/*! 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 42 The temperature in a process uni... [FREE SOLUTION] | 91Ó°ÊÓ

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The temperature in a process unit is controlled by passing cooling water at a measured rate through a jacket that encloses the unit. The exact relationship between the unit temperature \(T\left(^{\circ} \mathrm{C}\right)\) and the water flow rate \(\phi(\mathrm{L} / \mathrm{s})\) is extremely complex, and it is desired to derive a simple empirical formula to approximate this relationship over a limited range of flow rates and temperatures. Data are taken for \(T\) versus \(\phi\). Plots of \(T\) versus \(\phi\) on rectangular and semilog coordinates are distinctly curved (ruling out \(T=a \phi+b\) and \(T=a e^{b \phi}\) as possible empirical functions), but a log plot appears as follows: A line drawn through the data goes through the points \(\left(\phi_{1}=25 \mathrm{L} / \mathrm{s}, T_{1}=210^{\circ} \mathrm{C}\right)\) and \(\left(\phi_{2}=40 \mathrm{L} / \mathrm{s},\right.\) \(\left.T_{2}=120^{\circ} \mathrm{C}\right)\). (a) What is the empirical relationship between \(\phi\) and \(T ?\) (b) Using your derived equation, estimate the cooling water flow rates needed to maintain the process unit temperature at \(85^{\circ} \mathrm{C}, 175^{\circ} \mathrm{C},\) and \(290^{\circ} \mathrm{C}\). (c) In which of the three estimates in Part (b) would you have the most confidence and in which would you have the least confidence? Explain your reasoning.

Short Answer

Expert verified
The empirical relationship between \(\phi\) and \(T\) is \(T = a \phi^{b}\), where the values of \(a\) and \(b\) are determined by solving the corresponding log equations with the provided data points (\(\phi_{1}=25L/s, T_{1}=210^{\circ}C\) and \(\phi_{2}=40L/s, T_{2}=120^{\circ}C\)). Using this equation, the flow rates necessary to maintain temperatures of \(85^{\circ}C, 175^{\circ}C, 290^{\circ}C\) can be calculated. In terms of confidence, estimates falling within the range of the original data points would be most reliable, while those outside this range would be less dependable, as they extend beyond the range over which the empirical relationship is derived.

Step by step solution

01

Determine the function form

Since the line drawn through the data points on the log plot is a straight line, it can be concluded that the relationship between \(T\) and \(\phi\) is of the form \(T = a \phi^{b}\), where \(T\) is the unit temperature, \(\phi\) is the water flow rate, and \(a\) and \(b\) are constants to be determined.
02

Solve for the constants a and b

By taking the logarithm of both sides of the equation \(T = a \phi^{b}\), the equation transforms into a linear form and the constants \(a\) and \(b\) can be solved for. This results in \(\log(T) = \log(a) + b \log(\phi)\). Using the given data points, two equations can be formed: \(\log(T_{1}) = \log(a) + b \log(\phi_{1})\) and \(\log(T_{2}) = \log(a) + b \log(\phi_{2})\). These two equations can be solved simultaneously to find the values of \(a\) and \(b\).
03

Apply equation to calculate flow rates

Apply the derived equation with the determined constants to the desired temperatures to find the necessary flow rates to maintain these temperatures. Rearranging the equation to solve for \(\phi\) gives \(\phi = (\frac{T}{a})^{1/b}\). Place the desired temperatures of \(85^{\circ}C, 175^{\circ}C, 290^{\circ}C\) into this equation to calculate the corresponding flow rates.
04

Evaluate the confidence in estimates

The confidence in these estimates would vary based on their proximity to the original data points used to determine the function. Those estimates closer to the data points are more likely to be accurate since the function is an approximation that's most accurate within the range of provided data. Estimates lying within the range of \(\phi_{1}\) to \(\phi_{2}\) would have higher confidence, while those falling outside would have lesser.

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Key Concepts

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

Chemical Engineering
Chemical Engineering is a multidisciplinary branch of engineering that combines the principles of physics, chemistry, and mathematics to process raw materials or chemicals into more useful or valuable forms. In the context of process temperature control, chemical engineers must understand the behavior of systems where heat transfer is essential.

Temperature regulation in reactors or process units is a critical aspect of chemical engineering, as it can significantly affect the rate of reaction and the stability of the products. Cooling water flow, as demonstrated in the exercise, is an integral element of maintaining desired temperatures within industrial processes. Chemical engineers use empirical relationships, such as the one derived in our exercise, to predict how changes in such variables as flow rate might influence the system's temperature.
Process Control
Process control refers to the methods and technologies used to monitor and adjust manufacturing processes. It is crucial for maintaining product quality, optimizing performance, and ensuring safety. In chemical processes, controlling the temperature is often necessary to ensure that the reactions take place within the optimal temperature range.

To achieve this, control systems employ a variety of sensors and actuators. In our exercise, the flow rate of the cooling water is adjusted to control the temperature, reflecting a direct application of process control. By understanding the empirical relationship between temperature and flow rate, engineers can program control systems to adjust variables in real-time, maintaining optimal operating conditions.
Temperature Control
Temperature control remains a cornerstone of ensuring operational efficiency and safety in chemical processes. The ability to precisely control temperature influences reaction rates, product quality, and energy consumption.

Through heat exchange systems like jackets or coils, fluids such as cooling water absorb excess heat, hence regulating the temperature of the process unit. By adjusting the flow rate of the cooling water, the amount of heat removed from the system can be fine-tuned. As seen in our exercise, determining the empirical relationship between these two variables allows for predictive adjustments and is essential for robust temperature control strategies.
Cooling Water Flow Rate
The flow rate of cooling water is a critical variable in process temperature control. It's indicative of how much water passes through a cooling system at any given time and is usually expressed in liters per second (L/s) or gallons per minute (GPM).

In our exercise, a higher flow rate indicates increased heat removal capacity, hence a lower process unit temperature. However, beyond just determining the flow rate, understanding how it impacts temperature across various conditions is essential. The empirical formula derived offers a simplified representation of this complex interaction, enabling engineers to calculate the necessary flow rates for maintaining specific temperatures.
Logarithmic Relationships
Logarithmic relationships are fundamental when the relationship between two variables is multiplicative rather than additive. These relationships often appear in situations dealing with exponential growth or decay, such as cooling and heating processes in chemical engineering.

By applying logarithms, as shown in the step-by-step solution, nonlinear equations can be linearized, facilitating the determination of unknown constants. These constants can then be applied in the empirical formula to estimate other quantities of interest. In the textbook problem, the logarithmic transformation of the temperature and flow rate data allows for a simple, workable relationship between the two variables over the specified range, which is particularly valuable for process control where predictive capability is key.

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Most popular questions from this chapter

During the early part of the 20 th century, sulfanilamide (an antibacterial drug) was only administered by injection or in a solid pill. In \(1937,\) a pharmaceutical company decided to market a liquid formulation of the drug. Since sulfanilamide was known to be highly insoluble in water and other common pharmaceutical solvents, a number of alternative solvents were tested and the drug was found to be soluble in diethylene glycol (DEG). After satisfactory results were obtained in tests of flavor, appearance, and fragrance, 240 gallons of sulfanilamide in DEG were manufactured and marketed as Elixir Sulfanilamide. After a number of deaths were determined to have been caused by the formulation, the Food and Drug Administration (FDA) mounted a campaign to recall the drug and recovered about 232 gallons. By this time, 107 people had died. The incident led to passage of the 1938 Federal Food, Drug, and cosmetic Act that significantly tightened FDA safety requirements. Not all of the quantities needed in solving the following problems can be found in the text. Give sources of such information and list all assumptions. (a) The dosage instructions for the elixir were to "take 2 to 3 teaspoons in water every four hours." Assume each teaspoon was pure DEG, and estimate the volume (mL) of DEG a patient would have consumed in a day. (b) The lethal oral dose of diethylene glycol has been estimated to be 1.4 mL DEG/kg body mass. Determine the maximum patient mass \(\left(1 \mathrm{b}_{\mathrm{m}}\right)\) for which the daily dose estimated in Part (a) would be fatal. If you need values of quantities you cannot find in this text, use the Internet. Suggest three reasons why that dose could be dangerous to a patient whose mass is well above the calculated value. (c) Estimate how many people would have been poisoned if the total production of the drug had been consumed. (d) List steps the company should have taken that would have prevented this tragedy.

Using dimensional equations, convert (a) 2 wk to microseconds. (b) \(38.1 \mathrm{ft} / \mathrm{s}\) to kilometers/h. (c) \(554 \mathrm{m}^{4} /\) (day \(\cdot \mathrm{kg}\) ) to \(\mathrm{ft}^{4} /\left(\min \cdot \mathrm{lb}_{\mathrm{m}}\right)\)

The following are measured values of a system temperature versus time: $$\begin{array}{|c|c|c|c|c|c|c|}\hline t(\min ) & 0.0 & 2.0 & 4.0 & 6.0 & 8.0 & 10.0 \\\\\hline T\left(^{\circ} \mathrm{C}\right) & 25.3 & 26.9 & 32.5 & 35.1 & 36.4 & 41.2 \\\\\hline\end{array}$$ (a) Use the method of least squares (Appendix A.1) to fit a straight line to the data, showing your calculations. You may use a spreadsheet to evaluate the formulas in Appendix A.1, but do not use any plotting or statistical functions. Write the derived formula for \(T(t)\), and convert it to a formula for \(t(T)\). (b) Transfer the data into two columns on an Excel spreadsheet, putting the \(t\) data (including the heading) in Cells A1-A7 and the \(T\) data (including the heading) in B1-B7. Following instructions for your version of Excel, insert a plot of \(T\) versus \(t\) into the spreadsheet, showing only the data points and not putting lines or curves between them. Then add a linear trendline to the plot (that is, fit a straight line to the data using the method of least squares) and instruct Excel to show the equation of the line and the \(R^{2}\) value. The closer \(R^{2}\) is to 1 , the better the fit.

Calculate (a) the weight in \(\mathrm{Ib}_{\mathrm{f}}\) of a \(25.0-\mathrm{lb}_{\mathrm{m}}\) object. (b) the mass in \(\mathrm{kg}\) of an object that weighs \(25 \mathrm{N}\). (c) the weight in dynes of a 10 -ton object (not metric tons).

The following \((x, y)\) data are recorded: $$\begin{array}{|c|c|c|c|}\hline x & 0.5 & 1.4 & 84 \\\\\hline y & 2.20 & 4.30 & 6.15 \\\\\hline \end{array}$$ (a) Plot the data on logarithmic axes. (b) Determine the coefficients of a power law expression \(y=a x^{b}\) using the method of least squares. (Remember what you are really plotting \(-\) there is no way to avoid taking logarithms of the data point coordinates in this case.) (c) Draw your calculated line on the same plot as the data.

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