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PRODUCT OVERVIEW

PHASE BEHAVIOUR & FLUID PROPERTY PROGRAMWinProp™ is an essential tool for reservoir engineers, both in the laboratory and in the field, to accurately identify and model the phase behaviour and properties of reservoir fluids. It has proven its value for multi-phase and special processes, and where compositional variations exist. WinProp is an integral component in advanced reservoir simulation modelling.

WinProp creates tuned fluid property descriptions for IMEX™, GEM™ and STARS™, plus black oil fluid property data for third-party reservoir simulation software. WinProp can be used for:

� Component characterization

� PVT matching

� Miscibility studies

� Modelling of laboratory experiments

� Prediction of wax and asphaltene production

� Surface separation facilities modelling

� Generation of PVT data for CMG simulators

WinProp incorporates a user-friendly graphical interface that makes preparing data and interpreting results more effective and efficient.

ASPHALTENE & WAX PRECIPITATION MODELLINGWinProp has a multi-component solid solubility model coupled with the EoS for description of asphaltene or wax precipitation. WinProp models the precipitate as a multi -component solid. It also handles non-isothermal conditions and allows up to three fluid phases in equilibrium with the precipitate. Save time with the easy to use model that has few adjustable parameters and requires minimal experimental data.

MISCIBILITY PREDICTIONWinProp’s multiple contact miscibility option calculates condensing, vaporizing, or condensing -vaporizing drives. Based on user-defined lumping schemes, WinProp creates ternary diagrams to graphically interpret the miscibility mechanism. The minimum miscibility enrichment level allows calculation of the minimum fraction of rich gas required to be added to a lean gas stream to achieve multi-contact miscibility with oil at a specified pressure and temperature.

MULTIPLE EoSIt is often difficult for a single EoS description to perform adequately over a wide range of conditions encountered in reservoir phase behaviour modelling. This can be alleviated by the introduction of a second EoS model that is applied to calculations performed at surface (separator) conditions, while the first EoS set is used for calculations at reservoir conditions. Therefore, separator data can then be matched separately from other PVT data gathered at reservoir temperature, for example by CVD and differential liberation experiments.

AQUEOUS PHASE PROPERTIESUsing Henry’s Law, WinProp models the solubility of CO

2, H

2S, and light hydrocarbons in water of varying salinity.

Water content of gases is also predicted accurately. WinProp contains an extensive library of geochemical reactions for rock mineralogy interaction with the aqueous phase for output into GEM and STARS reservoir simulators.

BENEFITS

� Tune EoS to accurately match laboratory analysis results and predict fluid behaviour

� Understand property distribution within a reservoir fluid system, under different depletion scenarios

� Improve understanding of reservoir exploitation process

WinProp generated phase envelope showing vapor volumes.

3,500

3,000

2,500

2,000

1,500

1,000

500

00 100 200 300 400 500 600 700 800 900 1000

Temperature (Deg F)

Pre

ssur

e (p

sia)

2-Phase Boundary

10% Volume Fraction of Vapor Phase

30% Volume Fraction of Vapor Phase

50% Volume Fraction of Vapor Phase

Critical Point

+1.403.531.1300, INFO@CMGL.CACALGARY HOUSTON BOGOTA CARACAS LONDON DUBAI KUALA LUMPUR™Trademark of Computer Modelling Group Ltd. Copyright © 2015 Computer Modelling Group Ltd. 15.WI.02

PRODUCT OVERVIEW

iFOR MORE INFORMATION

PLEASE CONTACT marketing@cmgl.ca

WHY CMG?

Computer Modelling Group Ltd (CMG) is the leading supplier of advanced oil and gas recovery process simulation software. CMG offers products for Black Oil, Compositional and Thermal/Chemical reservoir simulation, Assisted History Matching and Optimization, and visualization software to best understand simulation results. Experienced support teams are stationed in offices around the world to provide the best software, training and client support for advanced recovery process simulation.

CMG is devoted to providing the ultimate customer experience through its commitment to R&D investment, superior technology, and support network.

1. R&D Investment: With more than half our employees devoted to R&D, CMG exceeds its customer needs. CMG reinvests 20% of its annual revenue back into R&D which results in significant expansion of the R&D team to further innovation and drive technology forward.

2. Superior Software Technology: CMG, the leader in enhanced oil recovery, delivers software that is easier to use and provides the most accurate results for unconventional, compositional, advanced IOR/EOR and conventional processes.

3. Customer Experience: CMG provides experienced technical sales and support personnel, located around the world. CMG engineers deliver same-day turnaround for support calls, small industry relevant training and a personalized customer experience.

2015 NEW FEATURES

� Differential evolution algorithm provides more stable search for minimum miscibility pressure (MMP) calculations

� Enhanced black oil PVT data generation for multi-contact swelling and improved extrapolation of properties vs. pressure

FEATURESLABORATORY ANALYSIS � Recombination � Fluid Compressibility � Constant Composition Expansion � Differential Liberation � Constant Volume Depletion � Separator Test � Swelling Test

FUNDAMENTAL CALCULATIONS � Isenthalpic flash and multi-phase flash

� Saturation pressure and temperature

� PT, PX, and TX envelopes, with quality lines, available for two and three-phase calculations

� Ternary Diagrams

� Standard phase property table also includes entropy, enthalpy and heat capacity

� Newton iteration for performing negative flashes in difficult regions

MISCIBILITY PREDICTION � First Contact Miscibility pressure calculation

� Multiple mixing cell method of Ahmadi and Johns to calculate minimum miscibility pressure

� Phase split calculation of Li, Johns & Ahmadi for multi-contact miscibility calculations

EoS PARAMETER REGRESSION � Multiple Peng-Robinson and Soave-Redlich- Kwong EoS models, both two and three parameter versions.

� Linear temperature-dependent volume shift model

� Regression on composition and properties

� Group parameters for regression and apply varying weights

� Automatic parameter selection and built-in parameter bounds

� Additional regression parameters for oil-gas-water flash

SIMULATOR FLUID PROPERTY SECTIONS � Complete PVT output for IMEX, GEM, and STARS and third-party reservoir simulators

� STARS gas viscosity parameter generation

� Ideal gas heat capacity coefficients estimated according to molecular weight

� Output of pressure dependent enthalpy model for STARS

RESERVOIR FLUID CHARACTERIZATION � Extensive library of hydrocarbon and non-hydrocarbon components

� Plus fraction splitting and component lumping

� Exponential, two-stage exponential, and gamma distribution functions for characterization calculations

� A user-friendly component lumping option