,00
50 ft pen LD=1
8,26 ft
o
C LD = 3 57,15 ft
nce K=0,5 ; 20,33 ft
K=1 ; LD = 41,30 ft
5
ft + 20,33
8 × 3,57
2
× 32,174 ×0,
10 ft
lbflbm
7,52-4394,8 63,91
F 6
× ρ
0,8 =
49,2 = 0,000046
046 m 0,6 048 Fig.2.1
13
30
; LD = 32
= 65
ft + 41,30
177,04 ,635
= 0
88 = 39 ft.l
26 ×1,13 × 6 550 ×0,8
m Geanko 35 m = 0,00
0.3 Geank
ft
0,26 ft.lbfl
bflbm
63,91 = 8,0
oplis, 1997 00072
koplis, 1997
lbm
Peters et.al 08 hp
7
l., 2004
Universitas Sumatera Utara
Maka
12. Pomp
