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ASTM F1172-88(1998)

(Specification)

Standard Specification for Fuel Oil Meters of the Volumetric Positive Displacement Type

Standard Specification for Fuel Oil Meters of the Volumetric Positive Displacement Type

SCOPE
1.1 This specification provides the minimum requirements for the design, fabrication, pressure rating, marking, and testing for fuel oil meters (volumetric positive displacement type).
1.2 The values stated in inch-pound units are to be regarded as the standard. Metric (SI) units are provided for information only.
1.3 The following safety hazards caveat pertains only to the test method section of this specification. This standard does not purport to address all of the safety problems, if any, associated with its use. It is the responsibility of the user of this standard to establish appropriate safety and health practices and determine the applicability of regulatory limitations prior to use.

General Information

Status
Historical
Publication Date
09-Apr-1998
ICS
75.200 - Petroleum products and natural gas handling equipment
Technical Committee
F25 - Ships and Marine Technology
Drafting Committee
F25.11 - Machinery and Piping Systems
Current Stage
Ref Project

Relations

Replaced By
ASTM F1172-88(2004) - Standard Specification for Fuel Oil Meters of the Volumetric Positive Displacement Type
Effective Date
01-Nov-2004

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ASTM F1172-88(1998) - Standard Specification for Fuel Oil Meters of the Volumetric Positive Displacement TypeASTM F1172-88(1998) - Standard Specification for Fuel Oil Meters of the Volumetric Positive Displacement Type
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ASTM F1172-88(1998) - Standard Specification for Fuel Oil Meters of the Volumetric Positive Displacement Type
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Standards Content (Sample)


NOTICE: This standard has either been superseded and replaced by a new version or withdrawn
Contact ASTM International (www.astm.org) for the lastest information
Designation:F 1172–88 (Reapproved 1998) AnAmerican National Standard
AMERICAN SOCIETY FOR TESTINGAND MATERIALS
100 Barr Harbor Dr., West Conshohocken, PA19428
Reprinted from theAnnual Book ofASTM Standards. CopyrightASTM
Standard Specification for
Fuel Oil Meters of the Volumetric Positive Displacement
Type
This standard is issued under the fixed designation F 1172; the number immediately following the designation indicates the year of
original adoption or, in the case of revision, the year of last revision.Anumber in parentheses indicates the year of last reapproval.A
superscript epsilon (e) indicates an editorial change since the last revision or reapproval.
1. Scope 2.4 API Standard:
Code No. 1101 Measurement of Petroleum Liquid Hydro-
1.1 This specification provides the minimum requirements
carbons by Positive Displacement Meter
forthedesign,fabrication,pressurerating,marking,andtesting
2.5 American Society of Mechanical Engineers:
for fuel oil meters (volumetric positive displacement type).
ASME Boiler and Pressure Vessel Code, Section VIII, Div.
1.2 Thevaluesstatedininch-poundunitsaretoberegarded
I, Pressure Vessels; Section IX, Welding and Brazing
as the standard. Metric (SI) units are provided for information
Qualifications
only.
1.3 The following safety hazards caveat pertains only to the
3. Terminology
testmethodsectionofthisspecification.Thisstandarddoesnot
3.1 Definitions of Terms Specific to This Standard:
purport to address all of the safety concerns, if any, associated
3.1.1 fuel oil meter (volumetric positive displacement
with its use. It is the responsibility of the user of this standard
type)—deviceintendedtoindicatethevolumeofliquidfueloil
to establish appropriate safety and health practices and
delivered to a fuel distribution system over a period of time.
determine the applicability of regulatory limitations prior to
3.1.2 maximum allowable working pressure (MAWP)—
use.
maximum system pressure to which a fuel oil meter may be
2. Referenced Documents subjected.
2.1 ASTM Standards:
4. Ordering Information
F722 Specification for Welded Joints for Shipboard Piping
4.1 Ordersforproductsunderthisspecificationshallinclude
Systems
3 the following applicable information:
2.2 ANSI Standards:
4.1.1 Title, number, and date of this specification.
B2.1 Pipe Threads
4.1.2 Operating pressure (psi) and temperature (°F).
B16.1 Cast Iron Pipe Flanges and Flanged Fittings
4.1.3 End connection and size.
B16.3 Malleable-Iron Screwed Fittings
4.1.4 Maximum capacity required.
B16.4 Cast-Iron Screwed Fittings
4.1.5 Type of fuel service.
B16.5 Pipe Flanges and Flanged Fittings
4.1.6 Materials—external and internal.
B16.11 Forged Steel Fittings Socket-Welding andThreaded
4.1.7 Other test requirements.
B16.34 Valves, Flanged and Buttwelding End
4.1.8 Qualification test reports as required.
B31.1 Power Piping
2.3 Manufacturers’ Standardization Society of the Valve
5. Materials and Manufacture
and Fittings Industry:
5.1 Fuel oil meter casings, as well as any pressure-retaining
MSS SP-25 Standard Marking System for Valves, Fittings,
parts, shall be constructed of ferrous material as listed in
Flanges and Unions
Section VIII, Division 1 of the ASME Boiler and Pressure
Vessel Code. All other parts shall be constructed of materials
suitable for the service intended. Fasteners in contact with
interior fluid shall be of corrosion-resistant steel.
This specification is under the jurisdiction ofASTM Committee F-25 on Ships
5.2 Seals and associated parts shall be of materials suitable
and Marine Technology and is the direct responsibility of Subcommittee F25.13 on
for the service and the fluid to be measured.
Piping Systems.
Current edition approved August 26, 1988. Published December 1988.
Annual Book of ASTM Standards, Vol 01.07.
3 5
Available from American National Standards Institute, 11 W. 42nd St., 13th Available from American Petroleum Institute, 1801 K St., N.W., Washington,
Floor, New York, NY 10036. DC 20226.
4 6
Available from Manufacturer’s Standardization Society of the Valve and Available from American Society of Mechanical Engineers, 345 E. 47th St.,
Fittings Industry, 1815 N. Fort Myer Dr., Arlington, VA 22209. New York, NY 10017.
F 1172
5.3 Manufacture: case,thevalueof BtobeusedindeterminingtheMAWPshall
5.3.1 Fuel oil meters with end fittings in compliance with be the maximum pressure to which the component was
ANSI Standards B2.1, B16.1, B16.3, B16.4, B16.5, B16.11, or subjected without rupture. Components that have been sub-
B16.34 as appropriate may be used within the pressure- jected to a hydrostatic proof test shall not be offered for sale.
temperature ranges permitted by the applicable standard pro-
6.2.1.2 The water temperature shall not exceed 125°F
vided the meter housing is satisfactory for these conditions. (52°C) during the test.
5.3.2 Threaded fittings above two nominal pipe size (NPS)
6.2.2 Design calculations are in accordance with the re-
and socket welded flanges above 3 NPS shall not be used in quirementsprescribedinSectionVIII,DivisionIoftheASME
fuel oil meters with a MAWP above 150 psig (1 N/mm ) and
Code.
for service above 150°F (65°C). 6.3 Whereweldedconstructionisusedforthefabricationof
5.4 Welding procedure qualification, welder performance
pressure containing parts, welded joint design details shall be
qualification, and welding materials shall be in accordance inaccordancewithSectionVIII,Division1oftheASMECode
withANSI B31.1 and Section IX of theASME Code. Brazing
and Specification F722. Except for fillet welds, all welds shall
or soldering shall not be used. befullpenetrationweldsextendingthroughtheentirethickness
of the shell.
6. Other Requirements
6.4 Inletandoutletconnectionsconsistingofweldedflanges
6.1 Components:
and fittings shall be in accordance with Specification F722.
6.1.1 The meter shall consist of a housing with measuring
Whenradiographyisrequired(see10.2),allweldsshallbebutt
mechanism and a register with counter mechanism.
welds for Class I piping as required by Specification F722,
6.1.1.1 Measuring Chamber—The measuring chamber for
except packing cylinders, drains, and similar ancillary connec-
all meters shall be so constructed as not to show distortion
tions may be attached by fillet or socket welds.
undermaximumallowableworkingpressureinanymanner,or
6.5 Capacity—Themaximumcapacityofthemetershallbe
to affect the sensitivity of the meter.
as specified by the manufacturer.
6.1.1.2 AdjustingDevice—Themetershallbeprovidedwith
6.6 Pressure Drop—The maximum pressure drop between
an adjusting device for changing the registered quantity to
the meter inlet and outlet shall not exceed 5 psi (34 MPa) as
attain desired calibration. The adjustment setting shall have
certified by testing in accordance with 8.1.1.2.
provisions for locking and shall not change during the meter
6.7 Error, Normal Flow—For flow rate and calibration
life except by manual readjustment.The adjusting device shall
settingbetween5and100%ofmaximumcapacity,theerrorof
be noncyclical and shall permit adjustment without disassem-
the meter s
...

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This specification provides the minimum requirements for the design, fabrication, pressure rating, marking, and testing for fuel oil meters (volumetric positive displacement type). The components of the meter shall be the following: housing, measuring chamber, adjusting device, direction marker, and register. Meter properties such as capacity, pressure drop, normal flow error, and maintainability shall be determined. Meters shall have all burrs or sharp edges removed and shall be cleaned of all loose metal chips and other foreign substances. A representative fuel oil meter shall undergo calibration and adjustment and hydrostatic test.
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1.4 Throughout this specification footnotes are provided for informational purposes and shall not be considered as requirements of this specification.  
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Standard Practice for Evaluating and Qualifying Oil Field and Refinery Corrosion Inhibitors Using Rotating Cage

SIGNIFICANCE AND USE
5.1 Selection of corrosion inhibitor for oil field and refinery applications involves qualification of corrosion inhibitors in the laboratory (see Guide G170). Field conditions should be simulated in the laboratory in a fast and cost-effective manner (1).3  
5.2 Oil field corrosion inhibitors should provide protection over a range of flow conditions from stagnant to that found during typical production conditions. Not all inhibitors are equally effective over this range of conditions so it is important for a proper evaluation of inhibitors to test the inhibitors using a range of flow conditions.  
5.3 The RC test system is relatively inexpensive and uses simple flat specimens that allow replicates to be run with each setup. (2-13).  
5.4 In this practice, a general procedure is presented to obtain reproducible results using RC to simulate the effects of different types of coupon materials, inhibitor concentrations, oil, gas and brine compositions, temperature, pressure, and flow. Oil field fluids may often contain sand; however, this practice does not cover erosive effects that occur when sand is present.
SCOPE
1.1 This practice covers a generally accepted procedure to use the rotating cage (RC) for evaluating corrosion inhibitors for oil field and refinery applications.  
1.2 The values stated in SI units are to be regarded as standard. The values given in parentheses after SI units are provided for information only and are not considered standard.  
1.3 This standard does not purport to address all of the safety concerns, if any, associated with its use. It is the responsibility of the user of this standard to establish appropriate safety, health, and environmental practices and determine the applicability of regulatory limitations prior to use.  
1.4 This international standard was developed in accordance with internationally recognized principles on standardization established in the Decision on Principles for the Development of International Standards, Guides and Recommendations issued by the World Trade Organization Technical Barriers to Trade (TBT) Committee.

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