ProSoft Technology, Inc. Summary Regarding Alberta Energy and Utilities Board Directive 017 of May 2007

Similar documents
The ERCB Directive 017 Overview

The Discussion of this exercise covers the following points:

Gas Measurement Fundamentals Certification. Curriculum

General Specifications

General Specifications

ONSITE PROVING OF GAS METERS. Daniel J. Rudroff WFMS Inc West Bellfort Sugar Land, Texas. Introduction

Impact of imperfect sealing on the flow measurement of natural gas by orifice plates

Special Documentation Proline Promass 500 Coriolis Flowmeter Modbus RS485 Petroleum Application Package

General Specifications

Vehicle-mounted meters, pump supplied

GAS TRANSPORTER S REQUIREMENTS FOR GAS MEASUREMENT SYSTEMS CONNECTED TO THE NATIONAL GRID GAS NETWORK

Gerald D. Anderson. Education Technical Specialist

General Specifications

Chapter 22 Testing Protocols

Vehicle- or rack-mounted liquefied gas meters, pump supplied

ONSITE PROVING OF GAS TURBINE METERS Daniel J. Rudroff Invensys Metering Systems

COMPAFLOW. Compressed Air. Volumetric flow. Gas. Mass flow. Steam. Net volumetric flow. Liquid

Issue Date: Effective Date: Supersedes: V-15 (rev. 2)

Automatically or individually calculated.

Measurement Guideline for Upstream Oil and Gas Operations. Oil and Gas Commission

vj.i GUIDELINES --.- PETROLEUM (EXPLORATION & PRODUCTION) (MEASUREMENT) REGULATIONS, 2016 (L.I. 2246)

Accurate Measurement Guidelines

STANDARD SPECIFICATION FOR FLOW INSTRUMENTS DOCUMENT NO : 44-LK /J.02/0006-A4

Special Documentation Proline Promass 300 Modbus RS485. Petroleum Application Package MANUAL

Compiled by: B Beard. Approved by: SH Carstens. Description of requirements and procedures for compact provers to be used as verification standards.

FAQs about Directive PNG017: Measurement Requirements for Oil and Gas Operations

Measurement Requirements for Upstream Oil and Gas Operations

Tutorial. BOSfluids. Relief valve

SUMMIT 8800 Handbook. Flow Computer Volume 2: Software. KROHNE 08/ MA SUMMIT 8800 Vol2 R02 en

Measurement & Analytics Wet gas monitoring

TWO PHASE FLOW METER UTILIZING A SLOTTED PLATE. Acadiana Flow Measurement Society

Validation of Custody Transfer Metering Skid at Site After Laboratory Proving

FAQs about Directive 017

Instructions for SMV 3000 Multivariable Configuration (MC) Data Sheets

Micro Motion 3098 Gas Specific Gravity Meter

A REVIEW OF THE 2000 REVISIONS TO ANSI 2530/API MPMS 14.3/AGA REPORT NO. 3 - PART2 Paul J. LaNasa CPL & Associates

Bubble Tube Installations

Metering Code Gas TSO, measurement by connected party Effective from to the present

Micro Motion Multiphase Applications

Technical Bulletin, Communicating with Gas Chromatographs

Injection Controller Program User Manual (for FloBoss 107 and ROC800-Series)

Software Applications

IT STARTS AT THE SOURCE - RE-CALIBRATING YOUR PLANT METERS

Modeling a Pressure Safety Valve

OVERVIEW OF THE CONVAL 10 SERVICE RELEASES

SOFTWARE APPLICATIONS DETAILS. Abstract This document is the calculation details for working with KELTON Standard Calculation Package (FLOCALC.

This test shall be carried out on all vehicles equipped with open type traction batteries.

ISO INTERNATIONAL STANDARD. Natural gas Measurement of properties Volumetric properties: density, pressure, temperature and compression factor

API MPMS Chapter 17.6 Guidelines for Determining the Fullness of Pipelines between Vessels and Shore Tanks

InstrumentationTools.com

Manual of Petroleum Measurement Standards Chapter 6 Metering Assemblies Section 3A Pipeline and Marine

Operational Settings:

CALCULATING THE SPEED OF SOUND IN NATURAL GAS USING AGA REPORT NO Walnut Lake Rd th Street Houston TX Garner, IA 50438

Truck-mounted Mass Flow Metering for LPG Delivery

IRC 2011 All Rights Reserved

This document is a preview generated by EVS

6-way characterised control valves DN15 and DN 20

Gas Flow Calibration Basics

How to specify a product. Process Sensors and Mechanical Instruments

Manual of Petroleum Measurement Standards Chapter 6.1A

Electronic Volume Correctors

A review of best practices for Selection, Installation, Operation and Maintenance of Gas meters for Flare Applications used for Managing facility

Ron Gibson, Senior Engineer Gary McCargar, Senior Engineer ONEOK Partners

WaterSense Specification for Spray Sprinkler Bodies. Version 1.0

Software Applications

These Terms and conditions apply to audit trails incorporated in weighing and measuring devices and systems 1.

Smart Water Application Technologies (SWAT)

M-06 Nitrogen Generator (Nitrogen Making Machine)

Exercise 2-2. Second-Order Interacting Processes EXERCISE OBJECTIVE DISCUSSION OUTLINE. The actual setup DISCUSSION

LIQUID METER PROVING TECHNIQUES CT 4095

National Occupational Standards For Measurement Processes Approved by UKCG May 2003

Requirements for the certification of movements and mechanical watches resistant to magnetic fields of 1.5 T ( G)

Technical Bulletin, Meter Factor Linearization

L 100. Bubble-Tube Level System. Installation, Operation and Maintenance Instructions

THE FUNDAMENTALS OF THE AIR SAMPLER CALIBRATION-VERIFICATION PROCESS

LPG DRIVER ATTENDED TRANSPORT LOADING

Measurement Requirements for Oil and Gas Operations

Standard Pneumatic Test Procedure Requirements for Piping Systems

HANDBOOK SAFETY DEVICES. Ed SAFETY DEVICES DS-ED 01/ ENG 1

ISO INTERNATIONAL STANDARD

SLOP RECEPTION AND PROCESSING FACILITIES

ISO 6570 INTERNATIONAL STANDARD. Natural gas Determination of potential hydrocarbon liquid content Gravimetric methods

Lab 1c Isentropic Blow-down Process and Discharge Coefficient

44 (0) E:

Micro Motion Advanced Phase Measurement

1 PIPESYS Application

Automatic Isokinetic Sampler. ST5 Evo

Type , , S2.20 Specialized test procedure Procedure for testing LPG bulk meters using a vapour displacement prover

SEMEM3-78 Testing and calibrating instrumentation and control equipment and circuits

SIZING THE EXTROL DIAPHRAGM-TYPE HYDRO-PNEUMATIC TANK

6-way characterised control valves DN15 / DN 20 / DN 25

Multiphase MixMeter. MixMeter specification. System Specification. Introduction

Analogue and Digital Mass Flow Meters and Controllers for Gases MASS-STREAM

JOS 15 JOS 25 JOS 40. Manual and semiautomatic test benches from DN 25 to DN 40. Characteristics. Basic characteristics. Test bench using balances

Vortex Meters for Liquids, Gas, and Steam

Paper 2.2. Operation of Ultrasonic Flow Meters at Conditions Different Than Their Calibration

CORESTA RECOMMENDED METHOD N 6

Location of CC Number if not located with the identification:

8:30 am 10:00 am Calculation of Petroleum Prover Quantity Calibration (COLM Ch. 12.4)

2016 Spring Committee on Petroleum Measurement Standards Meeting March 14-18, 2016 Hyatt Regency Dallas at Reunion Dallas, Texas

Transcription:

Overview ProSoft Technology, Inc. Summary Regarding Alberta Energy and Utilities Board Directive 017 of May 2007 ProSoft Technology s Gas and Liquid Flow Computer (AFC) products will comply with the requirements of the EUB Directive 017 of May 2007 with the release of the AFC version 2.05. These products are affected: MVI46-AFC MVI56-AFC MVI69-AFC MVI71-AFC PTQ-AFC The EUB document may be downloaded from: http://www.eub.ca/docs/documents/directives/directive017.pdf Details I. Using the AFC to Implement General EUB Requirements 1. Standard or Base Conditions The EUB base conditions of 15 C and 101.325kPaa are default for the SI System of Units. 2. Periodic Volumes Periodic volumes may be calculated by appropriate arithmetic on recorded accumulator values from all the archive records spanning the period, which values may be specified by appropriate configuration of the archive file. II. Notes on the EUB Directive 017 of May 2007 1 - Standards of Accuracy Compliant The AFC module is covered by adherence to requirements in subsequent sections. (See bold text in the directive, Sec 1.2, p 5) 2 - Calibration and Proving This is inapplicable in the AFC until the release of version 2.06. Furthermore, all requirements concern methods and procedures for meter physical inspection, transmitter calibration, and meter proving; applicability to v 2.06 AFC comprises only: (a) the expected prover types, and (b) the required number of runs and allowed tolerances of resulting meter factors, both of which will be accommodated in the design of the prover interface of the AFC v 2.06. Page 1 of 5

3 - Proration Factors, Allocation Factors, and Metering Differences This is inapplicable to the AFC, as AFC considers meter channels as independent entities only, and any such Factors or Differences belong more appropriately to a plant-balancing system; however, the AFC provides some support for API MPMS Ch 20.1 "Allocation Measurement" (distinct from EUB's "Allocation Factor") in the form of a "Shrinkage Factor" configurable for each meter channel (this appears to be related to EUB's "Metering Differences"). 4 - Gas Measurement All requirements concerning design, assembly, and installation are inapplicable to the AFC, as the AFC is a calculation device only. Sec 4.3.1 paragraphs 3 and 4 p 63 The AFC implements non-resettable counters (accumulators), accessible via Modbus; they can be displayed using a Modbus master such as AFC Manager, but a permanent physical display thereof is outside the scope of the AFC. Sec 4.3.1 paragraphs 5 p 63 The AFC does not implement measurement using Venturi tubes or flow nozzles. Sec 4.3.1 paragraphs 6, 7, and 8 p 63 The AFC can measure flow through an ultrasonic or coriolis meter, provided that it can issue a pulse train that represents gross volume or mass flow (configure the channel as "linear/pulse count"), or supply an output that represents gross volume or mass flow rate (configure the channel as "differential/flow rate integration"). The AFC can measure flow through a V-cone or wedge meter (configure the channel as "differential/orifice", set the option "V-cone/wedge device", and enter values from the device's calibration sheet or calculated therefrom by a spreadsheet supplied by ProSoft). Temperature, pressure, and compressibility corrections are calculated using AGA 8 (1992) Detail Characterization Method in conjunction with the real gas law. Sec 4.3.2 pp 64 All meter types (except Venturi or flow nozzles, which are unavailable in the AFC) provide as primary input one of: Differential pressure: Mass flow rate is calculated using the Bernoulli equation with diameter ratio "Beta", expansion factor "Y", and coefficient of discharge "Cd" determined according to meter type: Page 2 of 5

o Orifice: Beta calculated from entered pipe and orifice diameters. Y and Cd calculated using AGA 3 (1992) or ISO 5167-2 (2003). o V-cone and Wedge: Enter pipe and cone diameters. Set option "V-cone/wedge device"; this causes the AFC to use the correct "orifice-equivalent" Beta in its calculations and to use an alternate calculation for Y, resulting in a Bernoulli equation implementation consistent with that given in McCrometer's Lit# 24509-54 rev 3.0. Enter the Cd from the meter's calibration sheet. For a wedge device, use a ProSoft-supplied spreadsheet to calculate from data on the calibration sheet the equivalent "cone diameter" and "coefficient of discharge", and enter those values; calculation then proceeds as for a V-cone. Pulse count and/or frequency representing Gross Volume or Mass flow: Flow increments and/or rates are calculated as (pulses)/(k-factor)*(meter factor) with meter factor derivable via a five-point linearization curve. If pulse count is supplied then pulse frequency must also be supplied in order to calculate flow rate; this is to avoid instabilities in flow rate that would occur should the AFC attempt to differentiate the increment over time. Gross Volume or Mass flow rate: Used directly. The primary input thus yields either or both of a flow increment and a flow rate, measuring either Gross Volume or Mass. If the increment is not yet available (pulse count not supplied), then the increment is calculated by integrating the rate over time. Calculation of the remaining two quantities of Gross Volume or Mass, and Net Volume, is accomplished using the real gas law PV=ZNRT and the mass-volumedensity relationship M=VD, with compressibilities Z and densities D calculated from molar analysis via the Detail Characterization Method of AGA 8 (1992); any gas densities available from the meter are not used. The AFC provides no facility for converting a liquid measurement to a gas equivalent; the gas equivalent volume of any condensate stream measured as a liquid must be determined off-line by the methods of Appendix E-3 of EUB Directive 46. Updating the physical constants used by the AFC to the latest values from the GPSA Engineering Data Book or GPA-2145 can be performed by replacing the AFC's firmware with an updated version that contains those latest values; v 2.05 AFC uses values from GPSA 2004 and GPA-2145-03. Page 3 of 5

Sec 4.3.3 pp 66 All historical records required for compliance are or can be made available in the AFC's event log and archive files, or can be calculated from data recorded therein. The AFC does not apply an "effluent correction factor" to a gas stream. Volumetric flow rate alarms may be signaled by the PLC upon calculated flow rates returned to the PLC as a matter of course; if specific quantities are required for such alarms, they may be programmed for return. All process inputs, including the "primary input" that most directly represents flow rate (differential pressure, pulse frequency), are range-checked and alarmed when out of range; this may constitute sufficient compliance with the "volumetric flow rate alarm" requirement. Environmental alarms (communication failure, low power) are outside the scope of the AFC module. Test cases pp 68-77 Test Results Coming Soon Compliance of the AFC's calculations with the requirements of the EUB Test Cases will be made available in a separate document upon the release of version 2.05. Sec 4.3.4 pp 80 to the AFC Sec 4.3.5 pp 81 to the AFC 5 - Site-specific Deviation from Base Requirements 6 - Conventional Oil Measurement All requirements concerning design, assembly, and installation are inapplicable to the AFC, as the AFC is a calculation device only. All requirements concerning battery balancing are outside the scope of the AFC, as the AFC treats all its meter channels as independent from each other. Battery balancing calculations belong more appropriately to a plant balancing or similar system. The AFC does not implement tank gauging. Sec 6.3.2 pp 116 Calculation and application of correction factors (CTL, CPL) can be configured for a wide range of scenarios. A Shrinkage Factor can also be configured for some liquid product groups, which is applied to the final Net Volume increment and flow rate, after all other corrections and conversions. Page 4 of 5

Sec 6.8.1 pp 128 The hydrometer correction calculated by the AFC conforms to the method specified in the superceded API MPMS Ch 11.1 (1980); the AFC does not implement any other hydrometer correction calculation. All historical records required for compliance are or can be made available in the AFC's event log and archive files, or can be calculated from data recorded therein. Volumetric flow rate alarms may be signalled by the PLC upon calculated flow rates returned to the PLC as a matter of course; if specific quantities are required for such alarms, they may be programmed for return. Environmental alarms (communication failure, low power) are outside the scope of the AFC module. Test cases p 129 Test Results Coming Soon Compliance of the AFC's calculations with the requirements of the EUB Test Cases will be made available in a separate document upon the release of version 2.05. Appendix 1 - Sections Under Development Appendix 2 - EUB Documents Replaced Appendix 3 Glossary Appendix 4 - Water-Cut (S&W) Procedures Page 5 of 5