Specific Gravity of P-5 Fluid at.799.813.
Therefore, hvgo reflux temperature (E-6 outlet quel cadeau offrir a son copain pour les 1 an temperature) is set 145 oC (5 oC.6 higher than actual normal temperature).
H-1 duty reduction, 106 kcal/hour 1).796.
Loss caused by refinery/complex HP Steam product increase to supply let down system, US/hour 7) 156.9 Kerugian, US /hour 288.7 Total Loss, US/hour 251.3 Note : 1) H-1 duty reduction H-1 A duty reduction H-1 B duty reduction.P-5 Pumping temperature, oC 135 140.21.By Adhi Budhiarto.This table can be used for estimating the steam consumption in the preliminary design of steam applications.E-7 outlet temperature, oC 110,06 80 104,26.H-1 fuel consumption saving, tsrf/hour 2).1833.Prediction, oC 75,491 69,69 1).P-5 Casing Maximum Temperature, oC 450.H-1 fuel consumption saving, Bbl/hour.1762.From above simulation software results, it can be concluded that the proposal Reducing Charge Heater Fuel Consumption by Bypassing some hvgo from hvgo/BFW Heat Exchanger (Pre-heater) which can Increase Charge Heater Inlet Temperature with the Compensation of Reducing Medium Pressure Steam Production is technically feasible. .Feasibility Study Considering design and actual data shown in Table I, process/technical evaluation to the proposal is done with a limitation of hvgo storage tank temperature (it must be 80 oC, which is the storage tank design maximum temperature) and also by considering other parameters.
6) Because there is no MP Steam data in the company finance department which can be used, then MP Steam price is calculated based on its caloric value.
H-1 atomizing steam consumption saving, kg/hour.625.
Hvgo reflux temperature (E-6 outlet temperature oC 145.2 E-1.Do technical study on the proposal Reducing Charge Heater Fuel Consumption by Bypassing some hvgo from hvgo/BFW Heat Exchanger (Pre-heater) which can Increase Charge Heater Inlet Temperature with the Compensation of Reducing Medium Pressure Steam Production.2.By having higher E-3 concours next annales hvgo inlet temperature as E-3 heating media, E-5 Total Feed outlet temperature will also be higher which will increase inlet temperature of H-1 A/B. .Total Feed from E-5 is divided into 2 streams, to charge heater H-1 A and charge heater H-1. .Then, the stream is divided into 3 separate streams, 1) hvgo/Long Residue (from Tank) Heat Exchanger (E-2 2) hvgo/Total Feed Heat Exchanger (E-3 and 3) hvgo/Make up BFW Heat Exchanger (E-4).
Then, hvgo is routed to pre-heater to be used as heating media to increase VDU feed temperature before being charged to Charge Heater. .
Bakeries, dough room trough, 8 ft long 10 1 5 2, proof Boxes, 500 cu ft capacity, ovens 0 0, white bread, 120 sq ft surface, rye bread, 10 sq ft surface, breweries.
Hvgo (Heavy Vacuum Gas Oil) from Vacuum Distillation Column is taken from the draw off/collector tray, pumped to hvgo/BFW Heat Exchanger (E-1). .