ASTM F1510-98

Standard Specification for Rotary Positive Displacement Pumps, Commercial Ships Use

SCOPE
1.1 This specification defines the requirements applicable to design and construction of rotary positive displacement pumps for shipboard use. The classes of service are shown in Section 4.
1.2 This specification will not include pumps for hydraulic service or cargo unloading applications.

General Information

• Status: Historical
• Publication Date: 09-Jun-2001
• ICS: 47.020.30 - Piping systems
• Technical Committee: F25 - Ships and Marine Technology
• Drafting Committee: F25.11 - Machinery and Piping Systems

Relations

• Replaced By: ASTM F1510-01 - Standard Specification for Rotary Positive Displacement Pumps, Commercial Ships Use
• Effective Date: 10-Jun-2001
• Referred By: ASTM F2798-09(2023) - Standard Specification for Sealless Lube Oil Pump with Oil Through Motor for Marine Applications
• Effective Date: 10-Jun-2001
• Referred By: ASTM F1994-99(2023) - Standard Test Method for Shipboard Fixed Foam Firefighting Systems
• Effective Date: 10-Jun-2001
• Referred By: ASTM F2363/F2363M-17(2023) - Standard Specification for Sewage and Graywater Flow Through Treatment Systems
• Effective Date: 10-Jun-2001
• Referred By: ASTM F2283-12(2018) - Standard Specification for Shipboard Oil Pollution Abatement System
• Effective Date: 10-Jun-2001

Standards Content (Sample)

NOTICE: This standard has either been superseded and replaced by a new version or discontinued.
Contact ASTM International (www.astm.org) for the latest information.
Designation: F 1510 – 98 An American National Standard
AMERICAN SOCIETY FOR TESTING AND MATERIALS
100 Barr Harbor Dr., West Conshohocken, PA 19428
Reprinted from the Annual Book of ASTM Standards. Copyright ASTM
Standard Specification for
Rotary Positive Displacement Pumps, Commercial Ships
Use
This standard is issued under the fixed designation F 1510; the number immediately following the designation indicates the year of
original adoption or, in the case of revision, the year of last revision. A number in parentheses indicates the year of last reapproval. A
superscript epsilon (e) indicates an editorial change since the last revision or reapproval.
1. Scope Carbon Steel, for Intermediate and Higher Temperature
Service
1.1 This specification defines the requirements applicable to
A 536 Specification for Ductile Iron Castings
design and construction of rotary positive displacement pumps
A 563 Specification for Carbon and Alloy Steel Nuts
for shipboard use. The classes of service are shown in Section
A 564/A 564M Specification for Hot-Rolled and Cold-
4.
Finished Age-Hardening Stainless Bars and Shapes
1.2 This specification will not include pumps for hydraulic
A 574 Specification for Alloy Steel Socket-Head Cap
service or cargo unloading applications.
Screws
2. Referenced Documents
A 582/A 582M Specification for Free-Machining Stainless
and Heat-Resisting Steel Bars
2.1 ASTM Standards:
A 743/A 743M Specification for Castings, Iron-Chromium,
A 27/A 27M Specification for Steel Castings, Carbon, for
Iron-Chromium-Nickel, Corrosion-Resistant for General
General Application
Application
A 36/A 36M Specification for Structural Steel
B 150 Specification for Aluminum Bronze Rod, Bar, and
A 48 Specification for Gray Iron Castings
Shapes
A 53 Specification for Pipe, Steel, Black and Hot-Dipped,
B 584 Specification for Copper Alloy Sand Castings for
Zinc-Coated Welded and Seamless
General Applications
A 159 Specification for Automotive Gray Iron Castings
D 1418 Practice for Rubber and Rubber Lattices— Nomen-
A 193/A 193M Specification for Alloy Steel and Stainless
clature
Steel Bolting Materials for High-Temperature Service
D 2000 Classification System for Rubber Products in Auto-
A 194/A 194M Specification for Carbon and Alloy Steel
motive Applications
Nuts for Bolts for High-Pressure and High-Temperature
D 3951 Practice for Commercial Packaging
Service
F 104 Classification System for Nonmetallic Gasket Mate-
A 322 Specification for Steel Bars, Alloy, Standard Grades
rials
A 354 Specification for Quenched and Tempered Alloy
F 593 Specification for Stainless Steel Bolts, Hex Cap
Steel Bolts, Studs, and Other Externally Threaded Fasten-
Screws, and Studs
ers
F 912 Specification for Alloy Steel Socket Set Screws
A 395/A 395M Specification for Ferritic Ductile Iron
F 1511 Specification for Mechanical Seals for Shipboard
Pressure-Retaining Castings for Use at Elevated Tempera-
Pump Applications
tures
2.2 ANSI Standard:
A 434 Specification for Steel Bars, Alloy, Hot-Wrought or
B 16.5 Pipe Flanges and Flanged Fittings
Cold-Finished, Quenched and Tempered
2.3 SAE Standards:
A 449 Specification for Quenched and Tempered Steel
AS 568A Aerospace Size Standard for O-Rings
Bolts and Studs
J 429 Mechanical and Material Requirements for Externally
A 515/A 515M Specification for Pressure Vessel Plates,
Threaded Fasteners
This specification is under the jurisdiction of ASTM Committee F-25 on Ships
Annual Book of ASTM Standards, Vol 01.03.
and Marine Technology and is the direct responsibility of Subcommittee F25.11 on
Annual Book of ASTM Standards, Vol 02.01.
Machinery.
Annual Book of ASTM Standards, Vol 09.01.
Current edition approved Nov. 10, 1998. Published June 1999. Originally
Annual Book of ASTM Standards, Vol 09.02.
published as F 1510 - 94. Last previous edition F 1510 - 94. Annual Book of ASTM Standards, Vol 15.09.
2 12
Annual Book of ASTM Standards, Vol 01.02. Annual Book of ASTM Standards, Vol 01.07.
3 13
Annual Book of ASTM Standards, Vol 01.04. Available from American National Standards Institute, 11 W. 42nd St., 13th
Annual Book of ASTM Standards, Vol 01.01. Floor, New York, NY 10036.
5 14
Annual Book of ASTM Standards, Vol 01.05. Available from Society of Automotive Engineers, 400 Commonwealth Dr.,
Annual Book of ASTM Standards, Vol 15.08. Warrendale, PA 15096.
F 1510
2.4 AMS Standard: 3.1.10 net positive inlet pressure required (NPIPR)—the net
3215 Acrylonitrile Butadiene (NBR) Rubber Aromatic Fuel pressure above the liquid vapor pressure at rated flow and
Resistant 65-75 pumping temperature and at the pump inlet connection re-
2.5 AFBMA Standards: quired to avoid performance impairment due to cavitation.
9 Load Ratings and Fatigue Life for Ball Bearings 3.1.11 pressure, cracking—sometimes called set pressure,
11 Load Ratings and Fatigue Life for Roller Bearings start-to-discharge pressure, or popping pressure—the pressure
20 Bearing Interchange Guide at which the relief valve just starts to open. This pressure
2.6 AGMA Standard: cannot be determined readily if the relief valve is internal to the
390.03 Gear Classification, Materials and Measuring Meth- pump and it bypasses the liquid within the pump.
ods for Unassembled Gears 3.1.12 pressure, differential—the difference between dis-
2.7 API Standard: charge pressure and inlet pressure.
676 Positive Displacement Pumps—Rotary 3.1.13 pressure, discharge—the pressure at the outlet of the
2.8 Military Standards: pump. Discharge pressure is sometimes called outlet pressure.
MIL-S-901 3.1.14 pressure, inlet—the total pressure at the inlet of the
MIL-STD-167 pump. Inlet pressure is sometimes called suction pressure.
MIL-STD-740 3.1.15 pressure, maximum allowable working—the maxi-
mum continuous pressure for which the manufacturer has
3. Terminology
designed the equipment (or any part to which the term is
referred) when handling the specified fluid at the specified
3.1 Definitions:
temperature. This pressure should not be greater than ⁄3 of the
3.1.1 capacity—the quantity of fluid actually delivered per
hydrostatic test pressure of the pressure containing parts.
unit of time at the rated speed, including both the liquid and
3.1.16 rated condition—defined by discharge pressure, inlet
dissolved or entrained gases, under stated operating conditions.
pressure, capacity, and viscosity.
In the absence of any gas or vapor entering or forming within
3.1.17 rotary pump—a positive displacement pump consist-
the pump, the capacity is equal to the volume displaced per unit
ing of a casing containing gears, screws, lobes, cams, vanes,
of time, less slip.
shoes, or similar elements actuated by relative rotation between
3.1.2 capacity, maximum—the quantity of fluid delivered
the drive shaft and the casing. There are no inlet and outlet
that does not exceed the limit determined by the formula in 9.2.
valves. These pumps are characterized by their close running
3.1.3 displacement—the volume displaced per revolution of
clearances.
the rotor(s). In pumps incorporating two or more rotors
3.1.18 slip—the quantity of fluid that leaks through the
operating at different speeds, the displacement is the volume
internal clearances of a rotary pump per unit of time. Slip
displaced per revolution of the driving rotor. Displacement
depends on the internal clearances, the differential pressure, the
depends only on the physical dimensions of the pumping
characteristics of the fluid handled and in some cases, the
elements.
speed.
3.1.4 dry operation—a brief run during priming or stripping
3.1.19 speed, maximum allowable (in revolutions per
with suction and discharge lines unrestricted and pump cham-
minute)—the highest speed at which the manufacturers’ design
ber wet with liquid but pumping only air or vapor available
will permit continuous operation.
from the suction.
3.1.20 speed, minimum allowable (in revolutions per
3.1.5 effıciency, mechanical—the ratio of the pump power
minute)—the lowest speed at which the manufacturers’ design
output (hydraulic horsepower) to the pump power input (brake
will permit continuous operation.
horsepower) expressed in percent.
3.1.21 speed, rated—the number of revolutions per minute
3.1.6 effıciency, volumetric—the ratio of the pump’s capac-
of the driving rotor required to meet the rated conditions.
ity to the product of the displacement and the speed expressed
3.1.22 suction lift—a term used to define a pump’s capabil-
in percent.
ity to induce a partial vacuum at the pump inlet.
3.1.7 fuel, clean—fuel purified for direct use.
3.1.23 temperature, maximum allowable—the maximum
3.1.8 fuel, dirty—fuel before purification which may con-
continuous temperature for which the manufacturer has de-
tain water and some solids.
signed the equipment (or any part to which the term is referred)
3.1.9 net positive inlet pressure available (NPIPA)—the
when handling the specified fluid at the specified pressure.
total inlet pressure available from the system at the pump inlet
connection at the rated flow, minus the vapor pressure of the
4. Classification
liquid at the pumping temperature.
4.1 Pumps will be classified as follows:
4.1.1 Types:
4.1.1.1 Type II—Screws with timing gears.
Available from Anti-Friction Bearing Manufacturers Association, 1101 Con-
4.1.1.2 Type III—Screws without timing gears.
necticut Ave. N.W., Suite 700, Washington, DC 20036.
4.1.1.3 Type IV—Impellers with timing gears.
Available from American Gear Manufacturers Association, 1901 N. Fort Myer
Dr., Suite 1000, Arlington, VA 22209.
4.1.1.4 Type V—External gear (spur, helical, herringbone,
Available from American Petroleum Institute, 1801 K St., N.W., Washington,
lobe).
DC 20226.
4.1.1.5 Type VIII—Internal gear, internal rotary lobe.
Available from the Superintendent of Documents, U.S. Government Printing
Office, Washington, DC 20402. 4.1.1.6 Type X—Vane (sliding).
F 1510
4.1.1.7 Type XI—Sliding shoe. 7.2 Pumps shall be capable of sustained operation during
4.1.2 Classes: inclinations up to 45° in any direction.
4.1.2.1 Class A—Aqueous film forming foam, AFFF.
7.3 The pumps shall be capable of withstanding environ-
4.1.2.2 Class B—Bromine. mental vibration induced by shipboard machinery and equip-
4.1.2.3 Class CD—Clean distillate fuel, viscosity 32 to 100
ment in the frequency range from 4 to 25 Hz.
SSU (2 to 21 centistokes) (for example, jet fuel, JP-5, fuel).
7.4 The internally excited vibration levels of the pump shall
4.1.2.4 Class CH—Clean heavy fuel, viscosity 100 to 1500
not exceed 0.003-in. (0.00762-mm) displacement peak to peak
SSU (21 to 325 centistokes) (propulsion fuel).
during rated operation when readings are measured on the
4.1.2.5 Class DD—Dirty distillate fuel, viscosity 32 to 100
pump case near the coupling perpendicular to the pump shaft.
SSU (2 to 21 centistokes) (for example, transfer, stripping,
7.5 At normal operating conditions, the airborne noise level
purifier feed, leak-off).
of the pump shall not exceed 85 dBA.
4.1.2.6 Class DH—Dirty heavy oil, viscosity 32 to 4000
7.6 The pump driver (electric motor, air motor, turbine,
SSU (2 to 863 centistokes) (for example, waste oil, transfer,
hydraulic motor, diesel engine, attached) shall be as specified
stripping, purifier feed, drains).
in the ordering data. The driver shall be sized for maximum
4.1.2.7 Class G—Gasoline, aviation gasoline, gasohol.
flow at the relief valve full-flow bypass pressure, at maximum
4.1.2.8 Class LM—Lube oil, viscosity 130 to 4000 SSU (27
viscosity. If a two-speed motor is specified for high-viscosity
to 863 centistokes) (for example, propulsion, SSTG, control,
Class LM applications, the motor size shall be based on power
L.O. service).
required at low speed, which is used during cold startup.
4.1.2.9 Class LA—Auxiliary L.O. 130 to 4000 SSU (27 to
7.7 If a reduction gear is required between the driver and the
863 centistokes) service and L.O. transfer.
pump, it shall be provided by the pump manufacturer. Reduc-
4.1.2.10 Class M—Miscellaneous.
tion gears shall meet the requirements of AGMA 390.03. Gears
4.1.2.11 Class W—Heavily contaminated seawater, viscos-
shall be AGMA Class 7 or better, pinions shall be AGMA Class
ity 32 to 4000 SSU (2 to 863 centistokes) (bilge stripping, oily
8 or better, and bearings shall be designed for a L10 life of
waste transfer).
15 000 h.
7.8 Horizontal pumps may be mounted on a common
5. Ordering Data
horizontal bedplate with the driving unit or mounted directly to
5.1 The ordering activity shall provide manufacturers with
the driver. Vertical pumps may be mounted with a bracket to
all of the following information:
the driving unit or mounted directly to the driver.
5.1.1 Title, number, and date of specification,
7.9 All pump units shall incorporate guards over couplings,
5.1.2 Type and classification, see Section 4,
belts, and other external rotating parts.
5.1.3 Capacity in gallons per minute or litres per minute at
7.10 The mounting arrangement shall be sufficiently rigid to
rated discharge pressure,
assure alignment is maintained between the pump and the
5.1.4 Discharge pressure in pound-force per square inch
driver in accordance with the conditions in 7.2, 7.3, and 8.1.
gage (psig) or kilopascal (kPa) gage.
7.11 Seating surfaces of mounting bedplates, bracket
5.1.5 Airborne noise levels (if different than 7.5),
mounting plates, or other mounting arrangements shall be
5.1.6 Viscosity (only if different than Section 4),
machined.
5.1.7 Mounting configuration (vertical, horizontal),
7.12 Mounting bedplates, brackets, and plates shall be
5.1.8 Driver type (motor, turbine, engine, attached),
provided with holes of sufficient size and quantity to assure
5.1.9 Driver characteristics or specifications, or both,
adequate attachment to shipboard foundation or mounting
5.1.10 Relief valve cracking pressure and full-flow bypass
structure.
pressure,
7.13 Vertical units with face mounted motors shall be
5.1.11 Packaging and boxing requirements (immediate use,
arranged so there are four (4) possible orientations of motor
domestic; storage, domestic; overseas),
driver to pump. Other drivers are to be oriented in accordance
5.1.12 Quantity of pumps,
with the ordering information.
5.1.13 Quantity of drawings,
5.1.14 Quantity of technical manuals,
7.14 Vertical units that are motor driven shall be assembled
5.1.15 Quantity of test reports, with the conduit box mounted over the pump inlet flange,
5.1.16 Performance test, if required, unless otherwise specified.
5.1.17 Certified data required, and
7.15 Couplings between the pump and the driver shall be
5.1.18 Instruction plates and locations, if required.
keyed to both shafts.
7.16 Alignment between the pump and t
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