Energy balance on metallurgical furnace

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Discussion Overview

The discussion revolves around the energy balance in a metallurgical furnace used for roasting pure iron sulfide (FeS2). Participants analyze the heat calculations involved in the process, including the effects of excess air and the resulting exhaust gases. The focus is on understanding the discrepancies between the expected heat loss and the calculated values, as well as the implications of these findings on the operation of the furnace.

Discussion Character

  • Homework-related
  • Technical explanation
  • Debate/contested

Main Points Raised

  • One participant notes an inconsistency between the problem statement and the calculated heat loss, suggesting that the problem may be poorly designed due to the high excess air ratio.
  • Another participant calculates a different value for the molar flow of exhaust gases, which they believe could account for discrepancies in the heat calculations.
  • Some participants argue that the term "heat lost" in the problem statement is misleading, as the furnace is expected to add heat rather than lose it.
  • There is a discussion about the nature of roasting furnaces and whether the sulfide is actually burning, raising questions about the heat input required for the process.
  • Several participants express that the problem statement lacks sufficient data to accurately account for heat lost via radiation, complicating the energy balance analysis.

Areas of Agreement / Disagreement

Participants generally disagree on the interpretation of the problem statement regarding heat loss and the implications for the furnace's operation. There is no consensus on the correct approach to the energy balance, and multiple competing views remain regarding the calculations and assumptions made.

Contextual Notes

Participants highlight limitations in the problem statement, particularly regarding the lack of data needed to accurately calculate heat loss due to radiation. The discussion also reflects uncertainty about the operational characteristics of the furnace and the nature of the reactions occurring within it.

Who May Find This Useful

This discussion may be useful for students and professionals interested in thermodynamics, energy balances in chemical processes, and the operation of metallurgical furnaces.

MexChemE
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Homework Statement


Pure iron sulfide (FeS2) is fed into an Herreshoff furnace at 25 °C. An 83% of excess air is also fed into the furnace at 25 °C. The solid product consists only of Fe2O3. The solid product reaches a temperature of 1832 °C, and the exhaust gases (8.7% SO2, 9.8% O2, 81.5% N2) reach a temperature of 1472 °C. Determine the amount of heat lost (Q < 0) by the furnace due to radiation, per tonne of pyrite loaded.
Given solution: Q = +3,786,595 BTU per tonne of pyrite
(First off, there seems to be an inconsistency between the problem statement and the given solution; I'm not showing all of my procedure and calculations since I got very close numerically to the given solution, what I want to discuss is said inconsistency)
Process block diagram attached

Homework Equations


Q = ΔH (Energy balance on the furnace)
FeS2 + 2.75 O2 → 0.5 Fe2O3 + 2 SO2

The Attempt at a Solution


First off, I started by stablishing a basis of M1 = 1 mol. I performed a mass balance on the furnace in order to determine the rest of the molar flows. These were
M2 = 23.95 mol
M3 = 0.5 mol
M4 = 23.2 mol
It was a pretty straightforward balance, since I'm told the 100% of iron sulfide reacts to yield ferric oxide. Next, I set up the energy balance on the furnace
Q = \Delta H = \Delta H_{Rx}^° + \Delta H_3 + \Delta H_4
Where
\Delta H_{Rx}^° is the standard enthalpy of the roasting reaction (maximum amount of heat generated in the furnace)
\Delta H_3 is the amount of heat needed to raise the solid product's temperature to 1832 °C
\Delta H_4 is the amount of heat needed to raise the exhaust gases' temperature to 1472 °C
I got the enthalpies of formation of reactants and products in charts provided by the professor. Molar heat capacities of the products were also found in another set of charts provided by the professor. For the heat capacity of the exhaust gases, I used the heat capacities of each gas and their molar fractions to calculate the average molar heat capacity of the mix. My results were
\Delta H_{Rx}^° = -197650 \ cal
\Delta H_3 = (0.5 \ mol) \left(43.7 \ \frac{cal}{mol \ K} \right)(1832 \ °C - 25 \ °C) = 39482.95 \ cal
\Delta H_4 = (23.2 \ mol) \left(8.3 \ \frac{cal}{mol \ K} \right)(1472 \ °C - 25 \ °C) = 278634.32 \ cal
Next, I calculated Q, but this first result is for 120 grams (1 mol) of iron sulfide loaded. I did some calculations in order to adjust the result for a tonne of sulfide roasted.
Q = -197650 \ cal + 39482.95 \ cal + 278634.32 \ cal = \frac{120467.27 \ cal}{120 \ g}
Q = \frac{478.04 \ BTU}{120 \ g} = 3.98 \ \frac{BTU}{g}
Q = 3.98 \ \frac{BTU}{g} (1,000,000 \ g) = 3,980,000 \ BTU
Now, if the problem statement tells me heat is being lost by the furnace due to radiation, I would expect a negative result of Q, not positive. However, this is the correct result for the problem, even though it doesn't agree with the physical situation. What I'm guessing is that the problem (and the process modeled within) was badly designed by the professor. 83% excess of air seems a lot to me; the exhaust gases alone need a greater amount of the maximum generable heat by the process in order to reach 1472 °C. My understanding is that a real furnace operating under these conditions would need a heat input of 3.9 mega BTU in order to carry out the process, but real furnaces are supposed to release a large amount of heat, not consume it. What I'd do to fix this inconsistency is to lower the amount of air fed into the furnace, so the exhaust gases don't consume more heat than the amount generated by the process. I guess it's an obvious choice. I hope my analysis of the situation is correct.

Thanks in advance for any input!
 

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The value I get for M4 is 20.9 moles. That might account for the difference in the magnitude of Q.

They can't mean heat lost in the problem statement, because the furnace certainly adds heat. Otherwise, why is it called a furnace.

Chet
 
Chestermiller said:
The value I get for M4 is 20.9 moles.
Required amount of oxygen is 2.75 mol, times 1.83 yields 5.03 mol, which is the amount of O2 fed. 5.03 mol times the ratio of nitrogen to oxygen (0.79/0.21) yields 18.92 mol of N2. The amount of O2 exiting the furnace is 5.03 mol - 2.75 mol = 2.28 mol, plus 18.92 mol of N2 and 2 mol of SO2 generated add up to 23.2 mol.
Chestermiller said:
They can't mean heat lost in the problem statement, because the furnace certainly adds heat. Otherwise, why is it called a furnace.
Maybe I'm confusing the way this kind of furnaces are analyzed (from an energy balance point of view) versus industrial process furnaces (heaters), where your desired product is a large (and negative) magnitude of Q. In a roasting furnace your desired product is to make the sulfide react, by raising its temperature. But a metallurgical furnace still loses heat by radiation, doesn't it? And if this specific furnace needs 3.9 mega BTU, how do you supply the heat? What is actually happening in a roasting furnace? Is the sulfide actually burning? If it does, how does it ignite?
 
MexChemE said:
Required amount of oxygen is 2.75 mol, times 1.83 yields 5.03 mol, which is the amount of O2 fed. 5.03 mol times the ratio of nitrogen to oxygen (0.79/0.21) yields 18.92 mol of N2. The amount of O2 exiting the furnace is 5.03 mol - 2.75 mol = 2.28 mol, plus 18.92 mol of N2 and 2 mol of SO2 generated add up to 23.2 mol.
Oops. I forgot to include the oxygen in the exit stream. Sorry.
Maybe I'm confusing the way this kind of furnaces are analyzed (from an energy balance point of view) versus industrial process furnaces (heaters), where your desired product is a large (and negative) magnitude of Q. In a roasting furnace your desired product is to make the sulfide react, by raising its temperature. But a metallurgical furnace still loses heat by radiation, doesn't it? And if this specific furnace needs 3.9 mega BTU, how do you supply the heat? What is actually happening in a roasting furnace? Is the sulfide actually burning? If it does, how does it ignite?
It seems to me you analyzed this problem correctly. I don't know what else to say.

Chet
 
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I will also add, that even if the furnace is losing heat via radiation, it is not possible to account for it just with the information provided in the problem statement. The amount of heat lost by radiation is included in the value of Q, I guess, but impossible to calculate without the proper data. The bigger the heat loss due to radiation is, the bigger the amount of heat we need to provide the furnace with. So I guess the issue lies within the problem statement's wording.
 
MexChemE said:
I will also add, that even if the furnace is losing heat via radiation, it is not possible to account for it just with the information provided in the problem statement. The amount of heat lost by radiation is included in the value of Q, I guess, but impossible to calculate without the proper data. The bigger the heat loss due to radiation is, the bigger the amount of heat we need to provide the furnace with. So I guess the issue lies within the problem statement's wording.
I agree.

Chet
 
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