Gas streams containing hydrogen and nitrogen in different proportions arc produced on request by blending gases from two feed tanks: Tank A (hydrogen mole fraction = jea) and Tank B (hydrogen mole fraction = jeb )• The requests specify the desired hydrogen mole fraction, jep, and mass flow rate of the product stream, zhP(kg/h).
- Suppose the feed tank compositions are xa = 0.10 mol Hi/mol and xb = 0.50 mol H?/mol, and the desired blend-stream mole fraction and mass flow rate are xp = 0.20 mol H2/mol and ihp = lOOkg/h. Draw and label a flowchart and calculate the required molar flow rates of the feed mixtures, «A(kmol/h) and /iB(kmol/h).
- Derive a series of formulas for nA and ziB *n terms of xA, xB. xp, and mP. Test them using the values in Part (a).
- Write a spreadsheet that has column headings XA,XB.xP,zzzp,ziA.andziB. The spreadsheet should calculate entries in the last two columns corresponding to data in the first four. In the first six data rows of the spreadsheet, do the calculations for jea = 0.10, jeb = 0.50, and jep = 0.10. 0.20. 0.30, 0.40. 0.50, and 0.60, all forzzzP = lOOkg/h. Then in the next six rows repeat the calculations for the same values of jea, xb, and xP for zzzP = 250 kg/h. Explain any of your results that appear strange or impossible.
- Enter the formulas of Part (b) into an equation-solving program. Run the program to determine zza and hBfor the 12 sets of input variable values given in Part (c) and explain any physically impossible results.
Want to see the full answer?
Check out a sample textbook solutionChapter 4 Solutions
ELEM.PRIN.OF CHEMICAL PROC.-W/ACCESS
Additional Engineering Textbook Solutions
Starting Out with Java: From Control Structures through Objects (7th Edition) (What's New in Computer Science)
Concepts Of Programming Languages
Electric Circuits. (11th Edition)
Starting Out with Programming Logic and Design (5th Edition) (What's New in Computer Science)
Degarmo's Materials And Processes In Manufacturing
Computer Science: An Overview (13th Edition) (What's New in Computer Science)
- please, provide me with right resultsarrow_forwardEx. HW. A vertical glass tube, 2cm ID & 5m long in heated uniformly over its length. The water enter at (200-204 C) & 68.9 bar calculated the pressure drop if the flowrate 0.15 Kg/s & the power applied as a heat to the fluid is 100KW using the homogeneous model. Given that enthalpy at inlet temp.=0.87MJ/Kg, enthalpy saturation temp (285C)=1.26 MJ/Kg and μl=0.972*10-4 Ns/m2, μG=2.89*10-5 Ns/m2, UG=2.515*10-2m3/Kg and the change in UG over range of pressure=-4.45*10-4m3/Kg/bar.arrow_forward4. An experimental test rig is used to examine two-phase flow regimes in horizontal pipelines. A particular experiment involved uses air and water at a temperature of 25°C, which flow through a horizontal glass tube with an internal diameter of 25.4 mm and a length of 40 m. Water is admitted at a controlled rate of 0.026 kgs at one end and air at a rate of 5 x 104 kgs in the same direction. The density of water is 1000 kgm³, and the density of air is 1.2 kgm. Determine the mass flow rate, the mean density, gas void fraction, and the superficial velocities of the air and water. Answer: 0.02605 kgs 1, 61.1 kgm³, 0.94, 0.822 ms-1, 0.051 ms-1arrow_forward
- and the viscosity of the water is 1.24 × 104 Nsm 2. Answer: Slug flow 1. Determine the range of mean density of a mixture of air in a 50:50 oil-water liquid phase across a range of gas void fractions. The den- sity of oil is 900 kgm³, water is 1000 kgm³, and gas is 10 kgm³.arrow_forwardA chemical reaction takes place in a container of cross-sectional area 50.0 cm2. As a result of the reaction, a piston is pushed out through 15 cm against an external pressure of 121 kPa. Calculate the work done (in J) by the system.arrow_forwardExample 7.2 Steam is generated in a high pressure boiler containing tubes 2.5 m long and 12.5 mm internal diameter. The wall roughness is 0.005 mm. Water enters the tubes at a pressure of 55.05 bar and a temperature of 270°C, and the water flow rate through each tube is 500 kg/h. Each tube is heated uniformly at a rate of 50 kW. Calle (a) Estimate the pressure drop across each tube (neglecting end effects) using (i) the homogeneous flow model and (ii) the Martinelli-Nelson correlation. (b) How should the calculation be modified if the inlet temperature were 230°C at the same pressure?arrow_forward
- Please solve this question by simulation in aspen hysysarrow_forward(11.35. For a binary gas mixture described by Eqs. (3.37) and (11.58), prove that: 4812 Pу132 ✓ GE = 812 Py1 y2. ✓ SE dT HE-12 T L = = (812 - 7 1/8/123) d² 812 Pylyz C=-T Pylyz dT dT² See also Eq. (11.84), and note that 812 = 2B12 B11 - B22. perimental values of HE for binary liquid mixtures ofarrow_forwardplease provide me the solution with more details. because the previous solution is not cleararrow_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