The industry is trending towards less conventional oil resources, and as a result feed qualities have suffered in terms of salts, higher TANS etc.
Due to higher salt contents in the feed deposition temperatures are higher.
Has anyone operated a unit where the coker fractionator overhead temperature is lower than the NH4Cl deposition temperature. Taking into account that the system has a continuous water wash for the overhead exchangers and with the ability to water wash the tower in times of need.
Due to higher salt contents in the feed deposition temperatures are higher.
Has anyone operated a unit where the coker fractionator overhead temperature is lower than the NH4Cl deposition temperature. Taking into account that the system has a continuous water wash for the overhead exchangers and with the ability to water wash the tower in times of need.
