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At a Visbreakeing unit(coil type visbreaker) I worked on, the gas oil was drawn from the main fractionator to a gas oil stripper and then transferred via a pump to visbroken bottoms stream. We faced frequent high ampere problem at this pump. The pump returned to its normal amperes after its impeller was cleaned. Coke deposition was found on the impeller, suction strainer and discharge NRV. We had cut stripping steam to the gas oil stripper previously to decrease the overhead naphtha, however it was taken back in service to get the system back to 'design' conditions and doing so, reduced the frequency of high amperage problem. (The pump delivers 2~3 m3/hr gas oil flow. At higher flows it reaches/exceeds FLC(full load current). The pump's design minimum flow is 12 m3/hr.)
Can anyone please suggest possible remedies to this problem, specially the coke deposition at pump's impeller? Is it fairly common to have coke deposits in visbreaker gas oil lines if so what are some practices to reduce/remove the coke?
 
Answers
06/07/2018 A: Ravi shankar, HPCL, prskreddy@hpcl.co.in
Try a sort of spill back of cooled gasoil to be used as quench into the GO main take off line off the column (Column take off to Go pump suction ) in order to quench the Go to pump suction by a few degrees (I do not know your GO take off temperature to suggest the actual temp) or simply you may go for an Restricted orifice into such line based on heat balance to suit your needs.
Also there are some commercial coke preventers that can be dosed into the line to prevent Coking.