n-butane burns with 15% excess air, both streams enter at 25 °
C. The gas burns completely producing 90 mol of CO2 / 10mol of CO.
The combustion gas comes out at 400ºC and 1 atm. Taking as a basis
of calculation 1000 moles / h of the gas that feeds the oven:
1. Draw the process diagram
2. Calculate the air feed rate and the composition of the flue
gases.
3. Fill the enthalpy table in / out of the process. Clearly specify
the reference status.
4. Calculate the amount of heat given up in the reactor (kW).


n-butane burns with 15% excess air, both streams enter at 25 ° C. The gas burns...
n-butane burns with 15% excess air, both streams enter at 25°C. The gas burns completely producing 90 mol of CO2 / 10mol of CO. The combustion gas comes out at 400ºC and 1 atm. Taking as a basis of calculation 1000 moles/h of the gas that feeds the oven: Calculate the air supply speed and the composition of the combustion gases.
The heater in a house burns natural gas with x% excess air according to the reaction: CH4 2 02>CO2 2 H2O The flue gas leaves the burner at Tout. The air and the natural gas (CH4) enter the burner Prepare a spreasheet for this system using a basis of one mole of methane feed to deter at standard conditons of 25°C and 1 atm pressure. mine: a) The standard heat for the combustion for the reaction above, b) The required...
A fuel gas consists of 75% butane (C4H10), 10% propane (C3H8) and 15% butene (C4H8) by volume. It is to be fed to the combustion chamber in 10% excess air at 25ºC, where it is completely burnt to carbon dioxide and water. The flue gases produced are to be used to generate 5 bar steam from water at 90ºC. net calorific value (MJm-3) at 25oC Butane (C4H10) = 111.7MJm-3, Butene (C4H8) = 105.2 MJm-3. Propane (C3H8) = 85.8 MJm-3. air...
Q4/ Toluene gas (CH3) enters a continuous adiabatic heat exchanger at (35°C) and (300 KPa) and exits at (260°C). Superheated steam at (400°C) and (5 bar) enters to exchanger flowing counter currently to a Toluene and exits as a saturated liquid at the same pressure. 1- If (150 mol) of Toluene is fed, draw and label a process flow chart. 2- Calculate the values of inlet-outlet enthalpies. 3- Calculate the volumetric feed ratio of the two streams (m' steam fed/mºtoluene...