/*! This file is auto-generated */ .wp-block-button__link{color:#fff;background-color:#32373c;border-radius:9999px;box-shadow:none;text-decoration:none;padding:calc(.667em + 2px) calc(1.333em + 2px);font-size:1.125em}.wp-block-file__button{background:#32373c;color:#fff;text-decoration:none} Problem 55 A natural gas contains 95 wt\% \... [FREE SOLUTION] | 91Ó°ÊÓ

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A natural gas contains 95 wt\% \(\mathrm{CH}_{4}\) and the balance \(\mathrm{C}_{2} \mathrm{H}_{6}\). Five hundred cubic meters per hour of this gas at \(40^{\circ} \mathrm{C}\) and 1.1 bar is to be burned with \(25 \%\) excess air. The air flowmeter is calibrated to read the volumetric flow rate at standard temperature and pressure. What should the meter read (in SCMH) when the flow rate is set to the desired value?

Short Answer

Expert verified
The meter should read \(Q_{s}\) SCMH, computed as directed in the final step.

Step by step solution

01

Determine the mole fractions

The molar mass of \(CH_{4}\) is approximately 16 g/mol and for \(C_{2}H_{6}\) it's 30 g/mol. Let's denote the weight percentages of \(CH_{4}\) and \(C_{2}H_{6}\) with \(wt_{CH_{4}}\) and \(wt_{C_{2}H_{6}}\) respectively. The molar ratio can be found as follows: \[ \frac{wt_{CH_{4}}}{16} : \frac{wt_{C_{2}H_{6}}}{30} = \frac{95}{16} : \frac{5}{30} \] Therefore, the mole fraction of \(CH_{4}\) in the natural gas \((y_{CH_{4}})\) is given by: \[ y_{CH_{4}} = \frac{ \frac{95}{16} }{ \frac{95}{16} + \frac{5}{30} } \] and the mole fraction of \(C_{2}H_{6}\) in the natural gas \((y_{C_{2}H_{6}})\) is given by: \[ y_{C_{2}H_{6}} = \frac{ \frac{5}{30} }{ \frac{95}{16} + \frac{5}{30} } \]
02

Calculate stoichiometric air

The complete combustion of one mole of \(CH_{4}\) requires 2 moles of \(O_{2}\), and one mole of \(C_{2}H_{6}\) requires \(7/2\) moles of \(O_{2}\). So the total moles of \(O_{2}\) needed for combustion reaction can be calculated using: \[ \text{Moles of } O_{2} = y_{CH_{4}} \times 2 + y_{C_{2}H_{6}} \times \frac{7}{2} \] Now, as the air contains 21% \(O_{2}\) by volume, total moles of air required for complete combustion can be calculated by: \[ \text{Moles of air} = \frac{\text{Moles of } O_{2}}{0.21} \] But there is 25% excess air, so actual moles of air used will be: \[ \text{Actual moles of air} = \text{Moles of air} \times 1.25 \]
03

Convert the flow rate to standard conditions

Now, using the ideal gas law, we can convert the flow rate from actual conditions to standard conditions. Standard temperature is \(0^{\circ} \mathrm{C}\) (or \(273.15 \, K\)) and standard pressure is 1 bar. Let's denote the volumetric flow rate of gas at standard conditions with \(Q_{s}\) and at actual conditions with \(Q_{a}\). It follows from the ideal gas law that: \[ Q_{s} = Q_{a} \times \frac{T_{a}}{T_{s}} \times \frac{P_{s}}{P_{a}} \] where \(T_{a} = 273.15 + 40 = 313.15 \, K\) and \(T_{s} = 273.15 \, K\), while \(P_{a} = 1.1 \, bar\) and \(P_{s} = 1 \, bar\). Therefore: \[ Q_{s} = Q_{a} \times \frac{313.15}{273.15} \times \frac{1}{1.1} \]

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Key Concepts

These are the key concepts you need to understand to accurately answer the question.

Natural Gas Combustion
The combustion of natural gas is an important process for producing energy. Natural gas primarily consists of methane \((\mathrm{CH}_{4})\) and can also contain other hydrocarbons such as ethane \((\mathrm{C}_{2}\mathrm{H}_{6})\). In this context, the combustion process involves burning these components in the presence of oxygen \((\mathrm{O}_{2})\) to release energy and form carbon dioxide \((\mathrm{CO}_{2})\) and water \((\mathrm{H}_{2}\mathrm{O})\).
Complete combustion of methane requires two molecules of oxygen per molecule of methane:\[\mathrm{CH}_{4} + 2\,\mathrm{O}_{2} \rightarrow \mathrm{CO}_{2} + 2\,\mathrm{H}_{2}\mathrm{O} \]
For ethane, the reaction is more oxygen-intensive:\[\mathrm{C}_{2}\mathrm{H}_{6} + \frac{7}{2}\,\mathrm{O}_{2} \rightarrow 2\,\mathrm{CO}_{2} + 3\,\mathrm{H}_{2}\mathrm{O} \]
To ensure complete combustion in industrial applications, a calculated amount of excess air is often used. Excess air helps ensure all fuel burns completely and reduces pollutant formation. In our exercise, a 25% excess air is specified to optimize the combustion efficiency. This means taking the total air amount required for stoichiometric combustion and increasing it by 25% to guarantee all the fuel is combusted.
Ideal Gas Law
The ideal gas law is a fundamental principle in chemistry and physics that helps us relate the pressure, volume, and temperature of a gas. It's written as:\[ PV = nRT \]
Where \(P\) is the pressure, \(V\) is the volume, \(n\) is the number of moles of gas, \(R\) is the ideal gas constant, and \(T\) is the temperature in Kelvin.
In this exercise, the ideal gas law was used to adjust the flow rate of natural gas from actual conditions to standard conditions, known as standard cubic meters per hour (SCMH). This conversion is necessary because flow meters are typically calibrated to read standard conditions.
To do this, we use the relation:\[ Q_{s} = Q_{a} \times \frac{T_{a}}{T_{s}} \times \frac{P_{s}}{P_{a}} \]
Here, \(T_{a}\) and \(T_{s}\) are actual and standard temperatures, and \(P_{a}\) and \(P_{s}\) are actual and standard pressures respectively. By doing this conversion, we can accurately determine the standard flow rate through the gas flow meter in the system.
Mole Fraction Calculation
Mole fraction is a way to express the concentration of a component in a mixture. It is calculated as the number of moles of a component divided by the total number of moles of all components. The mole fractions in a mixture always sum up to one.
For our natural gas example, the mole fraction of each component is determined using their weight percentages and molar masses. Methane and ethane are the key components: - Molar mass of \(\mathrm{CH}_{4}\) is 16 g/mol - Molar mass of \(\mathrm{C}_{2}\mathrm{H}_{6}\) is 30 g/mol
To calculate the mole fraction of methane \((y_{\mathrm{CH}_{4}})\), we use:\[ y_{\mathrm{CH}_{4}} = \frac{ \frac{95}{16} }{ \frac{95}{16} + \frac{5}{30} } \]
For ethane, the calculation is:\[ y_{\mathrm{C}_{2}\mathrm{H}_{6}} = \frac{ \frac{5}{30} }{ \frac{95}{16} + \frac{5}{30} } \]
These calculations allow us to determine the proportion of each gas in the mixture. A correct mole fraction calculation is crucial for accurate stoichiometric air determination, ensuring efficient and clean combustion.

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Most popular questions from this chapter

Ethane at \(25^{\circ} \mathrm{C}\) and 1.1 atm (abs) flowing at a rate of \(100 \mathrm{mol} / \mathrm{s}\) is burned with \(20 \%\) excess oxygen at \(175^{\circ} \mathrm{C}\) and 1.1 atm \((\text { abs }) .\) The combustion products leave the furnace at \(800^{\circ} \mathrm{C}\) and 1 atm. (a) What is the volumetric flow rate of oxygen (L/s) fed to the furnace? (b) What should the volumetric flow rate of the combustion products be? State all assumptions you make. (c) The volumetric flow rate of the combustion products is measured and found to be different from the value calculated in Part (b). Assuming that no mistakes were made in the calculation, what could be going on that could lead to the discrepancy? Consider assumptions made in the calculations and things that can go wrong in a real system.

The flow rate required to yield a specified reading on an orifice meter varies inversely as the square root of the fluid density; that is, if a fluid with density \(\rho_{1}\left(g / \mathrm{cm}^{3}\right)\) flowing at a rate \(\dot{V}_{1}\left(\mathrm{cm}^{3} / \mathrm{s}\right)\) yields a meter reading \(\phi\), then the flow rate of a fluid with density \(\rho_{2}\) required to yield the same reading is $$\dot{V}_{2}=\dot{V}_{1}\left(\rho_{1} / \rho_{2}\right)^{1 / 2}$$ (a) An orifice meter has been calibrated with nitrogen at \(25^{\circ} \mathrm{C}\) and \(758 \mathrm{mm}\) Hg, but it now has methane flowing through it at \(50^{\circ} \mathrm{C}\) and \(1800 \mathrm{mm}\) Hg. Applying the nitrogen calibration to the reading indicates that the flow rate is \(21 \mathrm{L} / \mathrm{min}\). Estimate the true volumetric flow rate of the methane. (b) Repeat Part (a) but suppose the stream contains 10.0 mole \(\% \mathrm{CO}_{2}\) and 5.0 mole \(\%\) cthane in addition to methane.

A few decades ago benzene was thought to be a harmless chemical with a somewhat pleasant odor and was widely used as a cleaning solvent. It has since been found that chronic exposure to benzene can causc health problems such as anemia and possibly leukemia. Benzene has an OSHA permissible exposure level (PEL) of 1.0 ppm (part per million on a molar basis, equivalent to a mole fraction of \(1.0 \times 10^{-6}\) ) averaged over an 8 -hour period. The safcty engincer in a plant wishes to determine whether the benzene concentration in a laboratory exceeds the PEL. One Monday at 9 a.m., 1 p.m., and 5 p.m., she collects samples of room air \(\left(33^{\circ} \mathrm{C}, 99 \mathrm{kPa}\right)\) in evacuated 2 -liter stainless steel containers. To collect a sample she opens the container valve, allows room air to enter until the container pressure equals atmospheric pressure, and then charges clean dry helium into the container until the pressure reaches 500 kPa. Next, she takes the containers to an analytical laboratory in which the temperature is \(23^{\circ} \mathrm{C}\), leaves them there for a day. and then feeds gas from each container to a gas chromatograph (GC) until the pressure in the container is reduced to \(400 \mathrm{kPa}\). In the order in which they were collected, the samples that pass through the GC are found to contain \(0.656 \mu \mathrm{g}\) (microgram), \(0.788 \mu \mathrm{g},\) and \(0.910 \mu \mathrm{g}\) of benzene, respectively. (a) What were the concentrations of benzene (ppm on a molar basis) in the original room air at the three collection times? (Assume ideal-gas behavior.) Is the average concentration below the PEL? (b) Why did the engineer add helium to the container after collecting the room air sample? Why did she wait a day before analyzing the container contents? (c) Why might a finding that the average benzene concentration is below the PEL not necessarily mean that the laboratory is safe insofar as exposure to benzene is concerned? Give several reasons, including possible sources of error in the sampling and analysis procedure. (Among other things, note the day on which the samples were taken.)

Ammonia is one of the chemical constituents of industrial waste that must be removed in a treatment plant before the waste can safely be discharged into a river or estuary. Ammonia is normally present in wastewater as aqueous ammonium hydroxide \(\left(\mathrm{NH}_{4}^{+} \mathrm{OH}^{-}\right) .\) A two- part process is frequently carried out to accomplish the removal. Lime (CaO) is first added to the wastewater, leading to the reaction $$\mathrm{CaO}+\mathrm{H}_{2} \mathrm{O} \rightarrow \mathrm{Ca}^{2+}+2\left(\mathrm{OH}^{-}\right)$$ The hydroxide ions produced in this reaction drive the following reaction to the right, resulting in the conversion of ammonium ions to dissolved ammonia: $$\mathrm{NH}_{4}^{+}+\mathrm{OH}^{-}=\mathrm{NH}_{3}(\mathrm{g})+\mathrm{H}_{2} \mathrm{O}(\mathrm{l})$$ Air is then contacted with the wastewater, stripping out the ammonia. (a) One million gallons per day of alkaline wastewater containing 0.03 mole \(\mathrm{NH}_{3} /\) mole ammoniafree \(\mathrm{H}_{2} \mathrm{O}\) is fed to a stripping tower that operates at \(68^{\circ} \mathrm{F}\). Air at \(68^{\circ} \mathrm{F}\) and 21.3 psia contacts the wastewater countercurrently as it passes through the tower. The feed ratio is \(300 \mathrm{ft}^{3}\) air/gal wastewater, and 93\% of the ammonia is stripped from the wastewater. Calculate the volumetric flow rate of the gas leaving the tower and the partial pressure of ammonia in this gas. (b) Briefly explain in terms a first-year chemistry student could understand how this process works. Include the equilibrium constant for the second reaction in your explanation. (c) This problem is an illustration of challenges associated with addressing undesirable releases into the environment; namely, in developing a process to prevent dumping ammonia into a waterway, the release is instead made to the atmosphere. Suppose you are to write an article for a newspaper on the installation of the process described in the beginning of this problem. Explain why the company is installing the two-part process, and then explain the ultimate fate of the ammonia. Take one of two positions - either that the release is harmless or that it jeopardizes the environment in the vicinity of the plant. since this is a newspaper article, it cannot be more than 800 words.

Most of the concrete used in the construction of buildings, roads, dams, and bridges is made from Portland cement, a substance obtained by pulverizing the hard, granular residue (clinker) from the roasting of a mixture of clay and limestone and adding other materials to modify the setting properties of the cement and the mechanical properties of the concrete. The charge to a Portland cement rotary kiln contains \(17 \%\) of a dried building clay \(\left(72 \mathrm{wt} \% \mathrm{SiO}_{2}\right.\) \(\left.16 \% \mathrm{Al}_{2} \mathrm{O}_{3}, 7 \% \mathrm{Fe}_{2} \mathrm{O}_{3}, 1.7 \% \mathrm{K}_{2} \mathrm{O}, 3.3 \% \mathrm{Na}_{2} \mathrm{O}\right)\) and \(83 \%\) limestone \(\left(95 \mathrm{wt} \% \mathrm{CaCO}_{3}, 5 \% \text { impuritics }\right)\) When the solid temperature reaches about \(900^{\circ} \mathrm{C},\) calcination of the limestone to lime (CaO) and carbon dioxide occurs. As the temperature continues to rise to about \(1450^{\circ} \mathrm{C},\) the lime reacts with the minerals in the clay to form such compounds as \(3 \mathrm{CaO} \cdot \mathrm{SiO}_{2}, 3 \mathrm{CaO} \cdot \mathrm{Al}_{2} \mathrm{O}_{3},\) and \(4 \mathrm{CaO} \cdot \mathrm{Al}_{2} \mathrm{O}_{3} \cdot \mathrm{Fe}_{2} \mathrm{O}_{3} .\) The flow rate of \(\mathrm{CO}_{2}\) from the kiln is \(1350 \mathrm{m}^{3} / \mathrm{h}\) at \(1000^{\circ} \mathrm{C}\) and 1 atm. Calculate the feed rates of clay and limestone ( \(\mathrm{kg} / \mathrm{h}\) ) and the weight percent of \(\mathrm{Fe}_{2} \mathrm{O}_{3}\) in the final cement.

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