Question

In: Other

A stream of methane at 86.06 kg/hr is burned in a boiler to heat water. The...

A stream of methane at 86.06 kg/hr is burned in a boiler to heat water. The boiler is fed 47.7 % excess air. Solve for air flow rate in kg/hr.

Note: Air can be treated to be 78 % N2, 21 % O2 and 1% Ar, where all percentages are in mole percents. The average molecular weight for air of this composition is 28.970 kg/kgmol

Solutions

Expert Solution

For this question, you first need to understand how much O2 is required to react with the said amount of methane, as per the reaction.

The reaction is :

CH4 + 2O2 -> CO2 + 2H2O

The reaction shows that you need 2 moles of Oxygen per mole of CH4.

You have been given 86.06 kg/h of CH4. This is equal to 5.37875 kmole of CH4 / h (86.06 divided by molecular weight of CH4, i.e. 16)

As per the reaction you need 2 * 5.37875 kmole of O2 / h. This comes out to be 10.7575 kmole of O2/h).

Air contains about 21 % O2 by moles (or volume). In other words, 0.21 kmole of O2 are found in 1 kmole of air. Therefore 10.7575 kmole of O2/h would be found in kmoles of air/h. This comes out to be about 51.2262 kmoles of air/h.

Now you have been given that you are providing 47.7 % excess AIR.

This means that the actual amount of air you're providing is 1.477 times that required. Therefore, you are providing 1.477 * 51.2262 kmoles of air/h. This comes out to be 75.6611 kmoles of air/h.

You are required to report your answer in kg/h. The molecular weight of air is 28.970 kg/kmole. Therefore, the air flow rate you are providing is 28.970*75.6611 kg/h. This comes out to be 2191.9016 kg/h of air.

I can feel that you have a problem with reactions and stoichiometry. Try to follow these steps always and it should help. Also, you could have done these calculations in volumetric flow rates as well ( apart from molar flow rates). This because, as per the ideal law, molar flow rate s are directly related to volumetric flow rates.

All the best!


Related Solutions

The purge stream may be used to replace a portion of the methane burned in the reformer.
The purge stream may be used to replace a portion of the methane burned in the reformer. Assuming that the purge gas is at 35°C and that it is fed directly to the reformer burners with 5% excess air at 300°C, how much heat would be released per 100 kmol of purge gas? Estimate the savings ($ per kmol of purge gas) if the purge stream is used in place of natural gas for fuel. (Take $3 per million Btu...
Methane at 25°C is burned in a boiler furnace with 10.0% excess air. The air enters...
Methane at 25°C is burned in a boiler furnace with 10.0% excess air. The air enters the burner at a temperature of 100°C. Ninety percent of the methane fed is consumed; the product gas is analyzed and found to contain 10.0 mol CO2 per 1 mol of CO. The exhaust gases exit the furnace at 400°C. Calculate the rate of heat transferred from the furnace, given that a molar flow rate of 100 mol/s CH4 is fed to the furnace.
A stream of 70kg/hr superheated steam is used to heat 15kmol/hr nitrogen gas via a heat...
A stream of 70kg/hr superheated steam is used to heat 15kmol/hr nitrogen gas via a heat exchanger. The superheated steam at 3500C and 1 bar enters the heat exchanger and exits as saturated water liquid at the same pressure.The nitrogen gas is heated from 25oC to 300oC at constant pressure of 1atm.The heat exchanger is set up for countercurrent flow. i)Draw and label the flowchart of the heat exchanger process by indicating all the input and output process variables. ii)Determine...
Calculate the mass of methane that must be burned to provide enough heat to convert 266.0...
Calculate the mass of methane that must be burned to provide enough heat to convert 266.0 g of water at 39.0°C into steam at 110.0°C. (Assume that the H2O produced in the combustion reaction is steam rather than liquid water.)
Calculate the mass of methane that must be burned to provide enough heat to convert 300.0...
Calculate the mass of methane that must be burned to provide enough heat to convert 300.0 g of water at 30.0°C into steam at 106.0°C.
Calculate the mass of methane that must be burned to provide enough heat to convert 347.0...
Calculate the mass of methane that must be burned to provide enough heat to convert 347.0 g of water at 18.0°C into steam at 110.0°C. (Assume that the H2O produced in the combustion reaction is steam rather than liquid water.)
A steam power plant with boiler use coal fuel with net heat 4000 kcal/kg and boiler...
A steam power plant with boiler use coal fuel with net heat 4000 kcal/kg and boiler efficiency 90%. If steam utrbine from the power plsnt generate power output 100 MW, at condition vapor enter at 10 MPa, 520oC and condensate to saturated liquid at 0.08 bar. If the isentropic efficiency turbine and pump is 90%, then a) Calculate coal required (ton/hour) b) Calculate netto efficiency of the power plant c) Calculate Net Plant Heat Rate (kCal/kWh)
An iron boiler of mass 180 kg contains 730 kg of water at 11 ∘C. A...
An iron boiler of mass 180 kg contains 730 kg of water at 11 ∘C. A heater supplies energy at the rate of 58,000 kJ/h. The specific heat of iron is 450 J/kg⋅C∘, the specific heat of water is 4186 J/kg⋅C∘, the heat of vaporization of water is 2260 kJ/kg⋅C∘. Assume that before the water reaches the boiling point, all the heat energy goes into raising the temperature of the iron or the steam, and none goes to the vaporization...
Assume the water for a boiler is preheated using flue gases from the boiler stack. The...
Assume the water for a boiler is preheated using flue gases from the boiler stack. The flue gases are available at a rate of 0.25 kg/s at 150°C, with a specific heat of 1000 J/kg · K. The water entering the exchanger at 15°C at the rate of 0.05 kg/s is to be heated to 90°C. The heat exchanger is to be of the type with one shell pass and four tube passes. The water flows inside the tubes, which...
In a pharmaceutical application distilled water with a flow rate of 34560 kg/hr is to cool...
In a pharmaceutical application distilled water with a flow rate of 34560 kg/hr is to cool ethyl alcohol in a parallel flow heat exchanger. The alcohol flowing at 31320 kg/hr enters the exchanger at 75oC and is cooled to 45oC. Assuming that the water flows through the tubes and enters the exchanger at 15oC, determine, for an overall heat transfer coefficient of 0.5kW/m2K the dissipation rate, together with the required heat transfer area. The specific heat capacity of both the...
ADVERTISEMENT
ADVERTISEMENT
ADVERTISEMENT