Heat Exchangers Final o k= 0.667 wimk 75 25C 50 C of heat transfer coefficient LK) pouling coere ch @oil with a flow rate listovs (p=92417 Aglocp=4198 51 ngK : Agim CpJ in 3.78 x 10-3 heat exchanger. Iniet temperature of oil is Ims) kg curl be healed in a plate and outlet temperature Heating process will be niet temperature of EsC and occomplished by hot water at The convective heat transfer coefficient outlet temperature 75C. water 4000 Lem? ond fouling coefficient for the oil side is 2500 wim?K. The fouling coefficient for hot water side and wall resistance can be nedtected. Considering that the heat transfer operated series arrangement calculate the number of plotes required. NUE 0,26x Re PC Distance between plotes 3 mm 0,003 kwater = 4000 Plate width- lomm = 0,210m (4x) Plate height = 900 mm Effective 1.5x Projected area cuill be 0165 0 0 0,9m areo = Heat Exchangers Final o k= 0.667 wimk 75 25C 50 C of heat transfer coefficient LK) pouling coere ch @oil with a flow rate listovs (p=92417 Aglocp=4198 51 ngK : Agim CpJ in 3.78 x 10-3 heat exchanger. Iniet temperature of oil is Ims) kg curl be healed in a plate and outlet temperature Heating process will be niet temperature of EsC and occomplished by hot water at The convective heat transfer coefficient outlet temperature 75C. water 4000 Lem? ond fouling coefficient for the oil side is 2500 wim?K. The fouling coefficient for hot water side and wall resistance can be nedtected. Considering that the heat transfer operated series arrangement calculate the number of plotes required. NUE 0,26x Re PC Distance between plotes 3 mm 0,003 kwater = 4000 Plate width- lomm = 0,210m (4x) Plate height = 900 mm Effective 1.5x Projected area cuill be 0165 0 0 0,9m areo =