Latest Update - FLOWSOLV® V5.2

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.

FLOWSOLV® V5.2 EVALUATION

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.

 

FLOWSOLV® V5.2 EVALUATION

23rd April 2020