
(A)
Interpretation:
The exiting velocity of the steam.
Concept Introduction:
The energy balance equation around the nozzle.
Here, mass flow rate for inlet and outlet is
(B)
Interpretation:
The exiting velocity of the nitrogen.
Concept Introduction:
The modified steady state equation.
Refer the Appendix table D.1, “Ideal gas heat capacity”, obtain the ideal gas heat capacity of a compound as a function of temperature.
Here, constant pressure heat capacity on a molar basis for ideal gas is
The expression to calculate the specific change in molar enthalpy for an ideal gas is.
Here, constant pressure heat capacity on a molar basis for ideal gas is
(C)
Interpretation:
The exiting velocity of the ideal gas.
Concept Introduction:
The expression to calculate the specific change in molar enthalpy for an ideal gas.
Here, constant pressure heat capacity on a molar basis for ideal gas is
The modified steady state equation for nozzle with negligible mass.

Trending nowThis is a popular solution!

Chapter 3 Solutions
Fundamentals of Chemical Engineering Thermodynamics, SI Edition
- Chemical Engineering Use the psychrometric chart and demonstrate the linear interpolation method to obtain -0.52 KJ/KgDA. This is the enthalpy deviation. The exercise is uploaded below.arrow_forwardChemical Engineering Use the psychrometric chart. The remaining curves on the psychrometric chart are almost vertical and convex to the left, with labeled values (on Figure 8.4-1) of 0.05, 0.1, 0.2, and so on. (The units of these numbers arekJ/kg DA). Thesecurves are usedto determine theenthalpyof humid air that is not saturated. The procedure is as follows: (a) locate the point on the chart corresponding to air at its specified condition; (b) interpolate to estimate the enthalpy deviation at this point; (c) follow the constant wet-bulb temperature line to the enthalpy scale above the saturation curve, read the value on that scale, and add the enthalpy deviation to it. Also, you will see the exercise on the piece of paper.arrow_forwardCalculate the permeability of the bed of ion-exchange particles in Example 11.1.arrow_forward
- For spherical sand particles with Dp = 0.03 and ρparticles = 150 lbm / ft3 estimate the minimum fluidizing velocity for air and for water. Assume ε = 0.3. In the case of the water we must rederive Eq. 11.42, taking into account the buoyant force on the particles. Below are the provide answers. Please show all work to get to the correct answers.arrow_forwardPlease show all workarrow_forward2. A moving bed adsorption column needs to be designed to separate hydrophobic proteins from a fermentation broth. The following adsorption equilibrium data was observed in preliminary isotherm studies. The resin used was activated carbon with a porosity of 0.2. The overall mass transfer coefficient was determined to be 10 h¹, and the ratio of volumetric flow rate of broth to resin is 10. Determine the diameter of the column if the column height is limited to 2.5 m (indoor operation) with a flow rate of 20 m³/h, influent concentration of 7 g/L, and effluent concentration of 0.1 g/L. qi (mg/kg) Ci (g/L) 0.1 4.7 7.5 0.25 10.6 0.5 15.0 1.0 23.7 2.5 33.5 5.0 41.1 7.5arrow_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





