Flow Measurement Some Basic Terms and Concepts - PowerPoint PPT Presentation

1 / 26
About This Presentation
Title:

Flow Measurement Some Basic Terms and Concepts

Description:

Title: What is an RTU? Subject: Remote Terminal Unit Author: DCM / =S= Last modified by: Michael D. Williams Created Date: 7/24/1997 9:31:18 AM Document presentation ... – PowerPoint PPT presentation

Number of Views:127
Avg rating:3.0/5.0
Slides: 27
Provided by: DCMS1
Category:

less

Transcript and Presenter's Notes

Title: Flow Measurement Some Basic Terms and Concepts


1
Flow MeasurementSome Basic Terms and Concepts
  • Fluid - The state of a substance in which its
    particles easily move and change their relative
    position without a separation of the mass and
    that easily yield to pressure. A fluid can be a
    liquid (generally considered incompressible) or a
    gas.
  • Mass - Quantity of matter that causes it to have
    weight in a gravitational field. Mass flow is
    expressed in weight/time, ie kilograms/hr.
  • Volume - Space occupied or enclosed by cubic
    units. Volumetric flow is expressed in cubic
    measure/time i.e. cubic feet/minute or
    gallons/hour.
  • Density - Mass of a substance per unit volume.
  • Specific Gravity - The ratio of the density of a
    substance to the density of some some substance
    taken as a standard. For flow of liquids,
    specific gravity of fluid is compared against
    that of water, for gases against that of air.
  • Mole - grams/molecular weight
  • SCFM - Standard Cubic Feet per Minute.

2
Flow MeasurementSome Basic Terms and Concepts
  • Liquids are generally considered incompressible
  • Ideal Gas Law - The pressure, temperature and
    volume of a gas are all interrelated.
  • PV nRT
  • P pressure of the gas
  • V the volume that the gas occupies(ie ft3)
  • n number of moles
  • R ideal gas constant (a universal constant)
  • T temperature of the gas in absolute units
  • For the gas industry flow is most commonly
    measured as volumetric flow and expressed at base
    conditions
  • volume is dependant on temperature and pressure
    and composition
  • volumetric measurement must be corrected back to
    base conditions
  • usually 60 - 700F and 1 atmosphere (14.73 psia)
    pressure

3
The Object of Flow Measurement
  • How much went from one place to another?
  • Volumetric
  • corrected to base pressure and temperature
  • Mass
  • Mass is mass. It doesnt change with changes in
    temperature or pressure.

4
A Variety of Flow Measurement Methods
  • Orifice plate meter
  • Most common in the gas industry
  • Relatively low rangeability
  • Least accurate of all popular methods
  • High installation cost
  • No moving parts low (or no) maintenance
  • No calibration little maintenance
  • Intrusive device

5
Orifice Plate Meter
Differential Pressure
6
A Variety of Flow Measurement Methods
  • Turbine Meter
  • Most common meter type across all industries
  • Second most common in the gas industry
  • Much more accurate than orifice plate
  • Wide flow rangeability
  • Low relative cost to purchase but comparatively
    high cost to maintain
  • Has moving parts that can fail but is easily
    field repaired
  • Requires calibration
  • Intrusive device

7
Turbine meters
  • Use a vaned rotor engaged by the flowing fluid
  • the fluid spins the rotor at an angular velocity
    proportional to the flow rate
  • As the turbine rotates, an AC voltage is induced
    in a magnetic pickup
  • mounted externally to the fluid process
  • As each turbine blade passes the pickup the total
    magnetic flux density is changed
  • induces a single voltage pulse
  • Each pulse represents a finite volume of fluid
    that has been displaced through 2 adjacent rotor
    blades.

8
A Variety of Flow Measurement Methods
  • Positive displacement meter
  • Most accurate
  • Uses standard low speed digital input on PLC
  • Other less common types
  • Venturi meter
  • Ultrasonic meter
  • Vortex meter
  • Lots more

9
Flow Measurement by the Orifice Plate Method
  • Origins of the fluid flow Laws
  • More than 300 years ago, Charles and Boyle
    discovered that
  • Uf1 (P h)1/2
  • The formula looks deceptively simple
  • Qb (218.573Cd(FT)EvY1d2Tb/Pb)(Pf1Zb Zb
    airhw/GiZf1Tf) ½
  • And it would be,

10
Flow Measurement by the Orifice Plate Method
  • Origins of the fluid flow Laws
  • More than 300 years ago, Charles and Boyle
    discovered that
  • Uf1 (P h)1/2
  • The formula looks deceptively simple
  • Qb (218.573Cd(FT)EvY1d2Tb/Pb)(Pf1Zb Zb
    airhw/GiZf1Tf) ½
  • And it would be, except each component of the
    equation,

11
Flow Measurement by the Orifice Plate Method
  • Origins of the fluid flow Laws
  • More than 300 years ago, Charles and Boyle
    discovered that
  • Uf1 (P h)1/2
  • The formula looks deceptively simple
  • Qb (218.573Cd(FT)EvY1d2Tb/Pb)(Pf1Zb Zb
    airhw/GiZf1Tf) ½
  • And it would be, except each component of the
    equation, for example the Coefficient of
    discharge term, relies on solving an equation
    like this

12
Flow Measurement by the Orifice Plate Method
  • Origins of the fluid flow Laws
  • More than 300 years ago, Charles and Boyle
    discovered that
  • Uf1 (P h)1/2
  • The formula looks deceptively simple
  • Qb (218.573Cd(FT)EvY1d2Tb/Pb)(Pf1Zb Zb
    airhw/GiZf1Tf) ½
  • And it would be, except each component of the
    equation, for example the Coefficient of
    discharge term, relies on solving an equation
    like this
  • Cd(FT) Ci(FT).000511(106 ß/Red)0.7((0.0210.004
    9(19,000ß/ Red)0.8) ß4(106/ Red)0.35

13
Flow Measurement The Names and Numbers to Know
  • For measuring flow there are 3 equations that are
    the most common
  • For orifice plate meters, AGA 3
  • 1992 version
  • 1985 version
  • ISO 5167 is equivalent and is very similar
  • ISO is currently upgrading and will probably come
    into lock step with AGA
  • For turbine meters AGA 7
  • AGA 7 is a relatively simple equation compared to
    AGA 3
  • Uf1 (f/K)M

14
Flow Measurement The Names and Numbers to
Know(contd)
  • For high accuracy gas measurement a
    compressibility and sometimes supercompressibility
    equation is needed
  • AGA 8 Most common
  • 2 versions
  • 1985
  • 1992(ISO12213)
  • Multiple methods
  • Gross methods
  • 2 for 1992 (recommended method for use between 32
    to 130 oF and less than 1,200 psia, provided the
    gas composition is within the normal range)
  • 4 for 1985
  • Detailed methods
  • 1992 is the most accurate and most common

15
Flow Measurement The Names and Numbers to
Know(contd)
  • Other compressibility equations(in order of
    popularity)
  • NX-19 (developed in 1962)
  • Still used frequently in high C02 applications
  • Compressibility equations used for special gas
    compositions
  • Soave Redlich Kwong (SRK)
  • Wichert Aziz

16
Flow Measurement The Names and Numbers to
Know(contd)
  • API 2540
  • Used for liquid measurement with turbine or
    rotary displacement meters
  • Provides temperature and pressure compensation

17
Flow MeasurementPutting it all Together
  • For measuring gas with an orifice plate meter use
    one of these
  • AGA 3 alone
  • AGA 3 with AGA 8
  • AGA 3 with NX-19
  • AGA 3 with other

18
Flow MeasurementPutting it all Together (Contd)
  • For measuring gas with a turbine meter
  • AGA 7 alone
  • AGA7 with AGA 8
  • AGA7 with NX-19
  • AGA7 with other

19
Flow MeasurementPutting it all Together (Contd)
  • For measuring liquid with an orifice plate meter
  • AGA 3 alone
  • For measuring liquid with a turbine meter
  • AGA 7 alone
  • AGA 7 with API 2540
  • For measuring liquid with a rotary displacement
    meter
  • API 2540

20
Flow MeasurementAPI 21.1 Audit Trail and Event
Log
  • Custody transfer applications are those where the
    fluid being measured changes ownership at the
    meter point
  • If the measurement application is not custody
    transfer it is
  • Allocation (often requires API 21.1 for
    convenience)
  • Control
  • For custody transfer applications a detailed
    audit trail and event log are required
  • The Industry expects a minimum of
  • 7 days of hourly averages of specified variables
  • 35 days of daily averages of the same variables
  • A copy of the configuration of the meter
    parameters
  • A 100 entry time stamped log of events
  • All parameter changes
  • Alarms

21
Flow MeasurementIf You Dont Know for Sure, Just
Ask
  • If a customer says he needs an RTU that does AGA
    that doesnt mean anything!
  • Ask the customer some basic questions and consult
    your notes.
  • What is being measured?
  • What kind of meter do they have?
  • How accurate does the measurement need to be?
  • Is the customer doing custody transfer?
  • If a customer is just doing control based on flow
    measurement
  • AGA 3 or 7 alone are often accurate enough.

22
What is the Market for Flow Meters
  • Orifice Plate Meters
  • New installations projected to be
  • mil.
  • Revenues bil. Increasing by annually through
    2002
  • Turbine Meters
  • New installations projected to be
  • Revenues mil. Increasing by annually through
    2002
  • Source Frost Sullivan Worldsearch May,1996

Under Construction
23
What does Schneider offer?Orifice plate meters
  • Starling Associates Gas Flow Loadable Function
    Block Library
  • To run loadables on a continuous basis you must
    use the proper enabler, 130 HEK 301 01 or 130 HEK
    301 02
  • Fits in the bus expansion port of a Compact or
    Micro PLC.
  • Disallows the use of the AS HDTA 202 2 slot rack.
  • Must be used with a IA WBXT 204 cable if an AS
    WBXT 201 is used.
  • Loadables can be run, without an enabler, in demo
    mode for 48 hours after program load.

24
What does Schneider offer?Orifice plate meters
(continued)
  • Starling Associates Gas Flow Loadable Function
    Block Library
  • consists of 5 blocks that cover the different
    calculation combinations
  • G392 - up to 8 meters of AGA 3 1992 alone. API
    21.1 audit trail
  • GD92 - meter of AGA 3 1992 and AGA 8 detailed
    method.
  • GFNX - up to 8 meters of AGA3 1985 and NX-19.
    API 21.1 audit trail
  • GG92 - up to 8 meters of AGA 3 1992 and AGA 8
    both gross methods. API 21.1 audit trail
  • GM92 - up to 8 meters of AGA 3 1992 and AGA 8
    detailed method. API 21.1 audit trail

25
What does Schneider offer?Orifice plate meters
(continued)
  • Flow calculations run only on Compact and Micro
    612 04 CPUs
  • Except for the 612 04 you must have a minimum of
    16K 984 LL capable CPU to run GG92, GFNX or GM92
  • The 612 04 is a special case which can run any of
    the flow loadables and have a large amount of
    program space left.
  • GD92 and G392 may be run in as small as a Compact
    141 CPU
  • Using these loadables in an 8 K controller leaves
    little space for other programming.

26
What does Schneider offer?Turbine meters
  • AS BVRC 200, AS BCTR 205 and AS BCTR 224
  • High speed counter input cards, for the Compact
    and Modicon Micro, that perform the AGA 7
    Calculation in the module
  • K and M factors are configured in the module
    and a corrected count or rate is delivered to the
    CPU.
  • BVRC 200 takes direct turbine meter sine
    frequency input signal
  • BCTR 205 and 224 take square wave DC input
    signals, 5 VDC and 24VDC respectively.
  • API 2540 temperature compensation and pressure
    compensation is currently not supported as a
    solution but can be programmed by the end user.

27
What does Schneider offer?Orifice plate meters
(continued)
  • Flow calculations run only on Compact and Micro
    612 04 CPUs
  • Except for the 612 04 you must have a minimum of
    16K 984 LL capable CPU to run GG92, GFNX or GM92
  • The 612 04 is a special case which can run any of
    the flow loadables and have a large amount of
    program space left.
  • GD92 and G392 may be run in as small as a Compact
    141 CPU
  • Using these loadables in an 8 K controller leaves
    little space for other programming.
Write a Comment
User Comments (0)
About PowerShow.com