Tổng quan

Olga - Phần mềm mô phỏng dòng chảy động đa pha

Công cụ tiêu chuẩn ngành để mô phỏng dòng chảy đa pha động

Tổng quan OLGA

Phần mềm mô phỏng dòng chảy đa pha động Olga™ mô hình hóa dòng chảy tạm thời (các hành vi phụ thuộc thời gian) để tối đa hóa tiềm năng sản xuất. Mô hình hóa tạm thời là một thành phần thiết yếu cho các nghiên cứu khả thi và thiết kế phát triển mỏ. Mô phỏng động rất cần thiết trong vùng nước sâu và được sử dụng rộng rãi trong cả các dự án phát triển ngoài khơi và trên bờ để nghiên cứu hành vi tạm thời trong đường ống và giếng khoan. Mô phỏng tạm thời với phần mềm mô phỏng Olga cung cấp thêm một chiều hướng cho phân tích trạng thái ổn định bằng cách dự đoán động lực hệ thống, chẳng hạn như những thay đổi theo thời gian về lưu lượng, thành phần chất lỏng, nhiệt độ, lắng đọng chất rắn và các thay đổi trong hoạt động.

Từ động lực giếng khoan cho bất kỳ giếng nào đến hệ thống đường ống với nhiều loại thiết bị xử lý khác nhau, phần mềm mô phỏng Olga cung cấp dự đoán chính xác về các điều kiện vận hành chính liên quan đến dòng chảy tạm thời.

Kiểm chứng và Cải tiến dự án (OVIP) đã thu thập cơ sở dữ liệu lớn nhất thế giới về dữ liệu thí nghiệm và thực địa. Dữ liệu này đã được sử dụng để xác thực và điều chỉnh các mô hình dòng chảy đa pha. Kết quả liên tục được tích hợp vào phần mềm mô phỏng Olga, cải tiến công nghệ cốt lõi để phù hợp hơn với thực tế vận hành.

Ngoài ra, các dự án Xử lý CO2 Mạnh mẽ, Nâng cao độ Chính xác (REACH), Vận chuyển và Mở rộng Miền Tích hợp (Olga CO2 TIDE) được đồng tài trợ bởi các công ty dầu khí lớn. Các dự án này giải quyết những thách thức trong việc phát triển hiệu quả về chi phí và vận hành an toàn việc vận chuyển dòng khí ngưng tụ và dầu khí từ giếng khoan trên quãng đường dài.
 

Ứng dụng của phần mềm Olga

Phần mềm mô phỏng Olga cho phép thực hiện các ứng dụng mô phỏng dòng chảy quan trọng, bao gồm:

  • Xử lý chất lỏng.

  • Tính toán kích thước thiết bị tách và thiết bị thu gom chất lỏng dạng cục bộ.

  • Quản lý chất rắn.

  • Mô phỏng các quy trình vận hành chính bao gồm khởi động, tắt máy và làm sạch giếng.

  • Tối ưu hóa hoạt động nâng nhân tạo.

  • Lập mô hình cho kế hoạch dự phòng.

  • Đánh giá rủi ro môi trường trong môi trường khoan nước sâu phức tạp.

  • Mô hình hóa dòng chảy CO2 chính xác và mạnh mẽ.

Những lợi ích của phần mềm Olga

  • Tối đa hóa sản lượng và giảm thiểu rủi ro

  • Thiết kế và vận hành hệ thống sản xuất thành công đòi hỏi sự hiểu biết chi tiết về hành vi dòng chảy đa pha. Mô hình hóa và mô phỏng dòng chảy cung cấp những hiểu biết có giá trị về hành vi dòng chảy, bao gồm cả vật lý mô tả dòng chảy xuyên suốt toàn bộ hệ thống sản xuất, từ lỗ rỗng trong mỏ đến cơ sở xử lý.

  • Bộ mô phỏng Olga mô hình hóa các hành vi phụ thuộc thời gian, hay dòng chảy tạm thời, để tối đa hóa tiềm năng sản xuất. Mô hình hóa tạm thời là một thành phần thiết yếu cho các nghiên cứu khả thi và thiết kế phát triển mỏ. Mô phỏng động rất cần thiết trong khai thác dầu khí ở vùng nước sâu và được sử dụng rộng rãi trong cả các dự án phát triển ngoài khơi và trên bờ để nghiên cứu hành vi tạm thời trong đường ống và giếng khoan.

  • Những phát triển gần đây thông qua các dự án hợp tác công nghiệp về mô hình hóa dòng chảy CO2 cho phép thiết kế và vận hành đáng tin cậy các hệ thống vận chuyển và bơm CO2.

  • Tính linh hoạt trong các công cụ mô hình hóa PVT cung cấp cho các kỹ sư tùy chọn lựa chọn các công nghệ và phương trình trạng thái mà họ ưa thích.

  • Kiến trúc của bộ mô phỏng Olga cho phép chạy các mô phỏng trên đám mây để tối đa hóa dung lượng CPU khi khởi chạy nhiều mô phỏng để phân tích độ nhạy.

Download Olga và tải liệu:

Olga 2026.1

Product overview

The Olga™ dynamic multiphase flow simulator models transient flow (time-dependent behaviors) to maximize production potential. Transient modeling is an essential component for feasibility studies and field development design. Dynamic simulation is essential in deep water and is used extensively in both offshore and onshore developments to investigate transient behavior in pipelines and wellbores. Transient simulation with the Olga simulator provides an added dimension to steady-state analysis by predicting system dynamics, such as time-varying changes in flow rates, fluid compositions, temperature, solids deposition, and operational changes. The Olga simulator accurately predicts transient flow behavior across the entire production system—from wellbore dynamics through well completions to pipelines and associated process equipment.

Learn more about Olga

Release updates

As part of our ongoing commitment to excellence, we continuously innovate to enhance our product. This latest version brings multiple improvements, updates, and bug-fixes to benefit our users. The most important improvements are mentioned in this document below. Please read the release notes for the full overview.

 

Update of Symmetry Library

The latest Symmetry™ fluid engine release brings major stability and accuracy improvements for Olga compositional tracking and Symmetry flashes. Key highlights include:

  • Masked floating-point exceptions and corrected phase identification for gas–aqueous systems.
  • Enhanced pressure-enthalpy (P-H)-flash handling with consistent schemes for pressure-temperature (P–T) and PH flashes, ensuring stable density derivatives.
  • Fixes for internal flashes in inert and simplified three-phase cases when fluids are pure water or aqueous compounds.
  • Improved vapor-liquid equilibrium (VLE) predictions for CO₂–natural gas mixtures and better P-H-flash solutions for low-boiling-point fluids.

 

Update of Multiflash Library

The KBC Multiflash library has been upgraded from 7.5 to 7.6, delivering improved accuracy and robustness for compositional tracking simulations. Highlights include:

  • Enhanced advanced cubic EOS model with updated binary interaction parameters (BIPs) and component properties for better accuracy.
  • More robust extrapolation near the critical point for continuous property predictions (notably heat capacity and enthalpy).
  • Faster model initialization and updated EOS-CG (Combustion Gas) to the latest 2021 publication.
  • Improved handling outside validity ranges with a fallback cubic EOS method, while high-accuracy aqueous EOS remains active for tracking.

Additional improvements:

  • Better viscosity tuning with Pedersen and LBC models.
  • Updated mercury model. Licenses will be available through SLB.
  • Added THF and carbon monoxide as hydrate formers.

 

Update of PVTSim Library

The latest PVTSim Nova 7.2 release introduces key enhancements for Olga simulator integration:

  • Compositional tracking with PH Flash is now supported.
  • New option in the Olga tab file interface lets users control liquid–liquid splits. When two non-aqueous liquid phases occur (e.g. two hydrocarbons or a hydrocarbon and CO₂-rich phase), you can choose to merge them into one liquid or treat the lighter phase as gas in the tab file.
  • Ability to generate Olga PH tab files in both PVTSim Nova and PVTSim Nova CCS.

 

Intersect/p>

 

Directional leak functionality

The new directional leak feature improves depressurization simulations for stratified flow regimes, where gas sits above liquid in the pipeline. Unlike the default model (which assumes a well-mixed fluid), this functionality calculates leaked gas and liquid fractions based on:

  • Leak angle (position around the pipe circumference)
  • Leak diameter
  • Liquid level

This allows more realistic modeling of leaks dominated by either gas or liquid, depending on their position. Directional leak is only compatible with Olga new solver (CCS) in Olga 2026.1.

 

Intersect/p>

 

Equilibrium fluid model for pumps and compressors

Olga simulator now supports a new FLUIDMODEL key for centrifugal pumps and compressors, with two options:

  • IDEAL (default in Olga 2025.2 and earlier): assumes ideal gas and incompressible liquid.
  • • EQUILIBRIUM: uses the specified equation of state for more accurate calculations of pump head/torque and compressor compression ratio, without idealized assumptions.

 

CO₂ flow model

A dedicated CO₂ flow model is now available when the solver option is set to Olga new solver (CCS) and the flow model is set to Olga. It is designed for CO₂-dominated gas–liquid two-phase flow and ensures accurate simulation for these conditions. Compared to the Olga friction factor model, the pressure drop error is reduced by 51%, the hold-up error is decreased by approximately 31%, and the accuracy of flow regime prediction is increased by 34%.

 

Error on the pressure drop

Error on the hold up

Flow regime prediction accuracy

CO2 model improvement

Reduced by 51%

Reduced by 31%

Increased by 34%

Table 1 - Improvements for the CO2 model compared to the Olga friction factor flow model

 

Security enhancements

As part of SLB’s Software Lifecycle Management process, SLB will conduct tests to ensure that the software is free from security vulnerabilities and malicious codes, including viruses, trapdoors, trojan horses, or ransomware that could render the software inoperable or prevent its use as documented. If SLB becomes aware of such a threat, it will use commercially reasonable efforts to provide a patch or updated version of the software to eliminate or mitigate the issue, making it available for download or installation by the customer. SLB is not responsible for viruses introduced at the customer’s site or those that did not originate from the software.

With increased focus on security from both customers and internal initiatives, three scanning tools have been introduced for Olga simulator: Mend, Spectra Assure and FlexNet from Flexera. These tools scan for vulnerabilities and enable updates or replacement of outdated libraries.

Additionally, a penetration test was conducted on Olga simulator by a third-party company, which was successfully completed from the project’s perspective.

 

New output variables

Two new reservoir output variables have been added:

  • DPRES – Draw-down pressure
  • TMRES – Reservoir temperature

These variables provide enhanced monitoring and analysis capabilities for reservoir performance.

Additional variables have been added to capture and locate the minimum and maximum inner wall surface temperature (TWS) in branches.

  • MAXTWSBR – Maximum inner wall surface temperature in branch since start
  • MAXTWSPOS – Distance from branch inlet where maximum inner wall surface temperature since start occurs
  • MAXTWSBRCT – Maximum inner wall surface temperature in branch at current time
  • MINTWSBR – Minimum inner wall surface temperature in branch since start
  • MINTWSPOS – Distance from branch inlet where minimum inner wall surface temperature since start occurs
  • MINTWSBRCT – Minimum inner wall surface temperature in branch at current time

 

Node function improvements

Several updates have been made to node functionality:

  • INTERNAL node type renamed to MANIFOLD for clearer terminology.
  • Sources (mass flow, pressure-driven, or tracer) can now be added to manifold, separator, and phase split nodes, with the same capabilities as sources in flowpaths.
  • MASSFLOW node is obsolete and replaced by the manifold node.

Olga simulator cases created in version 2025.2 or earlier that include mass or internal nodes are automatically converted to manifold nodes when opened in the current Olga UI. Cases using manifold nodes are not backward compatible with older versions.

 

Steady-state preprocessor enhancements

The steady-state preprocessor (SSPP) now includes support for injection wells and negative pressure-driven sources, enabling more accurate modeling of CCS injection and drilling scenarios.

New options have been added to the steady-state preprocessor for RESREVOIRCONTACT through a new key INIWELLFLOW under BRANCH keyword. The following options are available:

  • Limit the solution to production only (PRODUCTION).
  • Limit the solution to injection only (INJECTION).
  • No limit on the solution. The steady-state preprocessor starts with a guessed production rate (INITPRODUCTION).
  • No limit on the solution. The steady-state preprocessor starts with a guessed injection rate (INITINJECTION).

 

Olga simulator's new solver

 

 

Performance improvements

Computational speed in the Olga simulator has been significantly increased through enhanced parallel processing.

Parallel processing has been optimized, providing additional benefits for running parallel simulations across most computer architectures. This improvement typically reduces simulation time by a factor of two to three (case-dependent) compared to Olga 2025.2. running simulations on four threads.

 

Users

The product is suitable for use by production, process, and flow assurance engineers, and those involved in multiphase flow simulation.

Olga 2025.2

Release updates

As part of our ongoing commitment to excellence, we continuously strive to enhance our product. This latest version brings multiple improvements, updates, and bug-fixes to benefit our users. The most important improvements are mentioned in this document below. Please read the release notes for the full overview.

Plots saved to the case-configuration

Previously, the plotting configuration for a case was discarded whenever the case was closed. Now, this configuration is saved within the case file, allowing plots to be automatically reloaded when the case is reopened. This enhancement applies to all types of 2D plots.

The feature can be disabled via the Olga options panel. Additionally, several plot-specific settings—such as axis scales, series scales, and series configurations—are now preserved as part of the saved configuration.

You can also now assign custom names to plots, making it easier to distinguish between them. When duplicating a case, the plotting configuration is carried over as well. However, if the result files are deleted, the plotting configuration will also be removed the next time the case is opened.

Plot-series alignment in plots

It is now possible to initialize profile and trend plots with an offset applied to the x-axis—length for profile plots and time for trend plots.

For profile plots, the offset granularity is per branch, allowing different branches to be arranged sequentially. In trend plots, the offset is applied per file, enabling simulation results to be shifted in time.

Offset values are preserved when the case is saved, ensuring consistent plot alignment across sessions.

Compare external data with Olga Simulations

We’ve introduced powerful new functionality to the plotting tool that enables you to import and compare external data directly with OLGA simulation results. For trend plots, you can now paste in measurement data along with corresponding timestamps to visualize and compare it against simulation outputs. For profile plots, in addition to time and data values, you can also specify a position, allowing for the comparison of spatial profiles along pipelines or other position-based data.

External datasets can be saved in CSV format, reopened later, and further edited directly within the plotting tool. This enhancement significantly improves the ability to validate simulations against field data and offers greater flexibility in your analysis workflow.

PVT packages for calculation of inhibitor properties

The PVT package used for calculating inhibitor properties is specified using the INHIBITORPROPERTIES key under the OPTIONS section. In addition to the previously available options—Simple and Multiflash—two new PVT packages are now supported: Symmetry and PVTSim..

Lennard-Jones viscosity model enabled for Multiflash

The Lennard-Jones viscosity model in Multiflash is now enabled for Olga compositional tracking simulations.

Level gradient in steady-state pre-processor

Previously, the level gradient term was not included in the steady-state pre-processor. Now, it is incorporated into the force balance calculations for oil and water layers within the steady-state pre-processor. The level gradient term influences the holdup calculations, particularly where changes occur due to pipe inclinations or rate adjustments. This is especially relevant at moderate superficial gas velocities with a very low liquid-to-gas ratio in large pipes. Incorporating this term into the steady-state pre-processor enhances the accuracy of holdup predictions.

However, this improvement comes at the cost of increased processing time, as the convergence time for the steady-state pre-processor may rise. It is important to note that in dynamic simulations, a more accurate steady-state condition can ultimately reduce the total simulation time. To illustrate the concept, a simple Olga model was set up, as shown in Figure 1

 

 

Olga
  Figure 1 - Olga model for demonstrating Level Gradient

 

An analysis of the hold-up trends using Olga version 2025.1.2 compared to Olga 2025.2, as depicted in Figure 2, reveals that the hold-up begins at 0.09 with a level gradient of zero for Olga 2025.1.2. As the simulation progresses, the hold-up value exhibits a declining gradient across the flowline. The simulation reaches a steady state after approximately 4.7 hours. The red line represents the hold-up value using Olga 2025.1.2.

 

 

Olga
  Figure 2 - Hold-up trends Olga 2025.1.2 vs Olga 2025.2

 

Comparing these results with Olga 2025.2, represented by the black line, it can be observed that the steady state pre-processor calculates the steady state conditions, allowing the simulation to directly reach steady state. Although the steady state pre-processor might take longer to converge, the overall simulation time could be shorter than before.

Olga 2024.2

Release updates

We continuously strive to enhance our product and Olga 2024.2 brings multiple improvements, updates, and bug-fixes to benefit our users. The most important improvements are mentioned below. Please read the release notes for the full overview. 

Improved Olga robustness

Stabilized well control simulations in the Olga simulator
 

Improvements to parametric studies

Improvements to parametric studies

Olga 2024.2 introduces the following important updates to the parametric study functionality:

  • Deletion of parameters: Users can now delete parameter columns in a study. A new “Delete Column” option is available in the right-click menu on the parameter column. If only one parameter is present in a study, the “Delete Column” menu item is disabled. 
  • Indicator for steady state pre-processor failures: Cases that end with a steady state pre-processor failure are highlighted in orange in the study window. This feature applies when the “Run” option is used to simulate cases.
  • Improved sorting in plotting: When plotting parametric study results, sorting is based on the entire case name rather than just the first digit. 

Improvement of inhibitor tracking 

Improvement of inhibitor tracking

Olga 2024.2 is released with improvements for the inhibitor tracking functionality. Previously, the Olga simulator relied on built-in correlations to adjust the density and viscosity of the water phase containing inhibitors. 

However, this approach could lead to inaccurate temperature calculations in the Olga simulator, e.g. for simulations where mono-ethylene glycol (MEG) or any other inhibitor was injected upstream a choke with a dP across the valve and Joule–Thomson (JT) cooling occurs. The new approach, released in Olga 2024.2, is using the Multiflash PVT package with high accuracy corresponding states model advanced (CSMA) equation of state (EOS) to adjust all water phase properties, such as density and viscosity of the water phase, but also thermal properties like thermal capacity and enthalpy. Notably, surface tension between water and gas, and between water and oil remains an exception. The improvement is relevant for COMPOSITIONAL equal to MEG, MEOH and ETOH. 

Olga simulator single phase version update

Olga simulator single phase 

In Olga 2024.1 Olga simulator single phase was introduced. Olga 2024.2 is released with expanded functionality for single phase. Single phase option (PHASE = GAS, OIL, WATER) is now compatible with COMPOSITIONAL = BLACKOIL or ON.

 

Stabilized well control simulations in the Olga simulator

Update of Multiflash library

Olga 2024.2 includes updated numerics to handle counter-current flow. In the past, during counter-current flow, the upstream control volume was retained from the last time step of co-current flow. However, when the upstream control volume became filled with one of the phases, there was no interface between the two phases, resulting in zero interface friction. This situation could lead to a stagnant column of a light phase (such as gas) not being displaced by a heavy phase (oil or water) in a vertical pipe, especially at very high heavy phase velocities. To remedy this, the total volume flow is used to determine the upstream conditions for slip calculations. Furthermore, the amount of oil/water in a control volume is used to limit the amount of oil/water dispersed in water/oil in transient simulations. This is applicable to bullheading as well as any other scenario with counter-current flow.
 

 

 

Uncertainty/noise in transmitter and controller output

Uncertainty/noise in transmitter and controller output

Olga 2024.2 introduces the functionality of applying uncertainty to controllers and transmitter signals. In the realm of uncertainty analysis, understanding how uncertainty affects measurements and parameter values is crucial. Accounting for uncertainty ensures robust decision-making and accurate system behavior. When uncertainty is applied to transmitters, it can represent measurement noise. When controllers are used to control parameter values on keyword keys, adding uncertainty on the controller output then represents input uncertainty on key value. Uncertainty can be applied to the transmitter OUTPUT as well as CONTROLLER outputs for controller types MANUALCONTROLLER and ALGEBRAICCONTROLLER. 

The uncertainty can be random, where the user selects either uniform distribution or normal distribution. Multiple identical shaped uniform distributions can be combined to form linear (order=1) and higher order distributions. Deterministic periodic uncertainty can be applied in terms of finite Fourier series.
 

Update of Multiflash library 

Multiflash

The KBC Multiflash™ library has been updated from the previous release, from 7.4.12 to 7.4.17. The new version contains several minor bug-fixes. 

Olga 2024

Release updates

Olga simulator single phase

In Olga 2024.1 we are introducing the first stage release of our Olga simulator single phase solution. This will be a lighter and faster version of the Olga simulator for handling single phase only. The improved version of the Olga simulator will minimize set of calculations required for pure single-phase flow to maximize simulation speed. In this way we can considerably improve efficiency and usability for the Olga simulator, when applied to single phase systems such as hydrogen simulations.

The following modifications are made:  

  • The user can select gas, oil, or water as single phase. This is selected under options in the Olga simulator. 
  • The rule engine in the Olga simulator has been modified for selecting single phase
  • Speed improvements compared to three phase calculations are achieved by:
    • Flash calculations being turned off 
    • Friction factors limited to single phase usage
  • The output variables are limited to single phase usage

Compositional tracking with Symmetry™ process simulation software

Olga 2024.1 is released with the possibility of using the Symmetry software fluids engine as an option for compositional tracking. Symmetry software can be selected as the compositional engine under COMPOPTION in the Olga simulator. The Symmetry software fluids engine is a powerful and accurate thermodynamics engine, part of the SLB software offering, bringing consistent thermodynamics from pore to product. The Symmetry software fluids engine is at the core of Symmetry software and has been imbedded in other software products including the Pipesim™ steady-state multiphase flow simulator. The Symmetry software fluids engine contains the most advanced simulation technology for fluids and has been extensively and continuously validated with data from the National Institute of Standards and Technology (NIST). Its fluid characterization system contains not only the traditional characterization techniques but also includes the molecular structure based fluid characterization enabling better modeling of the fluid’s properties since it considers not only physical properties but also chemical structures within the fluid. The Symmetry software fluids engine is completely tunable since components and equations of state (EOS) parameters can be modified to match experimental data.

Switch transient off for part of network

Olga 2024.1 is released with the possibility of freezing the transient calculations for a branch. This is done by adding “SIMULATIOINOPTIONS” for a flow path and setting the transient key to “FREEZE” or “NOFLOW”. If “FREEZE” is selected, no calculations are done for the flow path. If “NOFLOW” is selected only temperature calculations are conducted where only thermal capacity of the fluid is considered.

Further details on changes to Olga 2024.1 can be found in the Olga simulator release notes which are available for download via the production software download server on the SLB Software Download Center.

Update of Multiflash library

The KBC Multiflash™ library has been updated from the previous release from 7.3 to 7.4. Version 7.4 has the following important updates: 

  • Improved accuracy for CO2 modelling
  • Improved CO2 hydrates model
  • Improved PH flash stability
  • Improved GERG-2008/EOS-CG
  • AGA-8 density support
  • Improved data regression
  • Polymers modelling and perturbed chain statistical associating fluid theory (PC-SAFT) 

The new version also contains several minor bug-fixes. The binary interaction parameters were updated for a few binaries, with a view of improving the modelling around Carbon Capture applications.

IKH and VKH indicators in the Olga simulator

Olga 2024.1 is released with inviscid Kelvin–Helmholtz (IKH) and viscous Kelvin–Helmholtz (VKH) stability indicators as output. VKH instability combined with stratified flow may indicate large wave flow in the system. The user can then investigate wave formation and propagation using a fine grid dynamic Olga simulator model and the second order mass equation scheme in the Olga simulator. The VKH and IKH stability analysis is implemented as described in [1] and [2]. The indicators are available for plotting in the Olga simulator, and results from calculations that can be plotted in the same way as flow regime maps in the multiphase tool kit. The indicators are also available in the steady state preprocessor, enabling the possibility of creating a preprocessor parameter study to identify the boundary conditions causing VKH instabilities. The implementation is further backed by a paper on the appearance of single slugs [3].

[1] Barnea, Taitel: ”Interfacial and structural stability of separated flow” ; 1994, Int. J. Multiphase Flow Vol. 20, Suppl., pp. 387--414 

[2] Barnea, Taitel: ”Stratified three phase flow in pipes – Stability and transition” ; 1996, Chemical Engineering Communications, 141-142:1, 443-460, DOI: 10.1080/00986449608936428

[3] Roel Belt, Chris Lawrence, Henrik Eiding, Gunnar Staff, “Growth of solitary slugs in long flowlines”, 10th International Conference on Multiphase Flow, ICMF 2019, Rio de Janeiro, Brazil, May 19 – 24, 2019

[4] D. Biberg, M.B. Kirkedelen, P. Sassan Johansson, M. Nordsveen, T. Kindsbekken Kjeldby, "A New Mechanism for Flow Instabilities in Gas-Condensate Fields at Low Production Rates" 20th International Conference on Multiphase Technology, Multiphase 2023, Nice, France 26th-28th June, P257-271

Windows 11 compatibility

Olga 2024.1 has been tested with Windows 11 and found compatible. 

User

The product is suitable for use by production, process, and flow assurance engineers, and those involved in multiphase flow simulation.

Olga 2023

Release updates

Olga Model Management


Olga 2023 is being released with Olga Model Management compatibility. 
Olga Model Management is a cloud-powered model management solution providing a unified, collaborative ecosystem where models can be easily shared between different types of consumers such as:  

  • Existing users of the Olga simulator on laptop or desktop 
  • Existing users on the Delfi™ digital platform
  • Web applications: cloud and edge digital workflow solutions 
  • Digital services: scalable simulation, calibration, machine learning (ML)

Olga 2023 is released with the possibility of: 

  • Opening Olga simulator cases from Olga Model Management
  • Running cases locally 
  • Publishing models and simulation results back to Olga Model Management
  • Keeping track of model versions and changes
  • Easily comparing cases

The solution is subscription based. The user will need a Delfi user account and an Olga simulator license. 

The Olga simulator GUI will have some new functionality related to Olga Model Management. As can be seen from the screenshot in Figure 1 below, “Open Case From Cloud” is included in this new version.


Reynolds number

Reynolds number for the gas, oil, and water layers are exported as output variables.

Previously, Reynolds numbers for each of the layers in the Olga simulator were not accessible to users. In this release, they are being made available as part of boundary variables. There are three new variables for separated flow: gas (REYGSEP) , oil (REYHLSEP), water (REYWTSEP), and three new variables for dispersed flow: gas (REYGDISP), oil (REYHLDISP) , water (REYWTDISP). The separated flow Reynolds numbers are non-zero if the gas-liquid flow regime is stratified (ID=1) or annular (ID=2), unless the respective layer(s) is absent in the system, while the dispersed flow Reynolds numbers are all zero. The reverse is true if the gas-liquid flow regime is bubbly flow (ID=4). If slug flow prevails (ID=3), then all Reynolds numbers are non-zero except when the respective layer(s) is absent. The separated Reynolds numbers correspond to the bubble zone Reynolds number while the dispersed Reynolds numbers correspond to the slug zone Reynolds number. The non-zero values have lower limit of 0.1.

Use of saturation curve for temperature of a source and a node

A new subkey, saturation temperature (TSAT), is added to source, pressure node, and mass flow node.  TSAT can be off or on, with off as the default. This subkey can be used only if “COMPOSITION=SINGLE” or “STEAMWATER_HC”. When the TSAT is set to off, the temperature must be specified. When the TSAT is set to on and “COMPOSITION=STEAMWATER_HC”, the temperature is calculated based on the water saturation curve at the given pressure and user must input “STEAMFRACTION”.  When the TSAT is set to on and “COMPOSITION=SINGLE”, the temperature is calculated based on the saturation curve of the single component at the given pressure and user must input “GASFRACTION”.

New output variables for mass flow fraction

The following trend and profile output variables are now available as mass flow fractions at a section boundary, using absolute flowrates (STEAMWATER-HC fluid option).

 
New output variables
 Description
 GASFMFR  Gas mass fraction relative to total mass rate of gas, oil and water phase
 OILFMFR  Oil mass fraction relative to total mass rate of gas, oil and water phase
 WATFMFR  Water mass fraction relative to total mass rate of gas, oil and water phase

Further details on changes to Olga 2023 can be found in the Olga simulator release notes which are available for download via the production software download server on the SLB Software Download Center.

Users

The product is suitable for use by production, process, and flow assurance engineers, and those involved in multiphase flow simulation.

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