Solvent Distillation Unit

Distillation Heater 1
Open Steam In Heater 1 Flasher
Pipeline Size NB
Steam Temperature at
Valve Outlet
deg. C
Steam Flow through
valve
Kg/Hr
InDirect Steam Consumption in Heater 1
Oil % in Miscella after
Economiser
%
Mass of Oil Kg/Hr
Temp of Miscella at inlet deg. C
Temp of Miscella outlet deg. C
Oil % in Miscella after
Flasher 1
%
Vacuum in Heater 1 mm of
Hg
Steam Pressure bar g
Working Hours Hr/Day
Steam Consumption Kg/Hr
Total Steam
Consumption
Kg/Day
Distillation Heater 2
Open Steam In Heater 2 Flasher
Pipeline Size NB
Steam Temperature at
Valve Outlet
deg. C
Steam Flow through
valve
Kg/Hr
InDirect Steam Consumption in Heater 2
Oil % in Miscella after
Flasher 1
%
Temp of Miscella at inlet deg. C
Temp of Miscella outlet deg. C
Oil % in Miscella after
Flasher 2
%
Vacuum in Heater 2 mm of
Hg
Steam Pressure bar g
Steam Consumption Kg/Hr
Total Steam
Consumption
Kg/Day
Distillation Heater 3
Indirect Steam Consumption in Heater 3
Oil % in Miscella after
Flasher 2
%
Temp of Miscella at inlet deg. C
Temp of Miscella outlet deg. C
Steam Pressure bar g
Steam Consumption Kg/Hr
Total Steam
Consumption
Kg/Day
Distillation Stripper
Open Steam consumption in Stripper
Pipeline Size NB
Steam Temperature at
Valve Outlet
deg. C
Steam Flow
through valve
Kg/Hr
Indirect Steam Consumption in Stripper
Oil % in Miscella after
Heater 3
%
Temp of Miscella at inlet deg. C
Temp of Miscella outlet deg. C
Oil % in Miscella after
Stripper
%
Vacuum in Stripper mm of
Hg
Steam Pressure bar g
Steam Consumption Kg/Hr
Total Steam
Consumption
Kg/Day
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 of Miscella deg.C
Proposed Steam Savings
with FM steam system
kg/Day