It was found that at a column pressure of 8.5 barg and reboiler temperature of 180 ☌, the condensate is successfully stabilized to a RVP of 60.6 kPa (8.78 psia). The operating conditions which gave rise to the production of off-specification condensate were found. feed flow rate, temperature, pressure and reboiler temperature on the product Reid Vapour Pressure (RVP) and sulphur content were also studied. The effects of four process conditions, i.e. It was found that the simulation is closely matched with the plant data and in particular for medium range hydrocarbons. The results were also compared to the results obtained using PRO/II software. A simulation was conducted using Aspen HYSYS ® software for an industrial scale condensate stabilisation unit and the results of the product composition from the simulation were compared with the plant data.
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