Pivot Rol
Pivot Rol
Capacity lb/h When installed with recommended filling head above A. Pump capacity if filling head is 24": 1.16 x 6,935 = 8045 lb/h
Recovery
top of pump. B. Pump capacity using compressed air: 1.12 x 6,935 = 7767 lb/h
(% back pressure is 38—75=50%)
Motive Steam
Non-Electric
Pump
Exhaust
Condensate
Condensate
Return
Line
Return
At least
12" Seal Vented
on overflow Receiver (open system)
Recommended
Filling Installation
Head
The pump is fitted with
vented receiver or an inlet
reservoir.
Details of the application
will determine whether a
vented receiver or an inlet
Pressure reservoir will be needed
Filling to accomplish this.
Height Powered TD 42L or 52L Trap
Pump when steam supply is used
Local regulation may restrict the use of this product below the conditions quoted. Limiting conditions refer to standard connections only.
In the interests of development and improvement of the product, we reserve the right to change the specification. TI-5-030-US 4.13
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The Pivotrol® Pump Patented
Selection and Sizing
Vented Receiver (Open System) Inlet Reservoir Piping (Closed System)
To drain condensate from a single or multiple source an "open" system, a vented To drain condensate from a single piece of equipment in a "closed"
receiver should be installed in a horizontal plane above and ahead of the pump. system, a reservoir should be installed in a horizontal plane above and
Sufficient receiver volume is needed above the filling head level to accept the ahead of the pump. Sufficient reservoir volume is needed above the
condensate reachng the receiver during the pump discharge stroke. More filling head level to accept the condensate reaching the reservoir during
important, the receiver must be sized to allow sufficient area for complete flash the pump discharge stroke. The chart below shows minimum reser-
steam separation from the condensate. The chart below shows proper vented voir sizing, based on condensate load, needed to prevent equipment
receiver sizing (per criteria set forth in the A.S.H.R.A.E. Handbook) based on the flooding during the pump dischare stroke. The reservoir can be a length
amount of flash steam present. If the receiver is sized as shown below, there will of large diameter pipe or a tank.
be sufficient volume for condensate storage and sufficient area for flash steam
separation. The receiver can be a length of large diameter pipe or a tank.
Condensate
7000 3’ 2’
Recovery
8000 4’ 2’
9000 4.5’ 3’ 2’
10,000 5’ 3’ 2’
11,000 5’ 3’ 2’
Non-Electric
Flash Steam Pipe Size Vent Line
Pumps
Liquid Load Reservoir Pipe Size*
up to – Diameter Length Diameter lb/h 12" 16" 20" 24"
1000 lb/h 16" 60" 6" 10,000 5’ 3’ 2’
2000 lb/h 20" 60" 8" 20,000 10’ 7’ 4’
3000 lb/h 24" 60" 8" 30,000 9’ 6’ 4’
4000 lb/h 26’’ 60" 10" 40,000 12’ 7.5’ 6’
5000 lb/h 28" 60" 10" 50,000 9’ 6’
6000 lb/h 30" 72" 12" 60,000 9’ 6’
7000 lb/h 32" 72" 12"
* When BP/MP is less than 50%, these reser-
8000 lb/h 36" 72" 14" voir lengths can be reduced by 1/2.
Capacity Multiplying Factors for other Filling Heads Capacity Multiplying Factors for Motive Gas Supply
(other than steam)
Filling Head Check valve and piping size, pump type
Inches mm 2" x 2" 3" x 2" 2" and 3" x 2" PTC / PTF
PTF-HP PTF4 % Back Pressure
PTC/PTF PTC/PTF
10% 20% 30% 40% 50% 60% 70% 80% 90% VS. Motive Pressure
(bp / MP)
-3.0 -76 0.47 NA NA 0.23
-1.0 -25 0.66 0.40 NA 0.41 Capacity
1.04 1.06 1.08 1.10 1.12 1.15 1.18 1.23 1.28 Multiplying
0.0 0 0.76 0.43 0.6 0.70 Factors
6.0 152 0.90 0.69 0.9 0.89
PTF-HP
12.0 305 1.00 1.00 1.0 0.95 Capacity
18.0 457 1.08 1.02 1.1 0.98 1.19 1.43 1.43 1.53 1.85 2.04 2.14 2.20 2.44 Multiplying
24.0 610 1.16 1.04 1.2 1.00 Factors
36.0 914 1.38 1.17 1.3 1.00 PTF4
48.0 1219 1.48 1.25 1.4 1.08 Capacity
60.0 1524 N/A N/A 1.5 1.20 Multiplying
1.19 1.43 1.43 1.53 1.85 2.04 2.14 2.20 2.44 Factors
Local regulation may restrict the use of this product below the conditions quoted. Limiting conditions refer to standard connections only.
In the interests of development and improvement of the product, we reserve the right to change the specification. TI-5-030-US 4.13
3:275
The Pivotrol® Pump Patented
Selection and Sizing
Motive Back 2" x 2" 3" x 2" PTC/PTF 3" x 2" Motive Back 3" x 2"
Pressure Pressure PTC/PTF 3" x 3" PPF Top PTF-HTF Pressure Pressure PTF-HP
psig psig 12" Filling Head lb/hr 12" Filling Head lb/hr 12" Filling Head lb/hr psig psig 12" Filling Head lb/hr
200 180 - - - 300 200 12550
200 160 - 5250 3518 300 185 13875
200 140 6375 7375 4941 300 160 14565
200 120 7375 9440 6325 300 140 15750
200 100 8250 11145 7467 300 120 17125
200 80 9000 12565 8419 300 100 19125
200 60 9685 14260 9554 300 80 20315
200 50 10000 14875 9966 300 60 22065
200 40 10310 15690 10512 300 40 24375
200 30 10635 16310 10928 300 20 27500
200 20 10950 17000 11390 300 10 28750
200 10 11195 17640 11819 280 200 11125
180 160 - 3750 2513 280 180 12435
180 140 5425 6335 4244 280 160 13250
180 120 6685 8555 5732 280 140 14435
180 100 7760 10375 6951 280 120 16875
180 80 8600 11980 8027 280 100 17875
180 60 9450 13625 9129 280 80 19125
180 50 9830 14375 9631 280 60 20850
180 40 10230 15150 10151 280 40 23125
180 30 10560 15875 10636 280 20 26125
180 20 10895 16665 11166 280 10 27565
180 10 11195 17505 11728 250 200 9190
160 140 4250 4860 3256 250 180 10185
160 120 5750 7500 5025 250 160 11000
160 100 7040 9375 6281 250 140 12190
160 80 8065 11135 7460 250 120 13935
160 60 9105 12940 8670 250 100 15935
160 50 9565 13750 9213 250 80 17065
160 40 9990 14565 9759 250 60 19000
Condensate
Local regulation may restrict the use of this product below the conditions quoted. Limiting conditions refer to standard connections only.
In the interests of development and improvement of the product, we reserve the right to change the specification. TI-5-030-US 4.13
3:276
The Pivotrol® Pump Patented
Selection and Sizing
Motive Back 36” Fill Head
Pressure Pressure (70” Fill Height)
psig psig lb/hr
200 150 22120 To size the PTF4 in a closed system:
200 140 22970 Establish available motive pressure.
200 120 24870
200 100 27110 Establish static back pressure on Pump/Trap combination.
200 80 29860 Place established pressures in formula below:
200 60 33400
200 50 35640
• Pump Motive Pressure (psig) – min. VAV delta P (psig) > Back Pressure (psig)
200 40 38390
200 30 41930 • Capacity charts to be read as normal, i.e. at pump motive and back pressure.
200 20 46920 • If, Pump Motive Pressure (psig) – min. VAV delta P (psig) < Back Pressure (psig), then
200 15 50460 isolate or remove VAV and multiply capacity by 0.77 to find reduced capacity without VAV.
180 120 23700
180 100 26020
180 60 32500 Sizing Example: 1
180 50 34810 A closed system has the following conditions:
180 40 37640 Motive steam available = 150 psig. Static Back Pressure = 45 psig.
180 30 41300
180 20 46440
180 15 50090 Open System.
160 120 22530 PTF4
160 100 24920
160 80 27830
160 60 31590 Capacity charts show capacity at 150 psig motive with 45 psig back pressure.
160 50 33980
160 40 36890 Closed System.
160 30 40660
160 20 45960 The Vent Assist Valve on the PTF4 requires at least 75 psig differential
160 15 49720 pressure to operate in a closed system.
140 100 23410
140 80 26220
Condensate
To size the PTF4 pump:
Recovery
140 60 29850
140 50 32150 Pump Motive Pressure – min. VAV delta P > Back Pressure.
140 40 34960 150 psig – 75 psig > 45 psig
140 30 38590
140 20 43710
140 15 47340 As the motive pressure is 150 psig and the VAV requires a minimum 120 psig to operate
120 80 24610 (75 + 45 = 120), this combination is sized correctly.
120 60 28110
120 50 30320
Non-Electric
120 40 33030
Pumps
120 30 36530
120 20 41460
120 15 44950
100 60 24730
100 50 27100
100 40 30010
100 30 33750
100 20 39030
100 15 42780
80 60 21350
80 50 23880
80 40 26980
80 30 30970
80 20 36610
80 15 40600
70 50 21850
70 40 24830
70 30 28680
70 25 31120
70 20 34110
70 15 37960
60 40 22940
60 30 26840
60 25 29310
60 20 32330
60 15 36230
50 30 25310
50 25 27970
50 20 30910
50 15 34160
40 30 19480
40 25 22230
40 20 25600
40 15 29940
30 20 20440
30 15 25650
TI-5-030-US 4.13
Local regulation may restrict the use of this product below the conditions quoted. Limiting conditions refer to standard connections only.
In the interests of development and improvement of the product, we reserve the right to change the specification.
3:277
The Pivotrol® Pump Patented Selection and Sizing
Capacity Charts 2" x 2" Pivotrol® Pump
0 0
10 10 P S IG 10
B a ck
20
P ress 20
20 P S ure (
IG B 23ft
30 a ck ) 30
30 P P re
S IG s
40 40 B ac s ure 40
PS kP (4 6
IG re s ft)
50 50 P B ac su r 50
S IG kP e (6
Ba res 9ft)
60 60 P ck su r 60
S IG P re s e (92
70 B ac sur ft) 70
kP e (1
res 16
80 sur ft) 80
80 P e(
S IG 1 39
Ba ft)
ck
100 P re 100
100 ssu
PS re
110 IG ( 18 110
Ba
ck 5ft
120 P re ) 120
120 s s
PS u re
130 IG (23 130
Ba 1f
140 ck t) 140
140 P r
PS e s
150 IG su 150
Ba re
ck (27
160 Pr 7f 160
es t
su
)
170 re 170
( 32
Condensate
3f 180
Recovery
180 t)
190 190
200 200
11500
2000
6000
10500
2500
6500
5000
9000
4500
11000
3500
9500
1500
3000
4000
5500
7000
500
8500
10000
12000
7500
8000
1000
lb/hr
(1) (2) (3) (4) (5) (6) (7) (8) (9) (10) (11) (12) (13) (14) (15) (16) (17) (18) (19) (20) (21) (22) (23) (24) (GPM)
Non-Electric
Pumps
10 10
10 P S IG
B a ck P
20
20 P S IG re ssur 20
B a ck P e (23ft
30 re ssur ) 30
30 P S IG B e (46ft
ack P re )
40 ssure (6 40
40 P S IG 9ft)
B a ck P
50 50 P S IG re ssure 50
B a ck (92ft)
60
60 P S IG P re ss 60
B a ck P u re (116f
70 re ssu t) 70
re (13
9ft)
G
80 80
G
80 P S
90 IG B a 90
ck P r
Motive Pressure PSI
e s su
100 re (1 100
100 P 85ft)
110 S IG 110
B ac
k Pr
120 e ss 120
120 ure
PS (23
130 IG B 1 ft) 130
ack
140 140 P S P re 140
IG B ss u
150 ack re 150
P re (27
160 6
1 0P s s 7f 160
S IG u re
B ac (32
t)
170 170
kP 3f
res t)
180 sur 180
e (3
190 70 190
ft)
200 200
10500
16500
14500
15000
11000
12500
15500
11500
12000
13500
14000
17500
16000
13000
17000
2500
3500
4500
5500
6000
7000
8000
8500
9000
9500
3000
4000
5000
6500
7500
2000
10000
lb/hr
(4) (5) (6) (7) (8) (9) (10) (11) (12) (13) (14) (15) (16) (17) (18) (19) (20) (21) (22) (23) (24) (25) (26) (27) (28) (29) (30) (31) (32) (33) (33) (34) (GPM)
Local regulation may restrict the use of this product below the conditions quoted. Limiting conditions refer to standard connections only.
In the interests of development and improvement of the product, we reserve the right to change the specification. TI-5-030-US 4.13
3:278
The Pivotrol® Pump Patented Selection and Sizing
20
40
60
Motive Pressure PSIG
80
100
120
140
160
Condensate
Recovery
180
200
14,000
16,000
18,000
20,000
22,000
24,000
26,000
28,000
30,000
32,000
34,000
36,000
38,000
40,000
42,000
44,000
46,000
48,000
50,000
52,000
Non-Electric
Pumps
Capacity, lbs/hr
Local regulation may restrict the use of this product below the conditions quoted. Limiting conditions refer to standard connections only.
In the interests of development and improvement of the product, we reserve the right to change the specification. TI-5-030-US 4.13
3:279
The Pivotrol® Pump Patented Selection and Sizing
0
20 10
20 P P SIG
40 SIG
40 PS B acB
IG B ack kP
60 ack Pr
es re
MOTIVE PRESSURE (PSIG)
Pre ss
60 ss u s ur
80 PS re e( ur
IG (92 46 e(
80 Ba ft) f t )
23
100 PS ck ft)
IG Pr
10 Ba e s
120 0P ck su
re
SI Pr (1
140 12 B G e ss 39
0 ac ur ft)
160 PS k P e
re (1
IG s 85
Ba sur ft
180 ck e( )
1
18 60 1 P 2 3
200 0P P 40 re 1ft
SIG SI PS ss )
ur
220 Ba G B IG
Ba e
ck ac (2
Pr k P ck 77
es r P f t)
240 20 ure essu ress
s
PS 416 re (3 ure
0 (
260 IG ft) 70 (32
(4 ft) 3ft
280 6 2 )
ft)
300
10,000
12,000
14,000
16,000
18,000
20,000
22,000
24,000
26,000
28,000
30,000
1,000
2,000
4,000
6.000
8,000
(lb/hr)
Condensate
Recovery
(2) (4) (8) (12) (16) (20) (24) (28) (32) (36) (40) (44) (48) (52) (56) (60) (GPM)
CAPACITY
•
Pumps
• insulation
PTF - HP without PTF - HP with insulation
14
13
12
•
11
Steam used per 1000lbs water
10
• •
9
•
8
• •
•
7
6
•
5
• •
•
4
3
2
•
1
0
0 10 20 30 40 50 60 70 80 90 100 110 120 130 140 150 160 170 180 190 200
3:280
The Pivotrol® Pump Patented Selection and Sizing
Condensate
Recovery
Non-Electric
Pumps
© Spirax Sarco, Inc. 2013
TI-5-030-US 4.13
Spirax Sarco, Inc., 1150 Northpoint Blvd, Blythewood, SC 29016 Telephone: (803) 714-2000 FAX (803) 714-2222
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