
Summary of New Features in WELLFLO 7
·
Production
Mode - A new
‘Production’ mode is now available for quick and easy modeling of a producing
oil or gas well.
·
Tubular
Database - An
industry standard tubular database has been added as an option for selection of
tubing and casing dimensions.
·
VMG
Flash - A new
comprehensive set of up-to-date compositional equations of state from Virtual
Materials Group is now available as optional VLE (Flash) calculations.
·
New
Electrically Heated Tubing Option - The ability to model the effect of electrically
heated tubing on the hydrodynamic and thermodynamic performance of a well has
been added.
·
OLGAS2000
2-Phase in Rigsite Mode- The simplified UBD interface ‘Rigsite’ now offers the option to run
OLGAS2000 2-phase from ScandPower if licensed for this option.
·
Nozzle
Diameter Database - A
database of nozzle diameters has been added as an option for the drill bit of a
BHA for UBD applications.
·
OLGAS2000
3-Phase - WELLFLO
‘Expert’ mode now has OLGAS2000 3-phase from ScandPower as an option for
3-phase flow modeling. Contact Neotec
to activate this license.
·
Plotting
Improvements - Changes
have been made to the plotting system to allow synchronization of axes, improve
appearance, add scaling features, and save settings for future plots.
·
Rigsite
Mode - WELLFLO now
supports a ‘Rigsite’ GUI mode that is specially designed for quick and easy
data entry for UBD modeling.
·
Deliverability
Curve XML File - The
option to create an XML file containing deliverability curve information has
been added. This deliverability curve
information can then be imported into PIPEFLO.
This option is only available for a Wellhead Performance parametric
case.
·
Individual
Rates Option - An
‘Individual Rates’ option was added to IPR Flow Basis selections for a ‘Total
Flow Per Section’ IPR in the production casing.
·
Single
Section IPR Option - A
‘Single Section IPR’ option has been added to the production casing, so that a
user can add a single IPR section that is independent of the casing geometry.
·
Ignore
Facility Option - An
‘Ignore this Facility’ check has been added to all tubing and production casing
facilities (Point Source, Injection Point, Choke, BHA and ESP). When this option is selected, the data entry
screens for the facility will be disabled, the facility will not appear on the
schematic, and the facility will not be used in any calculations.
·
Calculation
Improvements
-
The
Thermal Expansion method used to compute specific gravity from relative gravity
or vice versa has been updated to now permit temperatures greater than 500
degrees Fahrenheit. Temperatures
greater than 500 degrees Fahrenheit now generate a warning message.
-
Point
source and Injection Point facilities now post stream warning messages.
-
The
minimum cuttings transport ratios for horizontal, inclined and vertical flow
are now reported in the summary output file.
-
IPR curves
are now generated anytime that a bottom hole IPR is present.
-
The
valid range for entropy values has been expanded from -10 to 10 BTU/lb-deg F to
-20 to 20 BTU/lb-deg F.
-
The
Watson Modified Oil Enthalpy correlation has been upgraded to now support a
negative API oil gravity.
·
XML
Fluid Import/Export Improvements - Minor modifications have been made to the XML
fluid import/export capabilities to improve their usability.
·
Multiple
Residuals - In
previous versions, the user was restricted to a single residual in a case. This restriction has been removed.
·
Frictional
Quality Multiplier for Foam - The user specifiable foam properties now include a frictional quality
multiplier.
·
New
Plotting Design - A
new plotting package has replaced the previous one in NeoGraph. One of the more significant options in this
new plotting package is the ability to plot two separate X axes against a
common Y axis.
·
ESP Facility and Database – An
Electric Submersible Pump can now be added anywhere in the well to apply
artificial lift. Users can enter their own performance data, choose from
a database of commercial ESP’s, or customize the existing database.
·
ESP Performance Curve Parametric Option – Using the
WELLFLO 7 parametric data option, the performance of an installed ESP can be
evaluated over a range of flow rates or bottom-hole pressures.
·
Power Management – Especially for
laptop users, an automated “power down” no longer causes the Neotec security to
fail due to inactivity.
·
Transient Buried Heat Transfer Environment – Well
bore heating/cooling can now be analyzed using a time-dependent heat transfer
computation based on the work of Ramey (1962), Willhite (1967), and Shinohara
(1979). This development was motivated by the requirements of geothermal
well analysis but is also applicable for any injection, production, or
circulation system with potential transient thermal concerns (i.e. hydrate
formation).
·
Helium Addition to Compositional and Limited
Compositional – Helium has now been added as a new component in the
fluid property library.
·
Eclipse Table Generation Changes – The
results from a well performance analysis can now be automatically tabulated and
output to an Eclipse™ compatible file for processing by that reservoir
simulator.
·
Injection Point Facility – At any depth in
the well, additional fluid can be added to the well to account for an injection
point. This could be used to simulate chemical injection or artificial
lift as the result of parasitic tubing injection, continuous gas-lift, or
concentric annulus injection.
·
Parametric Injection Point Capabilities –
Performance curves for multiple injection rates can be generated using the
parametric data option for a range of pressures or flow rates in the
well. This is especially useful to determine hydraulically optimum
gas-lift rates.
·
User Defined Unit Sets – Units for each and
every data item in the user interface can be selected independently and saved
in a custom Unit Set which can ultimately be shared with other users.
·
Calculation Engine Changes – The
non-compositional gas enthalpy prediction has been expanded beyond the previous
limit of 3000 psia, to 6000 psia. The corresponding non-compositional oil
enthalpy prediction has been improved to include a pressure and oil gravity
dependence.
·
Output Plot and Report Changes
-
NeoGraph has been modified to display only the
filename (as opposed to the full path and filename) when multiple XLS plot
files are displayed for comparison.
-
The P02 diagnostic file has been modified to report
the temperature profile across the various layers from the tubing to the
surroundings.
-
The gas max volume fraction for injection cases is now
reported in the mini, maxi and summary output files.
-
Both the per case and summary XLS output files now
report the wellhead and bottom hole pressures in their respective injection
point tables.
-
The in situ gas volume fraction is now reported
in the detailed report section of the .max output file and the XLS output
file. Additionally a gradient plot is now available to display the in
situ gas volume fraction.
-
The estimated height of the static column of liquid
for injection or production cases if the well is shut in is now reported in the
.min, .max and .sum output files. Additionally, the measured depth to the
top of the static column of liquid is reported in the summary section of the
.min and .max output files.
-
The cumulative liquid holdup and cumulative gas pack
for both production and injection cases as well as the total for circulating
cases is now reported in the summary section of the mini and maxi output files
and the summary output file.
-
The cuttings transport ratio is now reported in the detailed
results section of the .max output report.
·
Fluid Import/Export Capabilities – In the
Fluid Manager, users can now import or export fluid definitions to facilitate
the sharing, and storage, and retrieval, of fluid characterizations whether
compositional or non-compositional.
·
Water Saturation Calculation – An
option for computing the gas saturated water mole fraction has now been added
to the compositional data entry screens. This provides a convenient way
of characterizing the fluid molar composition to include only water of
saturation in the gas phase.
·
‘What’s New in this Version’ Help menu item – An
option on the Help menus now reveals a brief list of the new features contained
in the current release.
·
Wellhead and Bottomhole Stream Labeling Changes for
Drilling – Labels on various data entry screens have been
changed to be more suitable for drilling applications when the relevant options
are selected.
·
User Defined Initial Guess for Reverse Pressure
Calculation – For difficult convergence cases where an iterative
calculation is requested, a new option allows entry of an initial guess to
speed up the solution search algorithm.
·
‘Save As’ button on Main Toolbar