epare a ma nal flowsneet similar to Figure 6.I (shown below) for pro 2400 /hr of vinyi VC) based on the reaction path #5 with the operating parameters provided below. You MUST show the Molar flow ates of ALL compounds in ALL streams in your flowsheet. Reaction Path #5. Balanced process for Chlorination of Ethylene C2H4 + Cl2--> C2H4CI2 (C) Ileat Liberated by Reactinn 130 x 10 Blutr Ileat Abeorbed CzH4 + 2HCI + 1/2 O2--> C2H¾CI2 + H2O 2C2H¾CI2 --> 2C¿H3CI + 2HCI duriag Reaction = 52 x 10 Dluhr (E) (D) 58.00 Ib 2C2H4 + Cl2 +1/2 02 --> 2C2H3CI + H2O (C) 100% Conv. of Cl2 at 80°C and 150 kPa with 15% (G) Direct Chlorination y0C, 15 atm Pyrolysis Sorc CH.C 26 atea 111,AIKI hr CH.CI, HC CH,C, 10O Ibhr 4,900 tbrhr CH, -a CH,C, excess C2H4 CHCI, CHCI + HCI/ (E) 100% Conv. of HCl at 275°C and 150 kPa with 5% 105,500 Ib'hr excess C2H4 (D) 75% Conv. At 500 °C and 3000 kPa. Water is separated from the mixture before entering Figure 6.1 reactor D.
epare a ma nal flowsneet similar to Figure 6.I (shown below) for pro 2400 /hr of vinyi VC) based on the reaction path #5 with the operating parameters provided below. You MUST show the Molar flow ates of ALL compounds in ALL streams in your flowsheet. Reaction Path #5. Balanced process for Chlorination of Ethylene C2H4 + Cl2--> C2H4CI2 (C) Ileat Liberated by Reactinn 130 x 10 Blutr Ileat Abeorbed CzH4 + 2HCI + 1/2 O2--> C2H¾CI2 + H2O 2C2H¾CI2 --> 2C¿H3CI + 2HCI duriag Reaction = 52 x 10 Dluhr (E) (D) 58.00 Ib 2C2H4 + Cl2 +1/2 02 --> 2C2H3CI + H2O (C) 100% Conv. of Cl2 at 80°C and 150 kPa with 15% (G) Direct Chlorination y0C, 15 atm Pyrolysis Sorc CH.C 26 atea 111,AIKI hr CH.CI, HC CH,C, 10O Ibhr 4,900 tbrhr CH, -a CH,C, excess C2H4 CHCI, CHCI + HCI/ (E) 100% Conv. of HCl at 275°C and 150 kPa with 5% 105,500 Ib'hr excess C2H4 (D) 75% Conv. At 500 °C and 3000 kPa. Water is separated from the mixture before entering Figure 6.1 reactor D.
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
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
Transcribed Image Text:**Chlorination of Ethylene - Reaction Pathway and Process Diagram**
**Objective**: Prepare a material flowsheet similar to Figure 6.1 for the production of 2400 lb-mol/hr of Vinyl Chloride (VC) based on reaction path #5, ensuring to show the molar flow rates of all compounds in all streams.
**Reaction Path #5: Balanced Process for Chlorination of Ethylene**
1. **Reactions Involved**:
- \( \text{C}_2\text{H}_4 + \text{Cl}_2 \rightarrow \text{C}_2\text{H}_4\text{Cl}_2 \)
- \( \text{C}_2\text{H}_4 + 2\text{HCl} + \frac{1}{2} \text{O}_2 \rightarrow \text{C}_2\text{H}_4\text{Cl}_2 + \text{H}_2\text{O} \)
- \( 2\text{C}_2\text{H}_4\text{Cl}_2 \rightarrow 2\text{C}_2\text{H}_3\text{Cl} + 2\text{HCl} \)
- \( 2\text{C}_2\text{H}_4 + \text{Cl}_2 + \frac{1}{2} \text{O}_2 \rightarrow 2\text{C}_2\text{H}_3\text{Cl} + \text{H}_2\text{O} \)
2. **Operating Parameters**:
- **C**: 100% Conversion of Cl\(_2\) at 80°C and 150 kPa with 15% excess C\(_2\)H\(_4\)
- **E**: 100% Conversion of HCl at 275°C and 150 kPa with 5% excess C\(_2\)H\(_4\)
- **D**: 75% Conversion at 500°C and 3000 kPa
- Water is separated from the mixture before entering reactor D.
**Explanation of Figure 6.1**:
The flowsheet diagram provides a visual layout of the process for the chlorination of ethylene. It delineates various stages
Expert Solution
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Step 1
The reactions are
Let us assume that all the HCl produced is recovered and is used a reactant.
Basis: 2400 lbmol/h of vinyl chloride
According to stoichiometry of reaction (3)
HCl produced =
C2H4Cl2 needed =
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