/*! 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

Phosgene (CCl, O) is a colorless gas that was used as an agent of chemical warfare in World War I. It has the odor of new-mown hay (which is a good warning if you know the smell of new-mown hay). Pete Brouillette, an innovative chemical engincering student, came up with what he believed was an effective new process that utilized phosgene as a starting material. He immediately set up a reactor and a system for analyzing the reaction mixture with a gas chromatograph. To calibrate the chromatograph (i.e., to determine its response to a known quantity of phosgene), he evacuated a 15.0 cm length of tubing with an outside diameter of \(0.635 \mathrm{cm}\) and a wall thickness of \(0.559 \mathrm{mm}\), and then connected the tube to the outlet valve of a cylinder containing pure phosgene. The idea was to crack the valve, fill the tube with phosgene, close the valve, feed the tube contents into the chromatograph, and observe the instrument response. What Pete hadn't thought about (among other things) was that the phosgene was stored in the cylinder at a pressure high enough for it to be a liquid. When he opened the cylinder valve, the liquid rapidly flowed into the tube and filled it. Now he was stuck with a tube full of liquid phosgene at a pressure the tube was not designed to support. Within a minute he was reminded of a tractor ride his father had once given him through a hayfield, and he knew that the phosgene was leaking. He quickly ran out of the lab, called campus security, and told them that a toxic leak had occurred, that the building had to be evacuated, and the tube removed and disposed of properly. Personnel in air masks shortly appeared, took care of the problem, and then began an investigation that is still continuing. (a) Show why one of the reasons phosgene was an effective weapon is that it would collect in low spots soldiers often mistakenly entered for protection. (b) Pete's intention was to let the tube equilibrate at room temperature ( \(23^{\circ} \mathrm{C}\) ) and atmospheric pressure. How many gram-moles of phosgene would have been contained in the sample fed to the chromatograph if his plan had worked? (c) The laboratory in which Pete was working had a volume of \(2200 \mathrm{ft}^{3}\), the specific gravity of liquid phosgene is \(1.37,\) and Pete had read somewhere that the maximum "safe" concentration of phosgene in air is \(0.1 \mathrm{ppm}\) \(\left(0.1 \times 10^{-6} \mathrm{mol} \mathrm{CCl}_{2} \mathrm{O} / \mathrm{mol}\) air) \right. Would the "safe" concentration have been exceeded if all the liquid phosgene in the tube had evaporated into the room? Even if the limit would not have been exceeded, give several reasons why the lab would still have been unsafe. (d) List several things Pete did (or failed to do) that made his experiment unnecessarily hazardous.

The concentration of oxygen in a 5000 -liter tank containing air at 1 atm is to be reduced by pressure purging prior to charging a fuel into the tank. The tank is charged with nitrogen up to a high pressure and then vented back down to atmospheric pressure. The process is repeated as many times as required to bring the oxygen concentration below 10 ppm (i.c., to bring the mole fraction of \(\mathrm{O}_{2}\) below \(10.0 \times 10^{-6}\) ). Assume that the temperature is \(25^{\circ} \mathrm{C}\) at the beginning and end of each charging cycle. When doing \(P V T\) calculations in Parts (b) and (c), use the generalized compressibility chart if possible for the fully charged tank and assume that the tank contains pure nitrogen. (a) Speculate on why the tank is being purged. (b) Estimate the gauge pressure (atm) to which the tank must be charged if the purge is to be done in one charge-vent cycle. Then estimate the mass of nitrogen (kg) used in the process. (For this part, if you can't find the tank condition on the compressibility chart, assume ideal-gas behavior and state whether the resulting estimate of the pressure is too high or too low.) (c) Suppose nitrogen at 700 kPa gauge is used for the charging. Calculate the number of charge-vent cycles required and the total mass of nitrogen used. (d) Use your results to explain why multiple cycles at a lower gas pressure are preferable to a single cycle. What is a probable disadvantage of multiple cycles?

The product gas from a coal gasification plant consists of 60.0 mole \(\%\) CO and the balance \(\mathrm{H}_{2}\); it leaves the plant at \(150^{\circ} \mathrm{C}\) and 135 bar absolute. The gas expands through a turbine, and the outlet gas from the turbine is fed to a boiler furnace at \(100^{\circ} \mathrm{C}\) and 1 atm at a rate of \(425 \mathrm{m}^{3} / \mathrm{min}\). Estimate the inlet flow rate to the turbine in \(\mathrm{ft}^{3} / \mathrm{min},\) using Kay's rule. What percentage error would result from the use of the ideal-gas equation of state at the turbine inlet?

A fuel cell is an electrochemical device that reacts hydrogen with oxygen from the air to produce water and DC electricity. A proposed application is replacement of the gasoline-fueled internal combustion engine in an automobile with a \(100 \mathrm{kW}\) fuel cell. You are on a summer internship with a gas supplier planning to transport hydrogen to service stations for use in cars powered by fuel cells. The hydrogen is to be transported in tube trailers, each of which has 10 tubes of length \(10.5 \mathrm{m}\) and diameter \(0.56 \mathrm{m}\). Hydrogen in the tubes at 2600 psig and an average temperature of \(298 \mathrm{K}\) is discharged at service stations to a final pressure of 55 psig. Refueling cach fuel-cell-powered automobile is estimated to require 4.0 kg of hydrogen. (a) You and your office-mate- an intern from a different university - have been asked to estimate the number of automobiles that can be refueled by one tube-trailer load of hydrogen. He does a very quick calculation and comes up with a value of 95 cars. Speculate how he did it and provide support for your speculation. What was his mistake? (b) Do the calculation using the SRK equation of state. Instead of using Eqs. \(5.3-11\) and \(5.3-13\) for the parameter \(\alpha,\) use the following correlation developed specifically for hydrogen: \(^{23}\) \(\alpha=1.202 \exp \left(-0.3228 T_{\mathrm{r}}\right)\) (c) Do the calculation using the law of corresponding states. (d) In which of the three estimates would you have the greatest confidence, and why?

A gas cylinder filled with nitrogen at standard temperature and pressure has a mass of \(37.289 \mathrm{g}\). The same container filled with carbon dioxide at STP has a mass of 37.440 g. When filled with an unknown gas at STP, the container mass is \(37.062 \mathrm{g}\). Calculate the molecular weight of the unknown gas, and then state its probable identity.

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