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The liquid level in a tank is determined by measuring the pressure at the bottom of the tank. A calibration curve is prepared by filling the tank to several known levels, reading the bottom pressure from a Bourdon gauge, and drawing a plot of level (m) vs. pressure (Pa). (a) Would you expect the calibration curve to be a straight line? Explain your answer. (b) The calibration experiment was done using a liquid with a specific gravity of \(0.900,\) but the tank is used to store a liquid with specific gravity of \(0.800 .\) Will the liquid level determined from the calibration curve be too high, too low, or correct? Explain. (c) If the actual liquid level is 8.0 meters, what value will be read from the calibration curve? If the tank has a height of \(10.0 \mathrm{m},\) what value will be read from the curve when the tank overflows?

Short Answer

Expert verified
The calibration curve of level (m) vs pressure (Pa) will be a straight line due to the direct proportionality of pressure and liquid height. The liquid level determined from the calibration curve will be higher than the actual level due to the lower specific gravity of the stored liquid. For an actual liquid level of 8.0m, the read value will be greater and when the tank overflows, the reading will also be greater than the actual height of 10.0m.

Step by step solution

01

Understand the Pressure-Height Relation

The pressure at the bottom of a tank is given by the equation \(P=\rho gh\), where \(\rho\) is the fluid density, \(g\) is the acceleration due to gravity, and \(h\) is the height of the liquid column. Since \(\rho\) and \(g\) are constants, \(P\) is directly proportional to \(h\). Therefore, yes, we would expect the calibration curve of level (m) vs. pressure (Pa) to be a straight line.
02

Effect of Specific Gravity on Reading

The specific gravity of a liquid is the ratio of the density of the liquid to the density of water. If the specific gravity of the liquid used to calibrate the gauge is different from the specific gravity of the liquid being measured, then the reading will be off. Specifically, if the specific gravity of the liquid in use is less than the specific gravity of the liquid used for calibration (0.800 < 0.900), then the liquid level determined from the calibration curve will be too high.
03

Calculation of Liquid Level Reading

The pressure at the bottom of the tank when it is filled with 8 meters of the liquid to be stored can be calculated using the equation \(P=\rho gh\). The calculated pressure can then be used to read the liquid level from the calibration curve. Since the specific gravity of the liquid to be stored is less than the specific gravity of the liquid used for calibration, the read liquid level will be greater than 8.0 meters. Similarly, when the tank overflows (h=10.0m), the reading will be greater than 10.0 meters.

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Key Concepts

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

Understanding the Calibration Curve
When measuring liquid levels in a tank using pressure, creating a calibration curve is an essential step. This curve establishes the relationship between the measurable pressure at the bottom of the tank and the known liquid levels. The pressure can be modeled mathematically by the equation
\(P = \rho gh\),
where \(P\) is pressure, \(\rho\) is the density of the liquid, \(g\) is the gravitational acceleration, and \(h\) is the liquid's height. A fundamental assumption for the calibration curve to be a straight line is that both \(\rho\) and \(g\) remain constant, so pressure changes linearly with height. Any deviations from linearity could suggest changes in density, perhaps due to temperature variations, or errors in measurement. When plotting this relationship, a calibration curve can be used to determine unknown liquid levels by measuring pressure.

Calibration Curve and Its Linearity

A straight-line calibration curve simplifies the process of converting pressure readings into liquid level measurements. It allows for a straightforward interpretation where each pressure value corresponds to a unique liquid level. Therefore, for cases where the tank conditions are stable, a straight line is expected for the calibration curve. Any changes in the substance being measured, or the conditions under which the pressure is read, can affect the accuracy of the calibration and hence the usefulness of the curve.
Impact of Specific Gravity on Measurement
Specific gravity plays a pivotal role in accurately measuring liquid levels through pressure. It is defined as the ratio of a substance's density to that of a reference substance, typically water for liquids. This means that specific gravity is a dimensionless quantity, expressing how dense a substance is compared to water.

When dealing with liquids of different specific gravities, the pressure exerted at the bottom of the tank will vary, affecting the level measurement. For the problem at hand, since the specific gravity of the liquid used during calibration (0.900) is higher than that of the liquid in practical use (0.800), the actual pressure exerted for a given liquid level will be lower. As a result, the level read from a curve calibrated with a liquid of higher specific gravity will be erroneously high.

Adjusting for Specific Gravity Changes

To ensure accurate readings, it might be necessary to adjust the calibration curve or compensate for the difference in specific gravity between calibration and actual operating conditions. This ensures precision in level determination and avoids potential mistakes in assessing the amount of liquid in storage or processing units.
Bourdon Gauge Pressure Measurement Technique
The Bourdon gauge is a widely used device for measuring pressure, known for its simplicity and durability. It consists of a curved tube that straightens as pressure increases. This mechanical movement is then converted into a dial or a pointer movement, which provides a visual representation of the pressure.

The device’s operation is based on the elastic properties of the Bourdon tube; as the internal pressure rises, the curvature changes, and this change is calibrated to indicate pressure. Bourdon gauges are often used in various settings, including industrial processes, HVAC systems, and even domestic applications like a home boiler system. In the context of liquid level measurement, the gauge’s pressure reading—once correlated with a calibration curve—can translate to an accurate assessment of the liquid column height.

Advantages of Bourdon Gauges

Bourdon gauges offer several advantages, including robustness against harsh conditions, ease of calibration, and a broad range of measurable pressures, making them suitable for use with a range of liquids and gases. A clear understanding of the gauge’s function is essential for interpreting pressure readings accurately and ensuring that factors like specific gravity are appropriately considered in the established calibration curve for precise liquid level measurements.

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Most popular questions from this chapter

An open-end mercury manometer is connected to a low-pressure pipeline that supplies a gas to a laboratory. Because paint was spilled on the arm connected to the line during a laboratory renovation, it is impossible to see the level of the manometer fluid in this arm. During a period when the gas supply is connected to the line but there is no gas flow, a Bourdon gauge connected to the line downstream from the manometer gives a reading of 7.5 psig. The level of mercury in the open arm is \(900 \mathrm{mm}\) above the lowest part of the manometer. (a) When the gas is not flowing, the pressure is the same everywhere in the pipe. How high above the bottom of the manometer would the mercury be in the arm connected to the pipe? (b) When gas is flowing, the mercury level in the visible arm drops by \(25 \mathrm{mm}\). What is the gas pressure (psig) at this moment?

The level of toluene (a flammable hydrocarbon) in a storage tank may fluctuate between 10 and \(400 \mathrm{cm}\) from the top of the tank. Since it is impossible to see inside the tank, an open-end manometer with water or mercury as the manometer fluid is to be used to determine the toluene level. One leg of the manometer is attached to the tank \(500 \mathrm{cm}\) from the top. A nitrogen blanket at atmospheric pressure is maintained over the tank contents. (a) When the toluene level in the tank is 150 cm below the top \((h=150 \mathrm{cm})\), the manometer fluid level in the open arm is at the height of the point where the manometer connects to the tank. What manometer reading, \(R\) (cm), would be observed if the manometer fluid is (i) mercury, (ii) water? Which manometer fluid would you use, and why? (b) Briefly describe how the system would work if the manometer were simply filled with toluene. Give several advantages of using the fluid you chose in Part (a) over using toluene. (c) What is the purpose of the nitrogen blanket?

A mixture of methane and air is capable of being ignited only if the mole percent of methane is between 5\% and 15\%. A mixture containing 9.0 mole\% methane in air flowing at a rate of 7.00 \(\times 10^{2} \mathrm{kg} / \mathrm{h}\) is to be diluted with pure air to reduce the methane concentration to the lower flammability limit. Calculate the required flow rate of air in mol/h and the percent by mass of oxygen in the product gas. (Note: Air may be taken to consist of \(\left.21 \text { mole } \% \mathrm{O}_{2} \text { and } 79 \% \mathrm{N}_{2} \text { and to have an average molecular weight of } 29.0 .\right)\)

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