11:03 EVo)LTÉ.l 68%Sessional One 23HomeInsertViewReviewQ2. The process shown below, a 95% overall conversion of C3Hg is achieved. Calculate theproduct stream composition, the molar recycle ratio: (recycled)/(fresh feed), and the single-pass conversion.C,H, → C,H, +H,NR1 mol C3HaNr2 mol C3H6 (5% of n)Fresh feedReactorSeparator100 molnimol C3H8na moln6 mol CaHsCaH8C3HB(0.56% of na)NR2 molnamolnz mol C3H6C3H6na mol H2

Given: Feed=100 moles Overall conversion is given as 95% n6=0.56%(n3) Required to find : 1.The…

Answered: Q2. The process shown below, a 95%…

Introduction to Chemical Engineering Thermodynamics

8th Edition

ISBN:9781259696527

Author:J.M. Smith Termodinamica en ingenieria quimica, Hendrick C Van Ness, Michael Abbott, Mark Swihart

Publisher:J.M. Smith Termodinamica en ingenieria quimica, Hendrick C Van Ness, Michael Abbott, Mark Swihart

Chapter1: Introduction

Section: Chapter Questions

Problem 1.1P

See similar textbooks

Similar questions

Methane is found to be present in crude oil deposits. Explain how the fractionation process is carried out to separate methane from other fractions.
I need the answer as soon as possible
Q20. For the electrochemical cell Cr/CRPO4 //CUSOJ Cu [Given E° Cr/Cr = -0.74 V and E° Cu/Cu = +0.16 V] %3D i) Write oxidation half, reduction half and overall reactions. ii) Identify the oxidizing and reducing agent. iii) Construct a neat labelled diagram of electrochemical cell iv) Calculate the e.m.f (E°cell)
Please give me very detailed solution.
Thank you
10.) For the reaction:A + B + C ↓ productsthe following data was obtained. Complete the table. trial # [A]0 (M) [B]0 (M) [C]0 (M) initial rate mole/L.s (M/s) 1 0.21 0.11 0.10 7.01x10-6 2 0.21 0.11 0.20 1.40x10-5 3 0.21 0.33 0.10 7.01x10-6 4 0.42 0.11 0.10 2.80x10-5 5 0.84 0.11 0.10 6 0.21 0.11 3.50x10-6 7 0.11 0.10 1.40x10-5
When a peroxide P is heated to 60 ° C in an inert solvent, it decomposes by a first order process and 20% of the peroxide decomposes in 60 min. Polymerizes a bulk monomer using this initiator at 60 ° C, with an initial concentration of initiator equal to 4.0x10-4 mol / L. What fractions of the monomer and initiator should remain unconverted after 10 min? At 60 ° C, the system parameters are: k two p / kt = 22.34 Lmol-1 s -1 , f = 0.8.
The reaction 2A +5B --- > 3C + 6D Occurs in a reactor where fresh substance A is present with a 30% excess over the stoichiometric amount needed to react with the fresh B. The overall conversion of B in the process is 90% and the one-step conversion of B is 60%. Most of B that do not reacted is recovered in a separator and recirculated to the reactor. The fresh feed to the reactor contains A and B. . Use advance method of the reaction or rate of reaction. Calculate the unknown flows to produce 300 moles/h of C. Construct a table of degrees of freedom, determine solution sequence and validate results with checking. Use reaction progress or reaction rate method Relations: R1: Conversion of B in the reactor of 60% A2: Overall conversion of B is 95% R3: N1 A is fed 30% in excess of the theoretical for react with N1 b.
Prepare a material flowsheet similar to Figure 6.1 (shown below) for production of 2400 lb-mol/hr of Vinyl Chloride (VC) based on the reaction path #5 with the operating parameters provided below. You MUST show the Molar flow rates of ALL compounds in ALL streams in your flowsheet. Reaction Path #5. Balanced process for Chlorination of Ethylene C2H4 + Cl2--> C2H4CI2 (C) Ileat Liberated Ileat Absorbed y Reactinn 150 x 10 Blutr duriag Reaction = 52 x 10 Bluhr C2H4 + 2HCI + 1/2 O2--> C2H4CI2 + H2O 2C2H4CI2 --> 2C;H3CI + 2HCI (E) (D) 58.300 Ibhr 2C2H4 + Cl2 +1/2 O2 --> 2C2H3CI + H2O (C) 100% Conv. of Cl2 at 80°C and 150 kPa with 15% (G) Direct Chlorination YƯ C, 15 atm Pyrolysis Sorc +CH,CI- 26 ata HCI CH.CI, CAL 11.3,4KI hr 158,I Ihyhr CH,CI, C1,CI 4,900 Ihhr CH, -a CH,CI, excess C2H4 CH,ClCH,CI + HCI (E) 100% Conv. of HCl at 275°C and 150 kPa with 5% 105,500 Ib'hr excess C2Н4 (D) 75% Conv. At 500 °C and 3000 kPa. Water is separated from the mixture before entering Figure 6.1 reactor D.
Q2- The synthesis of ammonia proceeds according to the following reaction N₂ + 3 H₂ -----> 2 NH3 In a given plant, 4202 lb of nitrogen and 1046 lb of hydrogen are fed to the synthesis reactor per hour. Production of pure ammonia from this reactor is 3060 lb per hour. a. What is the limiting reactant. b. What is the percent excess reactant. c. What is the percent conversion obtained (based on the limiting reactant).
| (A stripping column with a given number of trays) The vapour phase alkylation of phenol is carried out by a selective zeolite catalyst to yield a mixture of 35 mole% p-cresol and the rest phenol. The mixture which is at its bubble point is to be separated at 1 atm pressure in a stripping column having nine ideal trays and a partial reboiler at a rate of 50 kmol/h to yield 95% p-cresol as the bottom product. The relative volatility of phenol in the mixture is 1.76. Calculate (a) the composition of the top product and (b) the boil-up rate, V/W, where V is the vapour rate and W is the rate removal of the bottom product.
Urgent

SEE MORE QUESTIONS

Recommended textbooks for you

Introduction to Chemical Engineering Thermodynami…

Chemical Engineering

ISBN:

9781259696527

Author:

J.M. Smith Termodinamica en ingenieria quimica, Hendrick C Van Ness, Michael Abbott, Mark Swihart

Publisher:

McGraw-Hill Education

Elementary Principles of Chemical Processes, Bind…

Chemical Engineering

ISBN:

9781118431221

Author:

Richard M. Felder, Ronald W. Rousseau, Lisa G. Bullard

Publisher:

WILEY

Elements of Chemical Reaction Engineering (5th Ed…

Chemical Engineering

ISBN:

9780133887518

Author:

H. Scott Fogler

Publisher:

Prentice Hall

Introduction to Chemical Engineering Thermodynami…

Chemical Engineering

ISBN:

9781259696527

Author:

J.M. Smith Termodinamica en ingenieria quimica, Hendrick C Van Ness, Michael Abbott, Mark Swihart

Publisher:

McGraw-Hill Education

Elementary Principles of Chemical Processes, Bind…

Chemical Engineering

ISBN:

9781118431221

Author:

Richard M. Felder, Ronald W. Rousseau, Lisa G. Bullard

Publisher:

WILEY

Elements of Chemical Reaction Engineering (5th Ed…

Chemical Engineering

ISBN:

9780133887518

Author:

H. Scott Fogler

Publisher:

Prentice Hall

Process Dynamics and Control, 4e

Chemical Engineering

ISBN:

9781119285915

Author:

Seborg

Publisher:

WILEY

Industrial Plastics: Theory and Applications

Chemical Engineering

ISBN:

9781285061238

Author:

Lokensgard, Erik

Publisher:

Delmar Cengage Learning

Unit Operations of Chemical Engineering

Chemical Engineering

ISBN:

9780072848236

Author:

Warren McCabe, Julian C. Smith, Peter Harriott

Publisher:

McGraw-Hill Companies, The

SEE MORE TEXTBOOKS

Q2. The process shown below, a 95% overall conversion of C3Ha is achieved. Calculate the product stream composition, the molar recycle ratio: (recycled)/(fresh feed), and the single- pass conversion. C,H, → C,H. +H,