I need to solve the material and energy balance
I need to solve the material and energy balance for the att.
I) Sulphur dioxide (SO2) with a volumetric flow rate 5000cm3/s at 1 bar and 1000C is mixed with a second SO2 stream flowing at 2500cm3/s at 2 bar and 200C. The process occurs at steady state. You may assume ideal gas behaviour. For SO2 take the heat capacity at constant pressure to be CP/R = 3.267+5
Calculate the pressure at the bottom of a column of Ethanol 100 ft high using a pressure (force) balance in American Engineering Units.
A stream of propane is throttled from 4.298 bar and 450 K to 0.22 bar. This process is irreversible due to frictional losses at the nozzle. a. In words or equations, why are frictional losses irreversible? Q : Thermodynamics I) Sulphur dioxide (SO2) I) Sulphur dioxide (SO2) with a volumetric flow rate 5000cm3/s at 1 bar and 1000C is mixed with a second SO2 stream flowing at 2500cm3/s at 2 bar and 200C. The process occurs at steady state. You may assume ideal gas behaviour. For SO2 take the heat capacity at constant pressure to be CP/R = 3.267+5
A stream of propane is throttled from 4.298 bar and 450 K to 0.22 bar. This process is irreversible due to frictional losses at the nozzle.
a. In words or equations, why are frictional losses irreversible?
I) Sulphur dioxide (SO2) with a volumetric flow rate 5000cm3/s at 1 bar and 1000C is mixed with a second SO2 stream flowing at 2500cm3/s at 2 bar and 200C. The process occurs at steady state. You may as
A heater (heat source temperature = 527 K) and turbine are connected in series as shown below: Q : Mass transfer adsorption how to how to calculate amount of ammonia adsorbed per kg of adsobent in ammonia calcium chloride adsorption process?
A heater (heat source temperature = 527 K) and turbine are connected in series as shown below:
how to calculate amount of ammonia adsorbed per kg of adsobent in ammonia calcium chloride adsorption process?
Please can you look into this assignment and let me know if its solve able.
Cumene is produced by the vapour phase reaction of benzene with propylene. The fresh feeds have the following compositions: Benzene: 99% w/w benzene, 1% w/w toluene Propylene: 98% v/v propylene,
Cumene is produced by the vapour phase reaction of benzene with propylene. The fresh feeds have the following compositions:
Benzene: 99% w/w benzene, 1% w/w toluene
Propylene: 98% v/v propylene,
Consider a chemical reaction: a CH3-CH=CH2 + b NH3 + c O2 → d CH2=CH-C≡N + e H2O 1. &
Consider a chemical reaction:
a CH3-CH=CH2 + b NH3 + c O2 → d CH2=CH-C≡N + e H2O
1. &
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