Concept explainers
(a)
Interpretation:
A flow diagram for the process needs to be drawn and the molar amount of product stream component along with extent of reaction needs to be determined.
Concept introduction:
Flow chart for the process is determined on the values of input and output that is the amount of feed entered in the reactor and product is formed also helps to predict the amount accumulated during formation of product.
For a single reaction system, the final moles of each of the components present can be estimated by the equation:
Here,
The values of number of moles for product stream calculation is based on the number of moles for product is calculated from feed stream that is product formed with respect to the feed consumed reference need to be taken from given reaction
(b)
Interpretation:
An assumption for which the value of energy balance
Concept introduction:
The amount of heat transferred can be represented as follows:
Here,
Enthalpy of reactant and product depends upon the specific heat and the temperature difference.
(c)
Interpretation:
The value of
Concept introduction:
The amount of heat transferred is represented as follows:
Here,
Enthalpy of reactant and product depends upon the specific heat and the temperature difference.
(d)
Interpretation:
Percentage error for outlet temperature Tout is to be calculated for given condition.
Concept introduction:
The amount of heat transferred is represented as follows:
Here,
And,
Enthalpy of reactant and product depends upon the specific heat and the temperature difference.
(e)
Interpretation:
Based on the value of Tout , whether it was a potential error or not needs to be determined for the given condition.
Concept introduction:
The amount of heat transferred is represented as follows:
Here,
And,
Where,
Enthalpy of reactant and product depends upon the specific heat and the temperature difference.
![Check Mark](/static/check-mark.png)
Want to see the full answer?
Check out a sample textbook solution![Blurred answer](/static/blurred-answer.jpg)
Chapter 9 Solutions
ELEM.PRIN.OF CHEM.PROCESS-ACCESS
- 2- What will be the power required to crush 150 tonnes per hour of limestone if 80 percent of the feed passes 50 mm screen and 80 percent of the product a 3.125 mm screen? Work index of limestone 12.74.arrow_forward3- A certain crusher accepts a feed material having a volume-surface mean diameter of 19 mm and gives a product of volume-surface mean diameter of 5 mm. The power required to crush 15 tonnes per hour is 7.5 kW. What will be the power consumption if the capacity is reduced to 12 tonnes per hour?arrow_forwardCR = CAOK1 K2-K1 - Cs CAO CR - CA = [e-k₁t + e-k₂t] --(6) Cs = Cao CAO 1+ K₂e-kit K₁e-k2t + K1-K2 K₂-K1 By differentiating eq (6) and set to zero (dCR = 0), the time at which concentration of R occurs is thus: dT K2 1 In Ki K1 tmax K₂-K1 Klogmean (7) Equation 7. Prove that?arrow_forward
- Question #6 a) Draw a simple block flow diagram of a petroleum refinery consisting of following sections. 1. Atmospheric and vacuum distillation 2. Hydrotreating of diesel steam 3. Hydrocracking of LVGO Show main product streams from each unit. (8)arrow_forwardPhosphate often needs to be removed from wastewater because it will cause eutrophication of receiving waters. At the Paso Robles Wastewater Treatment plant, they add MgCl2 to the pressate (concentrated liquid pressed from sludge) to precipitate phosphate as the mineral struvite. Struvite is formed by the reaction of phosphate with magnesium ions and ammonium, and the solubility product for struvite is 5.5x10-14. The ammonium concentration is very high at 300 mg N-NH4/L because the sludge is coming from an anaerobic digester. What minimum amount of MgCl2 (in mg/L) would be needed to precipitate all but 1 mg/L phosphate? Struvite precipitates by the following reaction: Mg++NH] +PO →MgNH PO 4 4 4arrow_forward· What is the pH of the following solutions? a) 1.0 M HCI (strong acid) b) 50 mg/L NaOH (strong base) • c) 0.10 M acetic acid (Ka = 1.75x10-5)arrow_forward
- A drinking water sample has 500 mg/L NaCl and 100 mg/L CaCO3. A. Calculate the ionic strength assuming no other ions present. B. What would be the activity coefficient for Pb2+ in this water? C. For a lead concentration of 15 ppb (SDWA standard), what would be the molarity and activity of the lead in this bottled water?arrow_forwardThe Debye-Hückel Theory and the Güntelberg and Davies Approximations are not accurate for very high ionic-strength solutions like seawater. Thus, more complicated methods must be used to calculate activity coefficients in seawater, or they can be determined experimentally. One study reported the following activity coefficients: Chemical Species Activity Coefficient (y) Ca2+ 0.28 CO32- 0.20 CaCO3 1.13* For a seawater sample with 140 µM Ca 2+ and 210 μM CO32-, let's determine if precipitation of CaCO3 is thermodynamically favorable: A) If you ignored the effect of the salinity on the activities of all the chemical species, what would be the value of Q? Based on this value of Q, would you expect CaCO3 to precipitate? B) Considering the activity coefficients given in the table above, what would be the value of Q (IAP)? Based on this value of Q (IAP), would you expect CaCO3 to precipitate?arrow_forwardA water sample contains 50 mg/L of Zn2+. How high must the pH be raised to precipitate all but 1 mg/L of the zinc? Assume that zinc primarily reacts with hydroxide ions in solution as part of its governing solubility equilibrium.arrow_forward
- Introduction to Chemical Engineering Thermodynami...Chemical EngineeringISBN:9781259696527Author:J.M. Smith Termodinamica en ingenieria quimica, Hendrick C Van Ness, Michael Abbott, Mark SwihartPublisher:McGraw-Hill EducationElementary Principles of Chemical Processes, Bind...Chemical EngineeringISBN:9781118431221Author:Richard M. Felder, Ronald W. Rousseau, Lisa G. BullardPublisher:WILEYElements of Chemical Reaction Engineering (5th Ed...Chemical EngineeringISBN:9780133887518Author:H. Scott FoglerPublisher:Prentice Hall
- Industrial Plastics: Theory and ApplicationsChemical EngineeringISBN:9781285061238Author:Lokensgard, ErikPublisher:Delmar Cengage LearningUnit Operations of Chemical EngineeringChemical EngineeringISBN:9780072848236Author:Warren McCabe, Julian C. Smith, Peter HarriottPublisher:McGraw-Hill Companies, The
![Text book image](https://www.bartleby.com/isbn_cover_images/9781259696527/9781259696527_smallCoverImage.gif)
![Text book image](https://www.bartleby.com/isbn_cover_images/9781118431221/9781118431221_smallCoverImage.gif)
![Text book image](https://www.bartleby.com/isbn_cover_images/9780133887518/9780133887518_smallCoverImage.gif)
![Text book image](https://www.bartleby.com/isbn_cover_images/9781119285915/9781119285915_smallCoverImage.gif)
![Text book image](https://www.bartleby.com/isbn_cover_images/9781285061238/9781285061238_smallCoverImage.gif)
![Text book image](https://www.bartleby.com/isbn_cover_images/9780072848236/9780072848236_smallCoverImage.gif)