A mixture of liquid hydrocarbon product and gas from a cracking unit enters a high-pressure separator V1. The vessel operates at a pressure of 50 barg (design pressure 55 barg) and a temperature of 30C. The gas offtake (methane) is directed to a compression system for subsequent treatment and export into the sales gas pipeline. The liquid from V1 (mostly butane) is transferred to the low-pressure separator V2. V2 operates at a pressure of 10 barg (design pressure 12 barg) also at a temperature of 30C. Gas from this vessel (a mixture of methane, ethane and propane) is directed to the fuel gas system. Pressure relief valves are located on each vessel. Vessel V1 relief discharges via PRV1 to a HP (high pressure) 10” flare line (back pressure 2 barg) and vessel V2 relief via PRV2 to a 18” MP (medium pressure) flare line (back pressure 0.7 barg). The flow from V1 to V2 is under level control (via loop LIC1) which maintains vessel V1 at 50% full. The orifice diameter for the level control valve when fully open is equivalent to a diameter of 30mm.
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