Download Campbell GCAP 10.2.1
GCAP software full crack license download from John M. Campbell from PetroSkills and This software is designed to aid the facilities engineer, process engineer, and manager with a quick review of detailed calculations done by someone else to check for accuracy. It is not designed to replace process simulators or equipment manufacturer’s verification.
Every engineer’s daily routine requires him to give quick checks and quick ideas for very complicated calculations. John M. Campbell & Co.’s solution: GCAP™. This software companion to volumes 1 and 2 of our “Gas Conditioning and Processing” series is based on the equations and correlations referenced in our textbooks.
To calculate the density of hydrocarbon liquids, the method of calculation must be decided. If the Molecular Weight is known but the Relative Density is not, select “Molecular Weight known” by clicking on and shading the circle provided for that selection. This will yield an answer for Relative Density. If the Relative Density is known but the Molecular Weight is not, select “Relative Density known” by clicking on and shading the circle provided for that selection. This will yield an answer for Molecular Weight.
Key Features of the GCAP software
- 3A. Physical Constants
- 3B. Properties of Paraffin Hydrocarbons
- 3C. Gas Compressibility and Density by Several Methods
- 3D. Liquid Density by COSTALD (Hankinson-Thomson) Method
- 3E. Approximate Correlation Between MW and Relative Density for Hydrocarbon Liquids.
- 3F. Effect of T and P on the Density of Liquid Hydrocarbon Mixtures
- 3 G. Relative Density of Liquids Containing Methane and Ethane
- 3 H. Viscosity of Paraffin Hydrocarbon Gases
- I. Viscosity of Liquid Hydrocarbons at Atmospheric Pressure
- 3 J. Viscosity of Crude Oils
- 3.K Surface Tension for Paraffins
- 3L. Surface Tension using the equation 3.28
- 5.A Bubblepoint, dewpoint, and flash calculations (SRK EOS)
- 5B. Properties of Hydrocarbon liquids
- 5C. Conversion between mole, volume and weight percent
- 5D. Composite stream analysis
- 6A. Water Content of Sweet, Lean Natural Gases
- 6B. Water Content of Sour Natural Gases
- 6C. Hydrate Formation T at Specific P (Katz)
- 6B. Water Content of Sour Natural Gases
- 6D. Hydrate Formation T at Specific P (Trekell-Campbell)
- 6E. Hydrate Inhibition Calculations
- 8A. Hydrocarbon Liquid Enthalpy using the Charts in Appendix 8A.
- 8B. Hydrocarbon Vapor Enthalpy using the charts in Appendix 8A
- 8C. The enthalpy and entropy of a two-phase stream by the SRK EOS
- 8D. The enthalpy of a two-phase stream from that of the vapor and liquid.
- 8E. Heat capacity and heat load for liquid hydrocarbons
- 8F. Heat capacity and heat load for 0.65-0.75 relative density natural gas
- 8G. Latent heat of hydrocarbon mixtures
- 8H. Pressure-enthalpy diagram of Propane, R-22 or Ammonia
- 10A. Total pressure Drop using Equation
- 10 B. Pipe Diameter using Equations
- 10C. Pipe Capacity using Equations
- 10D. Pipe Friction Pressure Loss Using Equation
- 10 F. Horizontal Gas Flow Rate Calculations
- 10 H. Static Pressure Due to Elevation Change, Equations
- 10J. Temperature Drop in Buried Lines Using Equation
- 10K. Maximum Temperature in Above Ground Lines Using Equation
- 10L. Capacity (Two-Phase-Modified Flanigan Calculation for Flow Lines)
- 10O. Equivalent Length Calculations using Equations in Table
- 10P. Equivalent diameter calculations for pipes in series
- Supported operating systems: Windows 10 & 11 x64/ Windows 8.1
- File size: 14 MB
- Crack: full crack (unlimited PC)
