Applying plate heat exchangers in crude preheat train for fouling mitigation

Application of Threshold Model with Various Tube Wall Temperatures for Crude Oil Preheat Train Fouling

The Propose of this paper is to introduce a new model for crude oil fouling in preheat trains of crude distillation unit. The experimental results of Australian light crude oil with the tube side surface temperatures between 200-260 oC and fluid velocity ranged 0.25 to 0.4m/s were used. The activation energy of chemical reaction depends on the surface temperature has been calcula...

Fouling in Heat Exchangers

An Industrial Case Study on Retrofitting Heat Exchangers and Revamping Preheat Trains Subject to Fouling

Crude refinery preheat trains (PHTs) are a major part of a refining process as these units reduce the amount of thermal energy required to heat the crude oil to its distillation temperature. Fouling is a longstanding problem in the operation of PHTs; the ability of a refinery to process different crude blends or to increase its production capacity depends on the thermal and hydraulic performanc...

application of threshold model with various tube wall temperatures for crude oil preheat train fouling

the propose of this paper is to introduce a new model for crude oil fouling in preheat trains of crude distillation unit. the experimental results of australian light crude oil with the tube side surface temperatures between 200-260 oc and fluid velocity ranged 0.25 to 0.4m/s were used. the activation energy of chemical reaction depends on the surface temperature has been calculated.  the model...

investigation of crude oil fouling on performance of preheat exchangers of crude distillation unit (cdu)

in this article the effect of fouling on tube side and the overall performance of preheat exchangers of crude distillation unit of petroleum refinery have been investigated. for this purpose the experimental data of australian light crude oil in surface temperature of 200-260oc and the velocity between 0.25 to 0.4 m/s have been used. first, an overall dirty heat transfer coefficient was calcula...