Production Efficiency Guidance notes January 2010.

Slides:



Advertisements
Similar presentations
PPPs and Affordability
Advertisements

© 2009 The Williams Companies, Inc. All rights reserved. ______________ WECC November 12, 2012.
The Generic Choke Model enterprise (GCMe)
SAND CLEANING STATFJORD C FIELD TEST Stavanger 18 – 19 January 2006 Henrik Dannström, MATOR AS.
ENERGY VALUE. Summary  Operational Value is a primary component in the Net Market Value (NMV) calculation used to rank competing resources in the RPS.
The Radius Of Exposure The F&EI is converted to a Radius of Exposure by multiplying the F&EI by a factor of 0.84 or by using the next figure. This is determined.
Asset Management Optimization using model based decision support Speaker: Francesco Verre SPE Dinner Meeting – 25 th October 2011 – London.
Process Intensification: An Offshore Oil & Gas Industry Perspective Heriot-Watt, June 3 rd 2004 Mike SWIDZINSKI Technology Team Leader - NSBU.
EcoVapor Recovery Systems
Inventory Control, Cost & Deterministic models Unit-III Revised version.
Part 4.3 Gas Processing.
Place your chosen image here. The four corners must just cover the arrow tips. For covers, the three pictures should be the same size and in a straight.
Risk Management & Real Options VIII. The Value of Flexibility Stefan Scholtes Judge Institute of Management University of Cambridge MPhil Course
Exergy: A Measure of Work Potential Study Guide in PowerPoint
1 Real-Time Optimization (RTO) In previous chapters we have emphasized control system performance for disturbance and set-point changes. Now we will be.
History PSI-WS7 has its origins 20 years ago in the Western Canadian Sedimentary Basin. This development was a new approach to dealing with the heavy.
UTSW Thermal Energy Plants, Power Generation and Electrical System What do we do to meet the Emission Reduction, Energy usage Reduction and Electrical.
Baker Jardine Petroleum Engineering & Software Gas Lift Diagnostics A New Approach Daniel Lucas-Clements Baker Jardine.
Injection of Gas and Improved Oil Recovery - the Norwegian Experience By Steinar Njå, Norwegian Petroleum Directorate.
Provide specialist expertise and practical assistance in the configuration of metering systems Investigation, analysis, review and documentation Identify.
Preliminary Analysis of the SEE Future Infrastructure Development Plan and REM Benefits.
Reduced Emission Completions (Green Completions) Lessons Learned from Natural Gas STAR Producers Technology Transfer Workshop Devon Energy and EPA’s Natural.
CARBON FOOTPRINTING 16 TH JANUARY CARBON FOOTPRINTING TODAY’S PRESENTER SIMON ALSBURY  Technical Director at Energise and have provided energy.
“Specializing in Operational Excellence” Outsourcing Is it right for you? Texas Technology Showcase Houston, Texas March 18, 2003 Integrated Process Solutions.
TECHNICAL ASSOCIATION OF THE EUROPEAN NATURAL GAS INDUSTRY Development of a Eurogas-Marcogaz Methodology for Estimation of Methane Emissions Angelo Riva.
Introduction ► This slide deck provides a suggested framework for the financial evaluation of an investment project. When evaluating any such project,
Installing Vapor Recovery Units to Reduce Methane Losses
Along the existing collectors Comprehensive Solution for Flaring Gases Issue at the Facilities of the Unitary SC ShurtanNeftegaz By Rakhmatilla Rajabov,
© Copyright 2005 POSC Production Reporting (draft specifications) Overview.
New Air Quality Regulation “NSPS OOOO” Oil and Natural Gas Industry Workshop October 24, 2012 Robert Keatley, PE Senior Engineer/Supervisor DEP – Division.
© 2008 Data Power Services, LLC By: Tom Taranto 2010 Energy Expo Hosted by National Grid NYSERDA Reducing Compressed Air Energy Cost Using a Systems Approach.
Lecture slides by Mehmet Kanoglu
Lesson 8 SECOND LAW OF THERMODYNAMICS
Click Here to Add Date February 11,  Introduction  An Alternative Perspective of Compression  Recycling of Residue Gas  Relative Costs of Dehydration.
Opportunities to Save Water Colorado Water Workshop – through Efficient Design, Appropriate Technology, and Effective Management.
Effective Energy Management. 1.Develop baseline 2.Identify and quantify savings opportunities 3.Measure and benchmark to sustain efforts.
Results of pilot benchmark study Anfried Sauerborn/René Colin EAQG Metrics WGtApril 2008.
Network Appurtenances Major operations within a water transport and distribution systems are: 1. Transmission. 2. Storage. 3. Pumping.
Chapter 4 Control Volume Analysis Using Energy. Learning Outcomes ►Distinguish between steady-state and transient analysis, ►Distinguishing between mass.
Facilities Engineering *1 st draft By: Saha. Development options ProposalDevelopment OptionEstimated Cost (Mil) A FPSO converted to Tanker Hull 300 kbo.
Actualforecast Hydro, wind, and other renewables NGLs Coalbed methane Conventional natural gas Mined and in situ bitumen Conventional heavy oil Conventional.
Gas Flaring Reduction: OPEC Views OPEC Secretariat.
Producer Partner Reported Opportunities Lessons Learned from Natural Gas STAR Producers Technology Transfer Workshop ExxonMobil Production Company, American.
Emergency Cashout Prices and Emergency Curtailment Quantity (ECQ) Adjustment Ritchard Hewitt Gas Code Development Manager.
CEM CEM – 520 Measuring the Effectiveness of Materials Management for Industrial Construction Projects in Saudi Arabia Thesis By Ali Al-Darweesh.
Implementation of the CHP Directive - overview and outlook Talking competitiveness! New perspectives for CHP/DHC EHP Annual Conference Brussels
Components of Water Networks Eng. Mona Al-Gharbawi Eng. Ayman Al-Afifi
ACCT 2302 Fundamentals of Accounting II Spring 2011 Lecture 18 Professor Jeff Yu.
MOD0164 Bi-Directional Connection Point Overrun Charge Calculation Stuart Waudby (Centrica Storage Ltd.)
 BASIC TERMS AND CONCEPTS (1) Petroleum: refers to crude oil and natural gas or simply oil and gas. (2) Crude oil: refers to hydrocarbon mixtures produced.
Flow of Compressible Fluids. Definition A compressible flow is a flow in which the fluid density ρ varies significantly within the flowfield. Therefore,
Oil and Gas Training Lusaka April 2016.
Improving performance, reducing risk Dr Apostolos Noulis, Lead Assessor, Business Development Mgr Thessaloniki, 02 June 2014 ISO Energy Management.
MARCELLUSCOALITION.ORG Royalties on Oil and Gas Leases – Treatment of Post-Production Costs.
UNDERSTANDING ISO 9001:2008.
Forties Pipeline System Contaminant Management & Waiver Process
Fuel Cost Components in the Fuel Adder
SPE Introduction to Exploration and Production :
Fuel Cost Components in the Fuel Adder
Strategic Capacity Management
Fuel Cost Components in the Fuel Adder
Reconstruction site Investigation, Planning, Scheduling, Estimating and Design Eng. Fahmi Tarazi.
Maui Pipeline Capacity
Engineering Economy: Replacement Study
With assistance from Deidra Garyk
Production Allocation Discrepancy Reporting
Stevenson 5 Capacity Planning.
AIR Quality Control Concepts
Benefit-Cost Analysis Course: Referent Group Analysis
Presentation transcript:

Production Efficiency Guidance notes January 2010

Contents Metric Principles Definitions –Production efficiency components –Total Annual throughput –Well potential –Plant potential –Export potential –Market potential –Structural Maximum Production Potential (SMPP) –Summary of Field Production measures Gas Balance Production Constraints –Oil & Gas field –Gas field producing under contract

PE Guideline - Metric Principles –The intention of the Production Efficiency (PE) metric is to provide a tool to help make improvements to production performance, by creating a standard to: Benchmark operations against Quantify the size and value of operational excellence opportunities Show the primary areas to improve performance on each metric –PE is an objective metric, not a subjective one, so 100% PE would imply “perfect” operations, such that additional production could only be achieved through structural changes. Structural changes require either further investment to increase the Structural Maximum Production Potential (SMPP) or negotiating additional Market Maximum Production Potential (MMPP)

Definitions: PE Components Structural Maximum Production Potential Structural Maximum Production Potential (SMPP) is the lowest structural production potential of the well, plant and export systems including third party processed volumes*. Structural MPP is the sum over the year of the monthly MPP figures evaluated at the beginning of each month. Well production potential is the sum of the individual operating well flow rates tested at the optimum operating conditions plus the sum of the third party forecast well potential. Plant production potential is the maximum monthly throughput potential measured daily, including third party forecast throughput. Export potential is the maximum monthly physical potential available through ships and/or pipeline measured daily, including third party forecast throughput. Market Potential (applicable only to gas fields producing under contract) is the sum of the daily contract nominations for the month. * Third party processed volumes include only processed flows and not ‘up and over’ flows

Definitions: Annual throughput definition Total annual throughput This is the total processed throughput which is delivered to the export* system. It includes third party volumes which undergo processing at the production facility, but not "up and over" volumes which pass through without being processed. Total annual throughput =annual oil production (including condensate and NGL if not included in gas) +oil processed for third parties +wet gas exported* (exported gas including NGL if not included in oil, but excluding flare). This will also include any third party gas. * For gas production, export system means all gas that is delivered off the production facilities i.e. the sum of gas exported to pipeline and re-injection. This should not include gas lift.

Definitions: Well potential Well Potential = The sum of the individual operating well flow rates tested at optimum operating conditions plus the sum of the third party forecast well potential including gas for fuel, flare and re-injection The optimum operating conditions being the flow potential for a well at the minimum 1st stage separator pressure or the optimum drawdown for good reservoir management (e.g. to prevent water or gas coning and sand free flow). The 1st stage separator pressure being the pressure in the first separator downstream of the well in question. Losses due to mechanical well impairment, localised reservoir restrictions or voidage replacement at the time of the well test will not be captured by the production potential. An “operating well” is defined as a well that is economically viable to operate under the operating conditions of the field. This includes the potential of an operating well that is shut-in for any reason (e.g. workover, annual valve maintenance, reservoir monitoring, etc) If a “non-operating well” is not economic to be brought back onstream and is to be permanently shut-in or abandoned then the well flow potential should be removed from the overall well potential. New well potential should only be included when it is brought onstream.

Definitions: Plant potential Plant potential = Sum of the daily throughput potential of the plant  The throughput potential is measured as the quantity of oil, gas, condensate and NGLs that could be processed over a set period of time when no interruptions occur.  Throughput potential should include gas for re-injection, fuel or flare.  The constraint on the throughput can be from any of the following; water, gas, oil processing, flare limits or water disposal limits  Plant potential should not be reduced for planned or unplanned shut-downs  New or modified plant giving additional potential for processing should only be added to the plant potential when brought onstream  The boundary between i. well and ii. plant is at the flange of the wing valve downstream of the christmas tree, so underwater equipment may be part of the plant / host facility rather than the well.

Definitions: Export potential Export potential = Maximum volume that can be exported through the pipeline or shuttle tankers (including third party volumes if processed) and re-injection.  Daily sum of the potential export volumes through the export system without any interruptions, planned or unplanned  Re-injection potential (this should not include gas lift)  Includes oil, gas, condensate and NGL potential  Includes any pipeline specification which may limit the export volumes (e.g. maximum % water, H2S PPM, wax content)  Market constraints should not reduce the Export potential.

Definitions: Market Potential (gas fields) Market Potential =for some gas fields production is constrained by the type of gas contract that is in place, and this can be the overriding consideration when calculating the SMPP. The monthly volume should be the sum of the daily gas nominations for that month. For the annual shut down when fields are not nominated the number should be zero.  Daily sum of the gas nominations  When reporting an individual field the total annual production should be the production from that field’s reservoir and should not include any substitution or attribution volumes.

Well availability or reservoir availability Oil Gas Water Export Total Annual Throughput Production Plant potential Losses recorded against SMPP * *Losses include an “unallocated” category where the reasons for the difference between SMPP and Actual Production have not been determined SMPP Market SMPP is the lowest constraint on production

Summary of Field Production Measures Total Annual Throughput is the total processed throughput which is delivered to the export system. It includes third party processing volumes, but excludes “up and over” volumes. Total Annual Production is the total produced and processed volume Total Annual Throughput 3 rd Party Gas 3 rd Party Oil Total Annual Production Wet Gas Evacuated Oil Production Gas Oil

Gas Balance GAS PRODUCTION 3 RD PARTY GAS PRODUCTION FLARE GAS FUEL GAS GAS EXPORT GAS RE-INJECTION (not gas lift) GAS THROUGHPUT PRODUCTION FACILITIES

Production Constraints – Oil & Gas Fields

Production Constraints – Gas fields