Perform an energy balance of a methanol production plant from wood waste, taking into account the main equipment that was used for mass balance that is presented in the attached tables. Keep in mind that the quality of H2 is 0.975% molar and MeOH has 0.95% weight. The order of the equipment begins with the dryer and ends at the distiller. Make a simple but well-explained and detailed energy balance. All calculations must be performed in kW. Note: The attached figure is a similar diagram of the process, with the difference that it is in a different order and neither the cyclone nor the filter is found, but it is only for a guide.
Dryer (kg/year) Gasifier (kg/year) Dry waste 43847535.7 INPUTS Waste 65771961.3 Water/Air Vapor 52617569 Dry waste 43847535.7 Syngas 91203347.7 OUTPUTS Water 21924425.6 Waste 5261756.9
Cyclone (kg/year) Input 91203347.7
Filter (kg/year)
Reactor 1 (kg/year)
Condenser 1 (kg/year)
Input
90968531.7
Syngas
90733715.6Reactor Product90733715.6
To the filter Waste
90968531.7 To the reactor 90733715.6 Synthesis Product90733715.6 234816.06 Waste 234816.06
Compound 86301128.4 Water 4432587.15
Condenser 2 (kg/year)
Condenser 3 (kg/year)
Condenser 4 (kg/year)
Reactor 2 (kg/year)
Absorption (kg/year) Condenser 5 (kg/year) Distiller (kg/year) Input 81868541.3 Input 77435954.1 |Synthesis Products| 73003367 Dissolved gases 66498767 MeOH product 73003367 MeOH solution 6504600 Compound 77435954.2Synthesis Products 73003367 Hydrogen 5444701 MeOH solution 6504600 Water 564344 MeOH product 73003367 Water 4432587.15 Water 4432587.15 Waste 61054066 Dissolved gases 66498767 MeOH 95% 5940255
INPUTS
Input 86301128.4 Compound81868541.3 OUTPUT Water 4432587.15