Sheet1NO.ITEMKWpower supplycable sizeLength1100 LITER
BATH63P,440V,50Hz41/2 core x 4 Sq. mmActual250 Liter
Bath43P,440V,50Hz41/2 core x 2.5 Sq. mmActual3Heating
Tape21P,230V,50Hz3 core x1.5Actual4Heating Tape21P,230V,50Hz3 core
x1.5 Sq. mmActual5Motor for 50 litre0.363P,440V,50Hz4 core x1.5 Sq.
mmActual6Motor for Heating system1.53P,440V,50Hz4 core x1.5 Sq.
mmActual7Heater for Heating System43P,440V,50Hz41/2 core x 2.5 Sq.
mmActual8Motor for Ejector1.53P,440V,50Hz4 core x1.5 Sq.
mmActual9Miscellaneous13P,440V,50Hz41/2 core x 2.5 Sq.
mmActualKW22.36HP29.81333333331.3333333333
Sheet2SR NOUNIT1Initial mass125KG2Benzoic Acid
%33%41.2525253Water %48%12ENERGY4Power cost/KW6RS375heater KW for
100 liter6kw5160706Latent heat of Vaporization-Benzoic
Acid99.08Kcal/kg10KG7Latent heat of
Vaporization-Water539.4Kcal/kg258Oil in Bath60Liiter1856.259Sp. Gr
of Oil0.92887.510Sp. Heat of Oil0.9Kcal/Kg-degc11Oil in
Bath54Kg12Initial Temperature25Degc13Final
Temperature250Degc7014Heat require to heat
oil10935Kcal2.11918604653314Heat require to Vaporize Benzoic
Acid4087.05Kcal15Heat require to heat
water32364Kcal7.91866994533883.6817Heat require to
vaporize36451.05Kcal4.515906976718Reflux ratio0.2519Heat for
Reflux1021.7625Kcal20Total heat37472.8125Kcal/hr33589.132521Time
for Distillation7.2621729651Hr6.509521802322Energy
Consumption43.5730377907KW39.05713081423Energy Consumption for
Heating oil261.4382267442INR234.342784883724Energy consumtion/Kg of
Benzoic Acid recovered6.3378964059INR5.6810372093ENERGY REQUIREMENT
FOR DISTILLATION6000watt5160KCAL6Powe cost/Kw1250.25LHE0.33benzoic
Acid41.2599.07962398874087.00.48Water60539.383846794332363.036450.1kcal/hrreflux
ratio0.259112.545562.68.8hr317.9RupeesPower at [email protected]/KgFor
Distillation
