22 Sep, 2015

# Visit us at SPE ATCE 2015

Are you planning to be at the SPE Annual Technical Conference & Exhibition (ATCE), September 28th – 30th in Houston, TX? If so, we welcome and encourage you to stop by our booth, 2317, and discuss how our comprehensive workforce development solutions can help your organization keep moving forward!

3 Sep, 2015

# Gas-Liquid Separators Sizing Parameter

In this Tip of the Month (TOTM), we will focus on the application of Souders-Brown approach in gas-liquid separators and present diagram, simple correlations and tables to estimate the Souders-Brown equation constant, KS (the so called sizing parameter). We will consider both vertical and horizontal gas-liquid separators. Knowing the actual gas flow rate through the vessel, one can use KS parameter to determine the maximum allowable gas velocity through the vessel and determine the required separator diameter. One can also use the appropriate value of KS to size the mist extractor in the vessel. The performance of a gas-liquid separator is highly dependent on the value of KS; therefore, the choice of appropriate KS –values is important.

11 Aug, 2015

# PetroSkills Instructors welcomed into SPE’s ‘Legion of Honor’

Two PetroSkills instructors, Mr. Richard Schroeder and Dr. George Slater, were recently welcomed into the Society of Petroleum Engineers (SPE) Legion of Honor. Both have held their SPE membership for 50 consecutive years. SPE honored each with a commemorative plaque and exempt dues for the remainder of their membership.

3 Aug, 2015

# Effect of Relative Density (Specific Gravity) on the Saturated Water Content of Sweet Natural Gases

In this Tip of the Month (TOTM), we will study the effect of relative density (Specific Gravity, SG) on the saturated water content of sweet natural gases. The results of this study include the water content of sweet natural gases as a function of relative density in the range of 0.60 to 0.80. Four temperatures of 4.4, 23.9, 37.8 and 149 °C (40, 75, 100, and 300 °F) were considered. For each temperature, the saturated water content was calculated for pressures of 1724, 3448, 6897, and 13 793 kPaa (250, 400, 100 and 2000 psia).