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Therefore, when the pressure in the vessel exceeds a maximum 3 psi, gas in the separator will pass directly to the mud room. In this case, the mud room had minimal ventilation. Any serious well control operation would not be possible with this arrangement. The size and length of the flare line from the separator to the flare pit are important components of the system. The larger the flare line, the better. The flare line must be straight and not less than 6 inches in diameter. In the prolific Tuscaloosa Trend, 12-inch flare lines are common.

It has been a practice in some areas to take a kick to determine specific pore pressures and reservoir fluid composition. In areas where formation productivity is historically low (roughly less than 1 million standard cubic feet per day without stimulation), operators often drill with mud hydrostatics below the pore pressures. Mud weight requirements are not always known for certain areas. The ability of the industry to predict formation pressures has improved in recent years and is sophisticated.

When the well blew out, a new road had to be constructed before well control operations could be commenced. Finally, fluid entry into the vessel is important. Some separators are designed to permit tangential entry. That is, the fluid enters tangential to the wall of the vessel. If the fluid is only gas and liquid, the design is satisfactory. However, if the fluid contains any solids, the vessel will erode rapidly. A perpendicular entry is best. 22. 23) is to provide remote hydraulic access to the well.

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