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One thousand liters of a 95 wt\% glycerol- \(5 \%\) water solution is to be diluted to \(60 \%\) glycerol by adding a \(35 \%\) solution pumped from a large storage tank through a \(5-\mathrm{cm}\) ID pipe at a steady rate. The pipe discharges at a point 23 m higher than the liquid surface in the storage tank. The operation is carried out isothermally and takes 13 min to complete. The friction loss ( \(\hat{F}\) of Equation \(7.7-2\) ) is \(50 \mathrm{J} / \mathrm{kg}\). Calculate the final solution volume and the shaft work in \(\mathrm{kW}\) that the pump must deliver, assuming that the surface of the stored solution and the pipe outlet are both at 1 atm. Data: \(\quad \rho_{\mathrm{H}_{2} \mathrm{O}}=1.00 \mathrm{kg} / \mathrm{L}, \rho_{\mathrm{gly}}=1.26 \mathrm{kg} / \mathrm{L} .\) (Use to estimate solution densities.)

Short Answer

Expert verified
The final volume of the solution is the sum of initial and added fluid volume, and it may be found by utilising successive steps of mass balance and mixture rules for density. The shaft work that the pump must provide can be calculated by taking into account the energy needed for lift, friction loss, and the energy required to overcome the gravitational potential energy difference.

Step by step solution

01

Initial Volume Calculation

Firstly, calculate the initial volume of glycerol (substance A) and water (substance B) in the solution. The given solution is 1000 L and composed of 95 % glycerol and 5 % water. Meaning there is \(0.95 \times 1000\) L of glycerol and \(0.05 \times 1000\) L of water.
02

Fluid solution Calculation

Next, consider the solution added from the storage tank. It consists of 35 \% glycerol (substance A) and 65 \% water (substance B) and the final solution is to be 60 \% glycerol. The mass balance for substance A is: \[ \text{initial of A} + \text{input of A} = \text{final of A} \] Where, \[ \text{initial of A} = \text{Volume of A initially}* \text{Density of A}, \text{input of A} = X*\text{Density of A}*0.35 \] Where X is the total volume of the solution input and \[ \text{final of A} = \text{Volume of A initially} + X \] Solving the above equation provides the value of X.
03

Final volume Calculation

The final volume of solution (F) is the sum of the initial solution and the volume added from the tank, so: \[ \text{F} = 1000 + X \]
04

Shaft work Calculation

In order to find the shaft work, we consider three components: energy required to lift the fluid h height (\(\rho_{fluid} g h\)), loss of energy due to friction (F), and energy required to overcome the potential energy change (\(p_{atm} V_{fluid}/\rho_{fluid}\)). The total shaft work W delivered by the pump will be the sum of these three quantities. \[W = \rho_{fluid} g h + F + p_{atm} V_{fluid}/\rho_{fluid}\] In this equation g is acceleration due to gravity, h is the height of lifting, \(V_{fluid}\) is the volume of fluid being moved, and \(p_{atm}\) is atmospheric pressure. Using the values given in the exercise, the final value of shaft work can then be calculated. This value must then be converted from J to kW and then divided by the time the operation took, 13 min = 780 s, to find the power (P) the pump needs to deliver in kW. \[P = W / 780\]
05

Density of the mixture

In order to find the densities of the initial and final solutions, you should use the rule of mixtures which states that the density of a mixture is equal to the sum of the fraction of each component times its respective density. It can be written as \[\rho_{\text{mix}} = \text{wt \% A} * \rho_A + \text{wt \% B} * \rho_B\] Here, A represents glycerol and B represents water. Using the provided densities of glycerol and water, the densities of the initial and final mixtures can be found.

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Key Concepts

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

Mass Balance
Mass balance is a fundamental principle used in chemical process calculations to maintain equilibrium in a system. In the context of this exercise, it involves calculating the amount of a particular substance before and after a mixture process.

  • Initially, we have 1000 L of a solution that is 95% glycerol and 5% water. This step calculates the initial amounts of each component. For glycerol, it is 0.95 times 1000 L, and for water, 0.05 times 1000 L.
  • We then introduce a second solution containing 35% glycerol to achieve a final mixture of 60% glycerol.
  • Using mass balances, we set up an equation to find how much additional solution we need to add, ensuring that the amount of glycerol and water in the system reaches the desired levels.
Understanding mass balance helps ensure that chemical processes are efficient and that final product compositions meet specific requirements.
Shaft Work Calculation
Shaft work calculation is crucial in determining the energy required for moving fluids using pumps in chemical processes. In this exercise, we aim to find the power needed to pump a dilute solution through a pipe.
  • The height difference between the storage tank and the discharge point is 23 meters, a key factor in the energy required. Gravity acts on the fluid requiring work to move it upward, calculated as \( \rho_{\text{fluid}} g h \).
  • Energy loss due to friction, given as 50 J/kg in the exercise, is another component. It affects the effectiveness of the pump.
  • The equation accounts for atmospheric pressure, which is consistent at both the storage tank surface and the pipe outlet, thus simplifying calculations.
  • Total work is summed and then converted to power by dividing by the total time, 780 seconds, required to complete the operation. This gives us the operational kW necessary from the pump.
Calculating shaft work in this manner illustrates the intricacies of energy management in fluid dynamics, aiding in efficient system design.
Solution Density Estimation
Estimating the density of a solution is a critical part of chemical process calculations. It allows us to determine how solutions behave and interact during mixing.
  • The density of a solution is not the simple average of the component densities but a weighted calculation based on their respective mass percentages, often referred to as the rule of mixtures.
  • For glycerol and water, given densities are 1.26 kg/L and 1.00 kg/L, respectively.
  • The calculation for the final solution density involves summing the product of each component’s weight percentage and its density: \( \rho_{\text{mix}} = (wt\% \text{glycerol}) \times \rho_{\text{glycerol}} + (wt\% \text{water}) \times \rho_{\text{water}} \).
  • Understanding these calculations helps predict how the solution will affect subsequent chemical reactions or physical processes.
Estimation of solution density is vital for ensuring consistency and quality in chemical manufacturing processes.
Fluid Dynamics
Fluid dynamics underpins many chemical engineering operations, especially involving movement through pipes and reactors.
  • Fluid dynamics is key to understanding how the glycerol solution is transported from the storage tank through the pipe system to the mixing area.
  • Pumping fluid up a 23-meter incline requires overcoming both gravitational and frictional forces, which are critical fluid dynamic components.
  • The diameter of the pipe, taken as 5 cm here, influences the flow rate and velocity of the solution, impacting the energy required for pumping.
  • By evaluating these factors, we can ensure that fluid moves efficiently without causing excess energy expenditure or operational issues.
The principles of fluid dynamics enable engineers to design systems that optimize flow paths, minimize energy uses, and enhance process efficiency.

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Most popular questions from this chapter

A certain gasoline engine has an efficiency of \(30 \% ;\) that is, it converts into useful work \(30 \%\) of the heat generated by burning a fuel. (a) If the congine consumes \(0.80 \mathrm{L}\) /h of a gasoline with a heating value of \(3.25 \times 10^{4} \mathrm{kJ} / \mathrm{L}\), how much power does it provide? Express the answer both in \(\mathrm{kW}\) and horsepower. (b) Suppose the fuel is changed to include \(10 \%\) ethanol by volume. The heating value of ethanol is approximately \(2.34 \times 10^{4} \mathrm{kJ} / \mathrm{L}\) and volumes of gasoline and ethanol may be assumed additive. At what rate ( \((\text { / } h\) ) does the fuel mixture have to be consumed to produce the same power as gasoline?

Water from a reservoir passes over a dam through a turbine and discharges from a \(70-\mathrm{cm}\) ID pipe at a point 55 m below the reservoir surface. The turbine delivers 0.80 MW. Calculate the required flow rate of water in \(\left.\mathrm{m}^{3} / \mathrm{min} \text { if friction is neglected. (See Example } 7.7-3 .\right)\) If friction were included, would a higher or lower flow rate be required? (Note: The equation you will solve in this problem has multiple roots. Find a solution less than \(2 \mathrm{m}^{3} / \mathrm{s}\).)

Steam produced in a boiler is frequently "wet"-that is, it is a mist composed of saturated water vapor and entrained liquid droplets. The quality of a wet steam is defined as the fraction of the mixture by mass that is vapor. A wet steam at a pressure of 5.0 bar with a quality of 0.85 is isothermally "dried" by evaporating the entrained liquid. The flow rate of the dried steam is \(52.5 \mathrm{m}^{3} / \mathrm{h}\). (a) Use the steam tables to determine the temperature at which this operation occurs, the specific enthalpies of the wet and dry steams, and the total mass flow rate of the process stream. (b) Calculate the heat input (kW) required for the evaporation process. (c) Suppose leaks developed in the feed pipe to the dryer and in the dryer exit pipe. Speculate on what you would see at each location.

Air is heated from \(25^{\circ} \mathrm{C}\) to \(140^{\circ} \mathrm{C}\) prior to entering a combustion furnace. The change in specific enthalpy associated with this transition is \(3349 \mathrm{J} / \mathrm{mol}\). The flow rate of air at the heater outlet is \(1.65 \mathrm{m}^{3} / \mathrm{min}\) and the air pressure at this point is \(122 \mathrm{kPa}\) absolute. (a) Calculate the heat requirement in \(\mathrm{kW}\), assuming ideal-gas behavior and that kinetic and potential energy changes from the heater inlet to the outlet are negligible. (b) Would the value of \(\Delta \dot{E}_{k}\) [which was neglected in Part (a)] be positive or negative, or would you need more information to be able to tell? If the latter, what additional information would be needed?

A piston-fitted cylinder with a 6 -cm inner diameter contains \(1.40 \mathrm{g}\) of nitrogen. The mass of the piston is 4.50 kg, and a 25.00-kg weight rests on the piston. The gas temperature is 30^ C, and the pressure outside the cylinder is 2.50 atm. (a) Prove that the absolute pressure of the gas in the cylinder is \(3.55 \times 10^{5} \mathrm{Pa}\). Then calculate the volume occupied by the gas, assuming ideal- gas behavior. (b) Suppose the weight is abruptly lifted and the piston rises to a new equilibrium position. Further suppose that the process takes place in two steps: a rapid step in which a negligible amount of heat is exchanged with the surroundings, followed by a slow step in which the gas returns to \(30^{\circ} \mathrm{C}\). Considering the gas as the system, write the energy balances for step \(1,\) step \(2,\) and the overall process. In all cases, neglect \(\Delta E_{\mathrm{k}}\) and \(\Delta E_{\mathrm{p}} .\) If \(\tilde{U}\) varies proportionally with \(T\), does the gas temperature increase or decrease in step 1? Briefly explain your answer. (c) The work done by the gas equals the restraining force (the weight of the piston plus the force due to atmospheric pressure) times the distance traveled by the piston. Calculate this quantity and use it to determine the heat transferred to or from (state which) the surroundings during the process.

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