/*! 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 18 A nitrogen rotameter is calibrat... [FREE SOLUTION] | 91Ó°ÊÓ

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A nitrogen rotameter is calibrated by feeding \(\mathrm{N}_{2}\) from a compressor through a pressure regulator, a needle valve, the rotameter, and a dry test meter, a device that measures the total volume of gas that passes through it. A water manometer is used to measure the gas pressure at the rotameter outlet. A flow rate is set using the needle valve, the rotameter reading, \(\phi\), is noted, and the change in the dry gas meter reading \((\Delta V)\) for a measured running time \((\Delta t)\) is recorded. The following calibration data are taken on a day when the temperature is \(23^{\circ} \mathrm{C}\) and barometric pressure is \(763 \mathrm{mm} \mathrm{Hg} .\) $$\begin{array}{rrr} \hline \phi & \Delta t(\min ) & \Delta V(\mathrm{L}) \\ \hline 5.0 & 10.0 & 1.50 \\ 9.0 & 10.0 & 2.90 \\ 12.0 & 5.0 & 2.00 \\ \hline \end{array}$$ (a) Prepare a calibration chart of \(\phi\) versus \(\dot{V}_{\text {sid }}\), the flow rate in standard \(\mathrm{cm}^{3} / \mathrm{min}\) equivalent to the actual flow rate at the measurement conditions. (b) Suppose the rotameter-valve combination is to be used to set the flow rate to 0.010 mol \(\mathrm{N}_{2} / \mathrm{min}\). What rotameter reading must be maintained by adjusting the valve?

Short Answer

Expert verified
For a flow rate of \(0.010 \ \mathrm{mol} \ \mathrm{N}_2 / \mathrm{min}\), the rotameter reading needs to be determined from the calibration chart after converting the flow rate to \(\mathrm{cm^3/min}\) under standard conditions. A direct answer cannot be provided without the actual calibration chart.

Step by step solution

01

Calculate the flow rates

First, convert the volume \(\Delta V\) and time \(\Delta t\) into a flow rate \(\dot{V}\) given in \(\mathrm{L/min}\) for each row of data. The flow rate can be calculated using the formula: \(\dot{V} = \Delta V / \Delta t\). Here, \(\Delta V\) is the change in volume (\(\mathrm{L}\)) and \(\Delta t\) is the running time (\(\mathrm{min}\)). Thus, the flow rates would be \[\begin{align*} &\text{for } \phi = 5.0, \dot{V} = 1.50 \ \mathrm{L} / 10.0 \ \mathrm{min} = 0.15 \ \mathrm{L/min}, \&\text{for } \phi = 9.0, \dot{V} = 2.90 \ \mathrm{L} / 10.0 \ \mathrm{min} = 0.29 \ \mathrm{L/min}, \ &\text{and for } \phi = 12.0, \dot{V} = 2.00 \ \mathrm{L} / 5.0 \ \mathrm{min} = 0.40 \ \mathrm{L/min}.\end{align*}\]
02

Convert the flow rates to standard units

To convert the flow rate from \(\mathrm{L/min}\) to standard \(cm^3/min\), you can use the conversion factor \(1 \ \mathrm{L} = 1000 \ \mathrm{cm^3}\). So, the standard flow rates \(\dot{V}_{sid}\) are \[\begin{align*} &\text{for } \phi = 5.0, \dot{V}_{sid} = 0.15 \ \mathrm{L/min} * 1000 = 150 \ \mathrm{cm^3/min}, \&\text{for } \phi = 9.0, \dot{V}_{sid} = 0.29 \ \mathrm{L/min} * 1000 = 290 \ \mathrm{cm^3/min}, \&\text{and for } \phi = 12.0, \dot{V}_{sid} = 0.40 \ \mathrm{L/min} * 1000 = 400 \ \mathrm{cm^3/min}.\end{align*}\]
03

Draw the calibration chart

Plot the values of rotameter readings \(\phi\) against the standard flow rates \(\dot{V}_{sid}\) you just calculated. This chart can then be used to determine the rotameter reading for any given flow rate.
04

Determine the rotameter reading for a specific flow rate

To determine the rotameter reading for a flow rate of 0.010 mol \(\mathrm{N}_2 / \mathrm{min}\), convert this flow rate into \(\mathrm{cm^3/min}\). Assume ideal gas behavior (which implies \(PV = nRT\)), where \(P = 1 \ \mathrm{atm}\), \(R = 0.08206 \ \mathrm{L \cdot atm / K \cdot mol}\), and \(T = 273 + 23 = 296 \ \mathrm{K}\), such that \[\begin{align*} \dot{V}_{mol} &= nRT / P \&= (0.010 \ \mathrm{mol/min})(0.08206 \ \mathrm{L \cdot atm / K \cdot mol})(296 \ \mathrm{K}) / 1 \ \mathrm{atm} \&= 24.29 \ \mathrm{L/min} = 24290 \ \mathrm{cm^3/min}.\end{align*}\]From the calibration chart, locate the value on the y-axis equal to 24290 \(\mathrm{cm^3/min}\). The corresponding value of \(\phi\) on the x-axis will be the required rotameter reading.

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Key Concepts

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

Understanding Chemical Engineering Principles in Rotameter Calibration
Rotameter calibration is an essential task in chemical engineering that ensures accurate measurement of gas flow rates. This process involves adjusting and correlating the output of the rotameter to known flow rates under specific conditions. Chemical engineering principles come into play, encompassing fluid dynamics and the properties of the gas being measured.

In a rotameter, the float inside the tapered tube rises or falls based on the flow rate of the gas, balancing the gravitational force and the drag force of the flowing fluid. The position of the float correlates to a scale on the rotameter that indicates the flow rate. For a rotameter to provide accurate readings across different operating conditions, it must be calibrated against known standards.

During calibration, variations in temperature and pressure are critical factors that need to be accounted for. As these conditions change, so do the density and viscosity of the gas, which can affect the flow rate and the position of the float within the rotameter. Adhering to chemical engineering principles ensures that rotameters are calibrated to accommodate these variables, thereby providing consistent and dependable measurements in various applications.
Gas Flow Rate Measurement Techniques
Measuring gas flow rate is a fundamental operation in many chemical engineering processes. Accurate flow measurement is crucial for process control, safety, and efficiency. There are several techniques to measure gas flow rates, with rotameters being one of the simplest and widely used devices.

A rotameter operates based on the variable area flow measurement principle. It consists of a vertically oriented, tapered tube and a float within it. The float moves up or down in the tube in response to changes in flow rate; the larger the flow, the higher the float rises. The reading from a rotameter is often given in volume per unit time, such as liters per minute, and requires calibration to ensure precision.

Another flow measurement instrument is the dry test meter that measures total volume passing through it, acting as a standard to calibrate other devices, like rotameters. This method provides a direct measurement of volume over time, which can then be converted into a flow rate using time recordings.
Application of the Ideal Gas Law in Flow Measurements
The ideal gas law is a fundamental equation in chemistry and chemical engineering that relates the pressure (P), volume (V), temperature (T), and number of moles (n) of an ideal gas through the equation: \( PV = nRT \).

When applied to flow measurements in gas systems, the ideal gas law allows for the standardization of flow rates to a common set of reference conditions, often at standard temperature and pressure (STP). This standardization is essential for comparing flow rates that were measured under varying conditions and is an important part of rotameter calibration.

For instance, to relate the flow rate of nitrogen in moles per minute to volume per minute at STP conditions, one can apply the ideal gas law to convert molar flow rate to volumetric flow rate. By doing this, we ensure that the flow rate is corrected for any deviations from the reference conditions, allowing for a more accurate and interchangeable measurement across different systems and environments. The correct interpretation and application of the ideal gas law are essential when translating between different units of flow, such as from cubic centimeters per minute to moles per minute, as highlighted in the exercise provided.

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Most popular questions from this chapter

An adult takes about 12 breaths per minute, inhaling roughly \(500 \mathrm{mL}\) of air with each breath. The molar compositions of the inspired and expired gases are as follows: $$\begin{array}{lcc} \hline \text { Species } & \text { Inspired Gas (\%) } & \text { Expired Gas (\%) } \\ \hline \mathrm{O}_{2} & 20.6 & 15.1 \\ \mathrm{CO}_{2} & 0.0 & 3.7 \\ \mathrm{N}_{2} & 77.4 & 75.0 \\ \mathrm{H}_{2} \mathrm{O} & 2.0 & 6.2 \\ \hline \end{array}$$ The inspired gas is at \(24^{\circ} \mathrm{C}\) and 1 atm, and the expired gas is at body temperature and pressure \(\left(37^{\circ} \mathrm{C}\right.\) and 1 atm). Nitrogen is not transported into or out of the blood in the lungs, so that \(\left(\mathrm{N}_{2}\right)_{\text {in }}=\left(\mathrm{N}_{2}\right)_{\text {out }}\) (a) Calculate the masses of \(\mathrm{O}_{2}, \mathrm{CO}_{2},\) and \(\mathrm{H}_{2} \mathrm{O}\) transferred from the pulmonary gases to the blood or vice versa (specify which) per minute. (b) Calculate the volume of air exhaled per milliliter inhaled. (c) At what rate (g/min) is this individual losing weight by merely breathing? (d) The rate at which oxygen is transferred from the air in the lungs to the blood is roughly proportional to \(\left[\left(p_{\mathrm{O}_{2}}\right)_{\mathrm{air}}-\left(p_{\mathrm{O}_{2}}\right)_{\mathrm{blood}}\right],\) where \(\left(p_{\mathrm{O}_{2}}\right)_{\mathrm{blood}}\) is a quantity related to the concentration of oxygen in the blood. Compared to regions where atmospheric pressure is 14.7 psia, what effect does the atmospheric pressure in Denver, which is approximately 12.1 psi, have on the transport rate and breathing rate? How does the body adjust to address this condition?

The flow of airto a gas-fired boiler fumace is controlled by a computer. The fuel gases used in the fumace are mixtures of methane (A), ethane (B), propane (C), \(n\) -butane (D), and isobutane (E). At periodic intervals the temperature, pressure, and volumetric flow rate of the fuel gas are measured, and voltage signals proportional to the values of these variables are transmitted to the computer. Whenever a new feed gas is used, a sample of the gas is analyzed and the mole fractions of each of the five components are determined and read into the computer. The desired percent excess air is then specified, and the computer calculates the required volumetric flow rate of air and transmits the appropriate signal to affow-control valve in the air line. The linear proportionalities between the input and the output signals and the corresponding process variables may be determined from the following calibration data: (a) Create a spreadsheet or write a program to read in values of \(R_{\mathrm{f}}, R_{T}, R_{P},\) the fuel gas component mole fractions \(x_{\mathrm{A}}, x_{\mathrm{B}}, x_{\mathrm{C}}, x_{\mathrm{D}},\) and \(x_{\mathrm{E}},\) and the percent excess air \(P X,\) and to calculate the required value of \(R_{\Lambda}\) (b) Run your program for the following data. $$\begin{array}{lcccccccc} \hline R_{\mathrm{f}} & R_{\mathrm{T}} & R_{P} & x_{\mathrm{A}} & x_{\mathrm{B}} & x_{\mathrm{C}} & x_{\mathrm{D}} & x_{\mathrm{E}} & P X \\ \hline 7.25 & 23.1 & 7.5 & 0.81 & 0.08 & 0.05 & 0.04 & 0.02 & 15 \% \\ 5.80 & 7.5 & 19.3 & 0.58 & 0.31 & 0.06 & 0.05 & 0.00 & 23 \% \\ 2.45 & 46.5 & 15.8 & 0.00 & 0.00 & 0.65 & 0.25 & 0.10 & 33 \% \\ \hline \end{array}$$

A small power plant produces \(500 \mathrm{MW}\) of electricity through combustion of coal that has the following composition on a dry basis: 76.2 wt\% carbon, \(5.6 \%\) hydrogen, \(3.5 \%\) sulfur, \(7.5 \%\) oxygen, and the remainder ash. The coal contains 4.0 wt\% water. The feed rate of coal is 183 tons/h, and it is burned with \(15 \%\) excess air at 1 atm, \(80^{\circ} \mathrm{F}\), and \(30.0 \%\) relative humidity. (a) Estimate the volumetric flow rate (ft \(^{3} / \mathrm{min}\) ) of air drawn into the furnace. (b) Effluent gases are discharged from the furnace at \(625^{\circ} \mathrm{F}\) and 1 atm. Estimate the molar (lb-mole/ min) and volumetric (ft \(^{3} / \mathrm{min}\) ) flow rates of gas leaving the furnace. (c) Injection of dry limestone ( \(\mathrm{CaCO}_{3}\) ) into the furnace is being considered as a means of reducing the \(\mathrm{SO}_{2}\) emitted from the plant. The technology calls for \(\mathrm{SO}_{2}\) to react with limestone: $$\mathrm{CaCO}_{3}+\mathrm{SO}_{2}+\frac{1}{2} \mathrm{O}_{2} \rightarrow \mathrm{CaSO}_{4}+\mathrm{CO}_{2}$$ Unfortunately, the process is expected to remove only \(75 \%\) of the \(\mathrm{SO}_{2}\) in the effluent gases, even though the limestone is fed at a rate 2.5 times the stoichiometric amount. What is the required feed rate of limestone? since some of the \(S O_{2}\) is removed from the furnace efflucnt [in contrast to Part (b)], recalculate the molar flow rate and composition of the effluent from the fumace. (d) The gas leaving the furnace passes through an electrostatic precipitator, where particulates from ash and limestone are removed, and then enters a stack (chimney) for release to the atmosphere. What is the gas velocity at a point in the stack where the stack diameter is \(25 \mathrm{ft}\) and the temperature is \(300^{\circ} \mathrm{F}\) ? Does the gas discharged from the stack meet the new Environmental Protection Agency standard that emissions from such power plants contain less than 75 parts of \(\mathrm{SO}_{2}\) per billion?

A stream of oxygen enters a compressor at \(298 \mathrm{K}\) and 1.00 atm at a rate of \(127 \mathrm{m}^{3} / \mathrm{h}\) and is compressed to \(358 \mathrm{K}\) and 1000 atm. Estimate the volumetric flow rate of compressed \(\mathrm{O}_{2},\) using the compressibility-factor equation of state.

Liquid hydrazine ( \(\mathrm{SG}=0.82\) ) undergoes a family of decomposition reactions that can be represented by the stoichiometric expression $$3 \mathrm{N}_{2} \mathrm{H}_{4} \rightarrow 6 x \mathrm{H}_{2}+(1+2 x) \mathrm{N}_{2}+(4-4 x) \mathrm{NH}_{3}$$ (a) For what range of values of \(x\) is this equation physically meaningful? (b) Plot the volume of product gas \([V(\mathrm{L})]\) at \(600^{\circ} \mathrm{C}\) and 10.0 bar absolute that would be formed from 50.0 liters of liquid hydrazine as a function of \(x,\) covering the range of \(x\) values determined in Part (b). (c) Speculate on what makes hydrazine a good propellant.

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