Peerless HORIZONTAL SPLIT CASE PUMPS SINGLE STAGE DOUBLE SUCTION Specifications

Peerless Pump Company
Indianapolis, IN 46207-7026
HORIZONTAL SPLIT CASE PUMPS
SINGLE STAGE DOUBLE SUCTION

Typical Specifications

1. General: The pump(s) shall be of the single stage, double
suction, horizontal split case design; split on the horizontal axis and shall be bronze fitted construction. Suction and discharge connections shall be located on opposite sides of the lower casing, allowing removal of the rotating element without disturbing the system piping connections. The pump(s) shall be a Peerless Pump Company AE design.
The pump(s) are to be designed for a capacity of at an efficiency of
2. Casing: The pump casing material shall be a minimum of class 35 cast iron. Water passageways shall be smooth to permit maximum efficiency. Casing shall be hydrostatically tested at 150% of the maximum working pressure under which the pump could operate at design speed. The suction flange shall be drilled (125 lb.) (250 lb.) ANSI. The discharge flange shall be drilled (125 lb.) (250 lb.) ANSI
The bearing brackets shall be cast as an integral part of the lower casing and have removable bracket caps. The bearing housing shall be doweled for location and anti­rotation. The pump feet shall also be cast as an Integral part of the lower casing.
Bronze renewable casing rings shall be furnished, doweled and shouldered In the casing. Ring dowels shall be located In slots on the split surface of the lower casing.
3. Impeller: The impeller shall be of one piece cast bronze, double suction type. The impeller shall be balanced, keyed to the shaft and fixed in an axial position by threaded shaft sleeves. The Impeller skirt shall be grooved and fit with close tolerances to the casing ring to permit a minimum of recirculation between the impeller and the casing ring for maximum efficiency. (Optional: Renewable bronze impeller rings shall be shrunk on the impeller and locked in place with stainless steel set screws. The impeller rings shall be grooved and fit with close tolerances to the casing ring for maximum efficiency.)
4. Stuffing Boxes: Packing - The stuffing boxes shall hold a minimum of
five rings of TFE packing. The bronze gland shall be split in two halves, to facilitate removal for repacking. Gland bolts shall be of the swing type made of steel with 18-8 stainless steel nuts.
Mechanical Seal - Sealing of the pump liquid cavity shall be with a face type mechanical seal with Ni-resist stationary seat, carbon sealing washer, Buna rubber flexible members, stainless steel metal parts and spring.
Seal to be rated for 225o F .(107o C.) @ 150 psig (10-34 bar) maximum. Mechanical seals shall be mounted over bronze shaft sleeves.
GPM at a total head of feet,
% of design condition.
SECTION 1220 Page 1
Type AE
5. Shaft and Shaft Sleeves: The shaft shall be carbon steel, adequately sized for the loads transmitted. Shaft deflection shall not exceed .002 Inches at the face of the stuffing box when operating between 95% and 105% of capacity at best efficiency at the pump's maximum 60 Hz. speed and with full diameter Impeller. The shaft shall be protected through the stuffing box by means of bronze shaft sleeves and they shall be threaded against shaft rotationand locked in place with set screws. The sleeves shall be sealed with "O" rings at the Inside diameter to eliminate leakage between the shaft and sleeve. (Optional: Shaft shall be positively sealed against pumped fluid by means of specially machined shaft sleeves and Impeller with sockets for use with "O" ring seals against Impeller hubs.) Shaft sleeves shall extend beyond the packing glands (or mechanical seal flanges).
6. Bearings: Bearings shall be single row, deep groove ball type; the inboard bearing shall be arranged for radial loads only. The outboard bearing shall be arranged for both radial and axial loads. Both bearings shall be grease lubricated with grease flush through the bearing housing (Optional: oil lube). Bearings shall be designed for an average life of 100,000 hours.
Bearings shall be protected from liquid entry by means of rubber deflectors mounted on the shaft and lip seals In the bearing housings.
Outboard bearing cover shall have a plugged opening for tachometer connection. Bearing housing lubrication design must be capable of being changed from grease to oil lubrication type without replacement of bearing housing or the lower pump casing. The outboard bearing shall have retaining ring retention.
7. Base: The pump and driver shall be mounted on a common steel base (with optional drip rim). Pump and driver shall be aligned and bolted In place prior to factory shipment. Final alignment must be performed at the jobsite In accordance with the standards of the Hydraulic Institute and the pump Installation, operation and maintenance instructions. Base Is to be grouted to eliminate vibration.
8. Coupling: A flexible coupling shall be provided between the pump and driver. A coupling guard shall be furnished over the coupling for protection.
Subject to change without notice
SECTION 1220 Page 2 June 1, 2004
HORIZONTAL SPLIT CASE PUMPS
SINGLE STAGE DOUBLE SUCTION
Type AE
Peerless Pump Company
Indianapolis, IN 46207-7026
WORKING PRESSURE AND TEMPERATURE LIMITATIONS
The maximum working pressure of a pump varies with the temperature of the pumped fluid. Tables A and B and Curve 4852154 on page 2.1 Section 1220, present the maximum working pressure and maximum suction pressure
limits for AE model pumps based on available flange drilling, casing material and fluid temperature.
IMPORTANT NOTE
The correct packing type, sleeve material or mechanical seal must be selected in accordance with their application rules. The standard mechanical seals for AE pumps are limited to 150 psig (10.34 bar) maximum suction pressure
and temperature up to 225
o
F. (107
o
C.). To verify that a given model AE pump is suitable for an application, the following steps must be taken. STEP 1:
Calculate the pump's maximum discharge pressure (MDP).
For constant RPM applications:
MDP = [Total Head at Shutoff (for the impeller diameter and RPM required for rated total head) ÷ 2.31 x fluid’s specific gravity] + suction pressure (psi) at zero flow.
STEP 2:
Locate the pump model in Table A and note the legend letter for the applicable pressure-temperature curve for maximum working pressure allowed.
STEP 3:
Locate the pump model in Table B and note the legend letters for the applicable pressure-temperature curve for maximum suction pressure allowed.
STEP 4:
o
Enter Curve 4852154 at the fluid temperature (
F.), read vertically to the curve line noted for the pump suction
and read the maximum permissible suction pressure. Repeat this procedure for the discharge side to determine the maximum allowable working pressure.
STEP 5:
Relate the maximum suction pressure to the pump's permissible suction pressure and choose the suction flange rating required. Repeat for the discharge flange.
EXAMPLE:
o
Model 4AE11, constant RPM, fluid temperature 70
F., suction pressure at 0 GPM = 85 psig, 1.0 specific gravity,
shutoff total head = 231 feet.
MDP = (231 ÷ 2.31 x 1.0) + 85 = 185 psi
4AE11 Discharge flange curve lines are E-E or D-D (from Table A) 4AE11 Suction flange curve lines are E-E or D-D (from Table B)
Maximum suction and discharge pressure for E-E = 175 psi, and D-D = 250 psi @ 70 Therefore: 125 lb. ANSI drilling for suction flange and 250 lb. ANSI drilling for discharge flange is required for cast
iron casing.
o
F
Subject to change without notice.
Peerless Pump Company
Indianapolis, IN 46207-7026
HORIZONTAL SPLIT CASE PUMPS
SINGLE STAGE DOUBLE SUCTION
Type AE
WORKING AND TEMPERATURE LIMITATIONS - Continued
TABLE A
(Maximum Working Pressure)
DISCHARGE FLANGE
Pump Size &
Type 125 LB. ANSI
2AE11 E-E C-C N.A. 3AE9 E-E C-C L-L 3AE14, G E-E D-D N.A. 4AE10, G E-E H-H B-B 4AE11, G E-E D-D N.A. 4AE12 E-E C-C A-A 5AE8, N E-E D-D N.A. 5AE11, G E-E C-C A-A 5AE12 E-E C-C A-A 5AE14, G, N E-E D-D N.A. 6AE11 E-E D-D N.A 6AE12 E-E J-J A-A 6AE14, G, N E-E D-D N.A. 6AE16G, N, V E-E D-D N.A. 6AE18 E-E C-C N.A. 8AE12 E-E D-D N.A. 8AE13 E-E D-D N.A. 8AE15, G E-E D-D N.A. 8AE17A, Q, W E-E C-C N.A. 8AE20, G E-E C-C N.A. 10AE12 E-E D-D N.A. 10AE14A, J E-E D-D N.A. 10AE16 E-E R.F. N.A. 10AE20 E-E D-D N.A.
Cast Iron
Casing
Drilling
(Maximum Suction Pressure
SUCTION FLANGE
Pump Size & Cast Iron Casing or Ductile Casing
Type 125 LB. ANSI Drilling 250 LB. ANSI Drilling
2AE11 E-E R.F. 3AE9 E-E D-D 3AE14, G E-E R.F. 4AE10, G E-E D-D 4AE11, G E-E D-D 4AE12 E-E D-D 5AE8, N E-E R.F. 5AE11, G E-E C-C 5AE12 E-E C-C 5AE14, G, N E-E R.F. 6AE11 E-E D-D 6AE12 E-E D-D 6AE14, G, N E-E D-D 6AE16G, N, V E-E R.F. 6AE18 E-E R.F. 8AE12 E-E E-E 8AE13 E-E E-E 8AE15, G E-E E-E 8AE17A, Q, W F-F F-F 8AE20, G F-F R.F. 10AE12 E-E D-D 10AE14A, J F-F F-F 10AE16 E-E R.F. 10AE20 E-E R.F.
N.A. = Not Available R.F. = Refer to the factory
Cast Iron
Casing
250 LB. ANSI
Drilling
TABLE B
Ductile Iron
Casing
250 LB. ANSI
Drilling
SECTION 1220 Page 2.1 June 1, 2004
AE PRESSURE-TEMPERATURE
LIMITATION CURVES
Subject to change without notice
4852154
Rev. 12-89
SECTION 1220 Page 2.2 June 1, 2004
Pump Size &
Type
Imp. Cplg. 2AE11 c
3AE9 .38 .12 5734 3600 6 1/2 3/4 1/2 1.625 1.375 9.56 1.2 6.13 3AE9G .38 .12 5734 3600 6 1/2 3/4 1/2 1.625 1.375 9.56 1.3 6.25 3AE14 .47 .12 5090
3AE14G .47 .12 5090 4AE10 .40 .12 5175 3600 6 1/2 3/4 1/2 1.625 1.375 10.38 1.7 7.00
4AE10G .40 .12 5175 3600 6 1/2 3/4 1/2 1.625 1.375 10.38 1.2 6.13 4AE11 .38 .12 6388
4AE11G .38 .12 6388 4AE12 d
5AE8 .38 .12 6830 3600 6 1/2 3/4 1/2 1.625 1.375 8.42 1.5 5.75 5AE8N .38 .12 6830 3600 8 1/2 3/4 1/2 1.625 1.375 8.42 1.3 5.75 5AE11 .50 .12 5902 3600 8 1/2 1 1/2 1.750 1.562 11.62 1.9 7.50 5AE11G .50 .12 5902 3600 8 1/2 1 1/2 1.750 1.562 11.62 1.9 7.50
5AE12 d 5AE14 .50 .12 4196
5AE14G .50 .12 4196 5AE14N .50 .12 4196 6AE11 .38 .12 6388 1800 5 1/2 1/2 1/2 1.375 1.125 11.29 2.1 7.00 6AE12 d
6AE14 .56 .12 4611 1800 8 1/2 3/4 1/2 1.750 1.562 15.66 5.0 10.00 6AE14G .56 .12 4611 1800 8 1/2 3/4 1/2 1.750 1.562 15.66 4.7 10.00 6AE14N .56 .12 4534 1800 8 1/2 3/4 1/2 1.750 1.562 15.66 7.9 11.00 6AE16 .56 .12 3841 1800 8 1/2 1 1/2 1.750 1.562 17.41 7.5 12.00 6AE16G .56 .12 3841 1800 8 1/2 1 1/2 1.750 1.562 17.41 7.3 12.00 6AE16N .56 .12 3841 1800 6 1/2 1 1/2 1.750 1.562 17.41 7.7 12.00 6AE16V .56 .12 3841 1800 8 1/2 1 1/2 1.750 1.562 17.41 9.5 12.00 6AE18 .69 .12 4034
8AE12 .44 .12 6024 1800 5 1/2 1/2 1/2 1.750 1.562 13.10 3.3 8AE13 .50 .12 4206 1800 8 1 1 1/2 1.750 1.562 13.72 8.6 9.00
8AE15 .56 .12 6013 1800 7 1 3/4 1/2 2.125 1.875 16.38 8.8 8AE15G .56 .12 6013
8AE17A d 8AE17Q d 8AE17W d
8AE20 .69 .12 3649 8AE20G .69 .12 3649 1800 8 1 1 1/2 2.500 2.250 20.84 29.9 14.00
10AE12 .56 .12 4799 1800 8 1 1 1/2 2.125 1.875 12.74 7.4 10AE14A d
10AE14J d 10AE16 d 10AE20 d
Nom.
Casing
Thick-
ness
Inches
.44 .12 6136 3600 4 1/2 1/2 1/2 1.375 1.125 11.00 1.3 7.00
.50 .12 6910 3600 7 1/2 3/4 1/2 1.625 1.375 12.58 2.4 8.50
.56 .12 6100 3600 6 1/2 1 1/2 1.750 1.562 13.00 2.9 8.50
.66 .12 6308 3600 7 1/2 3/4 1/2 2.125 1.875 13.00 5.5
.62 .12 3649 1800 8 1 1 1/2 2.125 1.875 18.90 12.1 12.00 .62 .12 3649 1800 8 1 1 1/2 2.125 1.875 18.90 11.8 12.00 .62 .12 3649 1800 8 1 1 1/2 2.125 1.875 18.90 12.8 12.00
.62 .12 4052 .62 .12 4052 .75 .12 3873 1800 8 1 1 1/2 2.500 2.250 17.00 22.9 11.50 .75 .12 3251
Corr-
osion
Allow-
ance
Inches
HORIZONTAL SPLIT CASE PUMPS
SINGLE STAGE DOUBLE SUCTION
Type AE

Pump Data

First
Critical
Speed
rpm
Max
Pump
Speed
rpm.
f
2300
f
2400
f
2000
f
2100
f
2000
f
2100
f
2100
f
1900
f
1900
f
2000
2000 f 2100 f
1900 f
No. of Vanes
Prime. or
Imp.
Csg. Vent
Conn.
NPT Size
5 1/2 1/2 1/2 1.375 1.125 14.50 3.0 9.75 6 1/2 1/2 1/2 1.375 1.125 14.50 1.7 9.00
8 1/2 3/4 1/2 1.375 1.125 11.91 1.8 7.62 6 1/2 3/4 1/2 1.375 1.125 11.91 2.0 7.62
8 1/2 3/4 1/2 1.625 1.375 14.62 5.7 10.00 8 1/2 3/4 1/2 1.625 1.375 14.62 3.6 10.00 6 1/2 3/4 1/2 1.625 1.375 14.62 3.1 10.00
8 1/2 1 1/2 2.125 1.875 18.15 14.7 13.00
8 1 3/4 1/2 2.125 1.875 16.38 8.4
8 1 1 1/2 2.500 2.250 20.84 22.0 14.00
8 1 1 1/2 2.500 2.250 15.08 16.0 8 1 1 1/2 2.500 2.250 15.08 16.6
7 1 1 1 2.750 2.500 21.25 37.4 15.00
Disch.
Drain
NPT Size
Suct
Drain
NPT Size
Shaft Diameter
Through (Inches)
Peerless Pump Company
Indianapolis, IN 46207-7026
Cut-
water
Dia.
In.
2
WR
Lb-Ft2
(Wet.
Brz.
Imp.)
Min. Imp.
Dia. In.
e 8.50
e 8.00
e 10.25 e 10.25
e 9.00 e 10.00 e 10.00
Single Suction Design d Double Volute Casing e Average Diameter
c f For applications where speeds exceed 4 pole motor speeds (1800 rpm), these must be reviewed by factory application department as
special pump construction may be required which may result in price additions for the special construction, refer to the factory for these applications.
See Page 2.21 for continuation of data Subject to change without notice
Peerless Pump Company
Indianapolis, IN 46207-7026
Pump Size Stuffing Box Bearing Size Distance
& Type Shaft
Sleeve
Dia.
Inches
2AE11 1.500 2.375 2.94 1.63 7/16 6 4.50 3/8 305 206 18.75 3AE9 1.750 2.750 3.31 1.82 1/2 6 4.75 1/2 306 207 20.00 3AE9G 1.750 2.750 3.31 1.82 1/2 6 4.75 1/2 306 207 20.00 3AE14 1.500 2.375 2.94 1.63 7/16 6 4.50 3/8 305 206 18.75 3AE14G 1.500 2.375 2.94 1.63 7/16 6 4.50 3/8 305 206 18.75 4AE10 1.750 2.750 3.31 1.82 1/2 6 4.75 1/2 306 207 20.00 4AE10G 1.750 2.750 3.31 1.82 1/2 6 4.75 1/2 306 207 20.00 4AE11 1.500 2.375 2.94 1.38 7/16 6 4.50 3/8 305 206 18.75 4AE11G 1.500 2.375 2.94 1.38 7/16 6 4.50 3/8 305 206 18.75 4AE12 1.750 2.750 3.31 1.82 1/2 6 4.75 1/2 306 207 20.00 5AE8 1.750 2.750 3.31 2.01 1/2 6 4.75 1/2 306 207 21.75 5AE8N 1.750 2.750 3.31 2.01 1/2 6 4.75 1/2 306 207 21.75 5AE11 2.000 3.000 3.31 1.68 1/2 6 5.25 1/2 307 208 22.00 5AE11G 2.000 3.000 3.31 1.68 1/2 6 5.25 1/2 307 208 22.00 5AE12 2.000 3.000 3.31 1.74 1/2 6 5.25 1/2 307 208 22.00 5AE14 1.750 2.750 3.31 1.82 1/2 6 4.75 1/2 306 207 23.25 5AE14G 1.750 2.750 3.31 1.82 1/2 6 4.75 1/2 306 207 23.25 5AE14N 1.750 2.750 3.31 1.82 1/2 6 4.75 1/2 306 207 23.25 6AE11 1.500 2.375 2.94 1.38 7/16 6 4.50 3/8 305 206 18.75 6AE12 2.375 3.500 3.75 2.20 9/16 6 6.25 5/8 308 210 25.50 6AE14 2.000 3.000 3.31 1.76 1/2 6 5.25 1/2 307 208 23.37 6AE14G 2.000 3.000 3.31 1.76 1/2 6 5.25 1/2 307 208 23.37 6AE14N 2.000 3.000 3.31 1.76 1/2 6 5.25 1/2 307 208 23.37 6AE16 2.000 3.000 3.31 1.74 1/2 6 5.25 1/2 307 208 26.12 6AE16G 2.000 3.000 3.31 1.74 1/2 6 5.25 1/2 307 208 26.12 6AE16N 2.000 3.000 3.31 1.74 1/2 6 5.25 1/2 307 208 26.12 6AE16V 2.000 3.000 3.31 1.74 1/2 6 5.25 1/2 307 208 26.12 6AE18 2.375 3.500 3.75 2.19 9/16 6 6.25 5/8 308 210 27.00 8AE12 2.000 3.000 3.31 1.74 1/2 6 5.25 1/2 307 208 22.00 8AE13 2.000 3.000 3.31 1.74 1/2 6 5.25 1/2 307 208 24.00 8AE15 2.375 3.500 3.75 2.20 9/16 6 6.25 5/8 308 210 25.50 8AE15G 2.375 3.500 3.75 2.20 9/16 6 6.25 5/8 308 210 25.50 8AE17A 2.375 3.500 3.75 2.19 9/16 6 6.25 5/8 308 210 27.00 8AE17Q 2.375 3.500 3.75 2.19 9/16 6 6.25 5/8 308 210 27.00 8AE17W 2.375 3.500 3.75 2.19 9/16 6 6.25 5/8 308 210 27.00 8AE20 2.750 4.000 4.12 2.44 5/8 6 7.50 5/8 310 212 33.50 8AE20G 2.750 4.000 4.12 2.44 5/8 6 7.50 5/8 310 212 33.50 10AE12 2.375 3.500 3.75 2.23 9/16 6 6.25 5/8 308 210 28.34 10AE14A 2.750 4.000 4.12 2.44 5/8 6 7.50 5/8 310 212 33.50 10AE14J 2.750 4.000 4.12 2.44 5/8 6 7.50 5/8 310 212 33.50 10AE16 2.750 4.000 4.12 2.44 5/8 6 7.50 5/8 310 212 33.50 10AE20 3.125 4.375 4.62 3.06 5/8 6 7.50 5/8 311 213 37.00
Bore
Inches
Depth
Inches
HORIZONTAL SPLIT CASE PUMPS
SINGLE STAGE DOUBLE SUCTION
Type AE
Pump Data-Continued
Face to Nearest
Obstruc-
tion on
Shaft
Inches
Packing
Size -
Square
Inches
Number of Rows
of
Packing
Each Box
f
Gland
Bolt
Circle
Dia. Inches Two @
180o
Apart
Gland
Bolt Dia.
Inches
SECTION 1220 Page 2.21 June 1, 2004
Thrust
(Single
Row)
Radial
(Single
Row)
Between
Bearing Centers
Inches
f Five with Optional Lantern Ring
Subject to change without notice
SECTION 1220
100
Page 2.22 June 1, 2004
90 80 70 60 50
% Torque
40
HORIZONTAL SPLIT CASE PUMPS
SINGLE STAGE DOUBLE SUCTION
Type AE
Speed - Torque Curve
Peerless Pump Company
Indianapolis, IN 46207-7026
30 20 10
0
0 102030405060708090100
% Speed
Information required to use speed-torque curve
1 - 100% of Torque 2 - 100% of Speed = Rpm (true running speed)
To determine 100% of torque in Ft.-Lbs., use the following equation:
100% torque (Ft.-Lbs)
RPM (true running speed)
c For open valve starting - use BHP at design point
For closed valve starting - use BHP at shut-off point
= Ft.-lbs @ Gpm Total Head Feet
BHP c x 5250
=
Subject to change without notice
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