De-Solventizing Toaster

De-Solventizing Toaster
Mass Balance at Extractor Seed Inlet
Inlet Seed Mass Kg/Hr
Percentage of Oil in Seed %
Mass of Oil Kg/Hr
% of Oil in Miscella %
Parameters at DT Inlet
Hexane % %
DT Meal Kg/Hr
Total Mass at Inlet Kg/Hr
Mass of Hexane Kg/Hr
Volume of Hexane Lit/Hr
Open Steam Consumption in DT
Pipe Size NB
Open Steam Pressure bar g
Number of Pipes for
Open Steam
No
Total Steam Flow Kg/Hr
Indirect Steam Consumption in DT
Inlet Temperature of
Meal at DT
deg.C
Outlet Temperature of
Meal at DT
deg.C
Flow of Meal into DT with
Moisture
kg/hr
Flow of Dry Meal
into DT
kg/hr
Mass of Moisture
in meal
kg/hr
Moisture in Meal % %
Indirect Steam Pressure bar g
Temperature of
superheated solvent
deg.C
Mass of Indirect Steam Kg/Hr
Losses in Existing Steam System
Steam Trap Status
Number of Traps Not
Working
No
Trap By-pass valve Status
By-pass Valve size mm
Number of By-pass valve
Opened
No
Percentage of By-pass
Opening
%
Temperature overshoot deg.C
Working Hours in a day hr
Steam Flow rate with
Existing Steam System
kg/hr
Steam Consumption with
Existing Steam System
Kg/Day
Savings with proposed
FM steam system
Kg/hr