FLOWSOLV®
V5.2 builds on our successful oil and gas calculation software, adding four new
light hydrocarbon liquid calculation methods for NGL (Natural Gas Liquids) and
LPG (Liquified Petroleum). The new standards added include:
·
API
MPMS Chapter 11.2.2: 1986 Compressibility
for Light Hydrocarbons with Relative Density of 0.350 to 0.637 at 60°F
·
API
MPMS Chapter 11.2.2M: 1986 Compressibility
for Light Hydrocarbons with Density of 350 to 637 kg/m3 at 15°C
·
API
MPMS Chapter 11.2.4: 2007 Temperature
Correction for Volume of NGL & LPG Tables 23E, 24E, 53E, 54E, 59E, &
60E
·
API
MPMS Chapter 11.2.5: 2009 Simplified
Equilibrium Vapour Pressure Correlation for Commercial NGL & LPG
These new
additions enable the calculation of compressibility, temperature correction
factors, density correction factor and the estimation of equilibrium vapour
pressure for NGL and LPG light hydrocarbon liquids.
The entire
FLOWSOLV® V5.2 PRO Oil & Gas package contains 50 oil and gas calculations
which cover instrument, fluid, measurement, and utilities for fiscal,
allocation, well test and process applications. FLOWSOLV® V5.2 calculations are
developed to conform to recognised international standards used in Fiscal and
Custody Transfer Flow Measurement. All inputs and outputs are checked for
compliance with the standards and non-compliance entries are clearly
identified. With 12 months support including free upgrades during the support
period and support from the flow measurement experts at SOLV® you will have a
great resource at your fingertips.
The evaluation
version of FLOWSOLV® V5.2 PRO Oil & Gas will run for 30 days and can be re-activated
by purchasing a copy. The evaluation version does not allow you to load or save
a file or to print but allows you to do full calculations. Once you have had
the opportunity to evaluate our product, we would welcome any comments and
feedback you have which may assist with future developments.
Existing
users can also update from FLOWSOLV® V5 or V5.1 to V5.2 with this download.
With the release of FLOWSOLV® V5.2 Windows 7 and Vista are no
longer supported, as Microsoft have ceased support for this software. FLOWSOLV® V5.2 is supported on all versions
of Microsoft Windows 8 and Windows 10.
Details on
our new NGL and LPG light hydrocarbon liquid calculation methods:
API MPMS Chapter 11.2.2: 1986 Compressibility
for Light Hydrocarbons with Relative Density of 0.350 to 0.637 at 60°F
This
calculation corrects hydrocarbon volumes metered under pressure to the
corresponding volumes at the equilibrium pressure for the metered temperature.
It contains compressibility factors related to the meter temperature and
relative density (60°F/60°F) of the metered material. The corresponding metric
(SI) version is API MPMS Chpt. 11.2.2M:1986
API MPMS Chapter 11.2.2M:
1986 Compressibility for Light Hydrocarbons with Density of 350 to 637
kg/m3 at 15°C
This
calculation corrects hydrocarbon volumes metered under pressure to the
corresponding volumes at the equilibrium pressure for the metered temperature.
It contains compressibility factors related to the meter temperature and
density at 15°C of the metered material. The corresponding customary version is
API MPMS Chpt. 11.2.2:1986 Amd.1994.
API MPMS Chapter 11.2.4:
2007 Temperature Correction for Volume of NGL & LPG Tables 23E, 24E,
53E, 54E, 59E, & 60E
This
calculation is used to determine the Temperature Correction Factor, given an
appropriate Density Factor at Base Temperature and an Observed Temperature. The
calculation also finds the appropriate Density Factor at Base Temperature given
a relative density at an Observed Temperature.
·
Six
tables are included in the calculation.
·
Tables
23 and 24 are at 60°F base temperature,
·
Tables
54 and 53 are at base temperature of 15°C
·
Tables
60 and 59 are at base temperature of 20°C.
API MPMS Chapter 11.2.5:
2009 Simplified Equilibrium Vapour Pressure Correlation for Commercial NGL
& LPG
This
calculation provides a simplified means of estimating Equilibrium Vapour
Pressures of various Natural Gas Liquids (NGLs) from the fluid’s Relative
Density (60°F/60°F) and Process Temperature.
23rd April 2020