/*! 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 14 Strawberries contain about \(15 ... [FREE SOLUTION] | 91Ó°ÊÓ

91Ó°ÊÓ

Strawberries contain about \(15 \mathrm{wt} \%\) solids and \(85 \mathrm{wt} \%\) water. To make strawberry jam, crushed strawberries and sugar are mixed in a 45: 55 mass ratio, and the mixture is heated to evaporate water until the residue contains one-third water by mass. (a) Draw and label a flowchart of this process. (b) Do the degree-of-freedom analysis and show that the system has zero degrees of freedom (i.e., the number of unknown process variables equals the number of equations relating them). If you have too many unknowns, think about what you might have forgotten to do. (c) Calculate how many pounds of strawberries are needed to make a pound of jam. (d) Making a pound of jam is something you could accomplish in your own kitchen (or maybe even a dorm room). However, a typical manufacturing line for jam might produce 1500 1b_m/h. List technical and economic factors you would have to take into account as you scaled up this process from your kitchen to a commercial operation.

Short Answer

Expert verified
A pound of strawberry jam requires more than a pound of strawberries – the exact mass can be calculated using mass balance equations. Scaling up the process from kitchen to commercial scale involves several factors such as product quality control, process efficiency, costs of raw materials and equipment, regulatory compliance, and process optimization.

Step by step solution

01

Drawing Flowchart

Firstly draw a flowchart. Create three boxes to indicate the input, the process, and the output. The input box (Strawberries & Sugar) should show ratios of solids, water, and sugar. The process (Mixing & Heating) contains steps of mixing the strawberries and sugar, and then heating the mixture. The output (Jam) shows one-third water and two-thirds jam by mass.
02

Degree of Freedom Analysis

The number of variables in this system are: mass of strawberry input (m_s), mass of sugar input (m_sg), mass of jam output (m_j), and mass of evaporated water (m_w). The relating equations are: mass balance of total mass, mass balance of solids from strawberries, and mass balance of water. So, Number of unknowns (4) = Number of equations (4). Therefore, degree of freedom = 0.
03

Calculation of Weight of Strawberries Per Pound of Jam

From mass balance of solids from strawberries, \((0.15*m_s) = ((1-1/3) * m_j)\), and from mass balance of water, \((0.85*m_s) = ((1/3 * m_j) + m_w)\), solve these two equations simultaneously for \(m_s\) in terms of \(m_j\). This gives us the pound of strawberries needed to make one pound of jam.
04

Factors in Scaling Up Process

Critical factors include ensuring the maintenance of the product quality, the effective and efficient process of evaporating water, the sources and costs of raw materials (strawberries and sugar), equipment selection and costs, complying with food safety and hygiene regulations, setting up control mechanisms to monitor and optimize the process.

Unlock Step-by-Step Solutions & Ace Your Exams!

  • Full Textbook Solutions

    Get detailed explanations and key concepts

  • Unlimited Al creation

    Al flashcards, explanations, exams and more...

  • Ads-free access

    To over 500 millions flashcards

  • Money-back guarantee

    We refund you if you fail your exam.

Over 30 million students worldwide already upgrade their learning with 91Ó°ÊÓ!

Key Concepts

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

Flowchart
A flowchart is a visual representation of a process, often used in chemical engineering to map out different stages. It provides clarity, showcasing how inputs undergo transformations to result in outputs. In our case, the flowchart begins with strawberries and sugar as inputs, indicating the mix ratio between them. This is followed by the process stage, where the mixture is heated to reduce water content. Finally, the output shows the resulting jam with specific water content.
Flowcharts help bridge the gap between theoretical calculations and practical implementation. They assist engineers in anticipating potential issues, understanding process dynamics, and communicating with team members. By using shapes and arrows, you can track material flows and transformations smoothly.
To create an effective flowchart:
  • Use standard symbols for inputs, processes, and outputs.
  • Clearly label each section.
  • Ensure the flow of the chart matches the sequence of operations.
Mass Balance
Mass balance, a fundamental concept in chemical engineering, involves accounting for all masses entering and leaving a system. It ensures that mass is conserved throughout a process. Think of it as a mathematical check that what goes into a process (input) either stays, transforms, or exits the system (output).
In the strawberry jam example, mass balance equations help determine unknown quantities like the needed mass of strawberries. By establishing equations for solids and water, you can solve for unknowns. For instance, the mass balance on solids from strawberries confirms the consistency of quantities transformed into jam.
To set up a mass balance:
  • Start by identifying all streams entering and exiting the process.
  • Write equations for individual components (e.g., solids, water).
  • Ensure all components are accounted consistently.
Degree of Freedom Analysis
Degree of Freedom Analysis helps determine how constrained a system is by comparing the number of unknowns to the number of equations. Having zero degrees of freedom means that all variables can be calculated using available equations without guessing.
In the strawberry jam scenario, we identify four unknowns: masses of strawberries, sugar, jam, and water evaporated. Three equations arise from mass balances, and thus we can establish a fourth since the total mass of input equals the total mass of output plus losses (evaporation).
To perform a Degree of Freedom Analysis:
  • Count the number of independent variables (unknowns).
  • Create equations from process balances and constraints.
  • Subtract equations from unknowns to find the degree of freedom (should be zero in a well-defined system).
Scaling Up Processes
Scaling up processes involves transitioning from small-scale to large-scale production, a significant step in chemical engineering. This transition involves several technical and economic considerations to ensure success and efficiency.
In transitioning from making jam in a kitchen to a commercial scale, several factors need addressing. First, maintaining product quality is crucial; the taste and texture of the jam should remain consistent. Equipment plays a vital role too, requiring appropriate selection to handle increased material volumes and meet safety standards. Additionally, optimization of heating processes is necessary to ensure efficient water removal without compromising the jam quality.
Some considerations when scaling up:
  • Quality and consistency of product outputs.
  • Sources and costs of raw materials at higher volumes.
  • Industry regulations and compliance, especially for food manufacturing.
  • Operational cost efficiency, including labor, maintenance, and energy use.
Scaling up is not just about replicating what works at a small scale. It demands careful planning, a deep understanding of process dynamics, and adherence to safety and quality standards.

One App. One Place for Learning.

All the tools & learning materials you need for study success - in one app.

Get started for free

Most popular questions from this chapter

Methanol is synthesized from carbon monoxide and hydrogen in a catalytic reactor. The fresh feed to the process contains 32.0 mole \(\%\) CO, \(64.0 \%\) H \(_{2}\), and \(4.0 \%\) Ne. This stream is mixed with a recycle stream in a ratio 5 mol recycle/ 1 mol fresh feed to produce the feed to the reactor, which contains 13.0 mole\% \(\mathrm{N}_{2}\). A low single-pass conversion is attained in the reactor. The reactor effluent goes to a condenser from which two streams emerge: a liquid product stream containing essentially all the methanol formed in the reactor, and a gas stream containing all the \(\mathrm{CO}, \mathrm{H}_{2}\), and \(\mathrm{N}_{2}\) leaving the reactor. The gas stream is split into two fractions: one is removed from the process as a purge stream, and the other is the recycle stream that combines with the fresh feed to the reactor. (a) Assume a methanol production rate of \(100 \mathrm{kmol} / \mathrm{h}\). Perform the DOF for the overall system and all subsystems to prove that there is insufficient information to solve for all unknowns. (b) Briefly explain in your own words the reasons for including (i) the recycle stream and (ii) the purge stream in the process design.

Natural gas containing a mixture of methane, ethane, propane, and butane is burned in a furnace with excess air. (a) One hundred kmol/h of a gas containing 94.4 mole\% methane, 3.40\% ethane, 0.60\% propane, and \(0.50 \%\) butane is to be burned with \(17 \%\) excess air. Calculate the required molar flow rate of the air. (b) Let Derive an expression for \(\dot{n}_{\mathrm{a}}\) in terms of the other variables. Check your formula with the results of Part (a). (c) Suppose the feed rate and composition of the fuel gas are subject to periodic variations, and a process control computer is to be used to adjust the flow rate of air to maintain a constant percentage excess. A calibrated electronic flowmeter in the fuel gas line transmits a signal \(R_{\mathrm{f}}\) that is directly proportional to the flow rate \(\left(\dot{n}_{\mathrm{f}}=\alpha R_{\mathrm{f}}\right),\) with a flow rate of \(75.0 \mathrm{kmol} / \mathrm{h}\) yielding a signal \(R_{f}=60 .\) The fuel gas composition is obtained with an on-line gas chromatograph. A sample of the gas is injected into the gas chromatograph (GC), and signals \(A_{1}, A_{2}, A_{3},\) and \(A_{4},\) which are directly proportional to the moles of methane, ethane, propane, and butane, respectively, in the sample, are transmitted. (Assume the same proportionality constant for all species.) The control computer processes these data to determine the required air flow rate and then sends a signal \(R_{\mathrm{a}}\) to a control valve in the air line. The relationship between \(R_{\mathrm{a}}\) and the resulting air flow rate, \(\dot{n}_{\mathrm{a}},\) is another direct proportionality, with a signal \(R_{\mathrm{a}}=25\) leading to an air flow rate of \(550 \mathrm{kmol} / \mathrm{h}\). Write a spreadsheet or computer program to perform the following tasks: (i) Take as input the desired percentage excess and values of \(R_{\mathrm{f}}, A_{1}, A_{2}, A_{3},\) and \(A_{4}\) (ii) Calculate and print out \(\dot{n}_{\mathrm{f}}, x_{1}, x_{2}, x_{3}, x_{4}, \dot{n}_{\mathrm{a}},\) and \(R_{\mathrm{a}}\) Test your program on the data given below, assuming that \(15 \%\) excess air is required in all cases. Then explore the effects of variations in \(P_{\mathrm{xs}}\) and \(R_{\mathrm{f}}\) on \(\dot{n}_{\mathrm{a}}\) for the values of \(A_{1}-A_{4}\) given on the third line of the data table. Briefly explain your results. (d) Finally, suppose that when the system is operating as described, stack gas analysis indicates that the air feed rate is consistently too high to achieve the specified percentage excess. Give several possible explanations.

Inside a distillation column (see Problem 4.8), a downward-flowing liquid and an upward-flowing vapor maintain contact with each other. For reasons we will discuss in greater detail in Chapter \(6,\) the vapor stream becomes increasingly rich in the more volatile components of the mixture as it moves up the column, and the liquid stream is enriched in the less volatile components as it moves down. The vapor leaving the top of the column goes to a condenser. A portion of the condensate is taken off as a product (the overhead product), and the remainder (the reflux) is returned to the top of the column to begin its downward journey as the liquid stream. The condensation process can be represented as shown below: A distillation column is being used to separate a liquid mixture of ethanol (more volatile) and water (less volatile). A vapor mixture containing 89.0 mole \(\%\) ethanol and the balance water enters the overhead condenser at a rate of \(100 \mathrm{lb}\) -mole/h. The liquid condensate has a density of \(49.01 \mathrm{b}_{\mathrm{m}} / \mathrm{ft}^{3},\) and the reflux ratio is \(3 \mathrm{lb}_{\mathrm{m}}\) reflux/lb \(_{\mathrm{m}}\) overhead product. When the system is operating at steady state, the tank collecting the condensate is half full of liquid and the mean residence time in the tank (volume of liquid/volumetric flow rate of liquid) is 10.0 minutes. Determine the overhead product volumetric flow rate (ft \(^{3}\) /min) and the condenser tank volume (gal).

Oxygen consumed by a living organism in aerobic reactions is used in adding mass to the organism and/or the production of chemicals and carbon dioxide. since we may not know the molecular compositions of all species in such a reaction, it is common to define the ratio of moles of \(\mathrm{CO}_{2}\) produced per mole of \(\mathrm{O}_{2}\) consumed as the respiratory quotient, \(R Q,\) where $$R Q=\frac{n_{\mathrm{CO}_{2}}}{n_{\mathrm{O}_{2}}}\left(\text { or } \frac{\dot{n}_{\mathrm{CO}_{2}}}{\dot{n}_{\mathrm{O}_{2}}}\right)$$ since it generally is impossible to predict values of \(R Q\), they must be determined from operating data. Mammalian cells are used in a bioreactor to convert glucose to glutamic acid by the reaction $$\mathrm{C}_{6} \mathrm{H}_{12} \mathrm{O}_{6}+a \mathrm{NH}_{3}+b \mathrm{O}_{2} \rightarrow p \mathrm{C}_{5} \mathrm{H}_{9} \mathrm{NO}_{4}+q \mathrm{CO}_{2}+r \mathrm{H}_{2} \mathrm{O}$$ The feed to the bioreactor comprises \(1.00 \times 10^{2} \mathrm{mol} \mathrm{C}_{6} \mathrm{H}_{12} \mathrm{O}_{6} / \mathrm{day}, 1.20 \times 10^{2} \mathrm{mol} \mathrm{NH}_{3} / \mathrm{day},\) and \(1.10 \times\) \(10^{2}\) mol \(\mathrm{O}_{2} /\) day. Data on the system show that \(R Q=0.45 \mathrm{mol} \mathrm{CO}_{2}\) produced/mol \(\mathrm{O}_{2}\) consumed. (a) Determine the five stoichiometric coefficients and the limiting reactant. (b) Assuming that the limiting reactant is consumed completely, calculate the molar and mass flow rates of all species leaving the reactor and the fractional conversions of the non-limiting reactants.

In the production of a bean oil, beans containing 13.0 wt\% oil and \(87.0 \%\) solids are ground and fed to a stirred tank (the extractor) along with a recycled stream of liquid \(n\) -hexane. The feed ratio is \(3 \mathrm{kg}\) hexane/kg beans. The ground beans are suspended in the liquid, and essentially all of the oil in the beans is extracted into the hexane. The extractor effluent passes to a filter where the solids are collected and form a filter cake. The filter cake contains 75.0 wt\% bean solids and the balance bean oil and hexane, the latter two in the same ratio in which they emerge from the extractor. The filter cake is discarded and the liquid filtrate is fed to a heated evaporator in which the hexane is vaporized and the oil remains as a liquid. The oil is stored in drums and shipped. The hexane vapor is subsequently cooled and condensed, and the liquid hexane condensate is recycled to the extractor. (a) Draw and label a flowchart of the process, do the degree-of-freedom analysis, and write in an efficient order the equations you would solve to determine all unknown stream variables, circling the variables for which you would solve. (b) Calculate the yield of bean oil product (kg oil/kg beans fed), the required fresh hexane feed \(\left(\mathrm{kg} \mathrm{C}_{6} \mathrm{H}_{14} / \mathrm{kg} \text { beans fed }\right),\) and the recycle to fresh feed ratio (kg hexane recycled/kg fresh feed). (c) It has been suggested that a heat exchanger might be added to the process. This process unit would consist of a bundle of parallel metal tubes contained in an outer shell. The liquid filtrate would pass from the filter through the inside of the tubes and then go on to the evaporator. The hot hexane vapor on its way from the evaporator to the extractor would flow through the shell, passing over the outside of the tubes and heating the filtrate. How might the inclusion of this unit lead to a reduction in the operating cost of the process? (d) Suggest additional steps that might improve the process economics.

See all solutions

Recommended explanations on Chemistry Textbooks

View all explanations

What do you think about this solution?

We value your feedback to improve our textbook solutions.

Study anywhere. Anytime. Across all devices.