ค Example 9.6-3 C₂H6C₂lly + H₂ сенье Иг → гену سوار الم 0.20 reactor (1/²) (0) 14 1m₂ (m³) C₂H4) hy (m) ₂) hy (nut (My) The fractional convernun of ethane is 0. 50% and the fractional yield of ethylene 16 0.971, 4 answers h₁ = 42,4 ms] G₂tts 240.0 mol CHy 237. Y nol th 5.2 MJ RHY -43~ nu Use the atomic Specier balance for Me the thing that the in из ты and
ค Example 9.6-3 C₂H6C₂lly + H₂ сенье Иг → гену سوار الم 0.20 reactor (1/²) (0) 14 1m₂ (m³) C₂H4) hy (m) ₂) hy (nut (My) The fractional convernun of ethane is 0. 50% and the fractional yield of ethylene 16 0.971, 4 answers h₁ = 42,4 ms] G₂tts 240.0 mol CHy 237. Y nol th 5.2 MJ RHY -43~ nu Use the atomic Specier balance for Me the thing that the in из ты and
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
Related questions
Question
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Chemical processes. Use the atomic species balances to calculate n3 and n4. This has two chemical reactions.
![## Example 4.6.3
### Reaction:
\[ \text{C}_2\text{H}_6 \rightarrow \text{C}_2\text{H}_4 + \text{H}_2 \]
\[ \text{C}_4\text{H}_{10} \rightarrow 2\text{C}_2\text{H}_4 \]
### Diagram:
A diagram illustrating a reactor is shown with arrows indicating inflow and outflow:
- **Inputs:**
- 100 mol of \(\text{C}_4\text{H}_{10}\) and other reactants.
- **Outputs:**
- Mixture including \(\text{C}_2\text{H}_{6}\), \(\text{C}_2\text{H}_{4}\), etc.
### Problem Statement:
Determine the fractional yield of ethylene (\(\text{C}_2\text{H}_4\)).
### Calculations:
**Answers:**
- \( n_1 = 423 \) mol \(\text{C}_2\text{H}_4\)
- \( n_2 = 400 \) mol \(\text{C}_2\text{H}_6\)
- \( n_3 = 162 \) mol of another substance
### Notes:
- Use the atomic species balance for N2 and N4.
- Ensure precise calculations for optimal yield assessment.](/v2/_next/image?url=https%3A%2F%2Fcontent.bartleby.com%2Fqna-images%2Fquestion%2F9ba88ecd-654b-4f6b-9783-e93c33ca6a16%2Fd395362e-c85a-458e-8162-8b291b21efb3%2F7eznmi_processed.jpeg&w=3840&q=75)
Transcribed Image Text:## Example 4.6.3
### Reaction:
\[ \text{C}_2\text{H}_6 \rightarrow \text{C}_2\text{H}_4 + \text{H}_2 \]
\[ \text{C}_4\text{H}_{10} \rightarrow 2\text{C}_2\text{H}_4 \]
### Diagram:
A diagram illustrating a reactor is shown with arrows indicating inflow and outflow:
- **Inputs:**
- 100 mol of \(\text{C}_4\text{H}_{10}\) and other reactants.
- **Outputs:**
- Mixture including \(\text{C}_2\text{H}_{6}\), \(\text{C}_2\text{H}_{4}\), etc.
### Problem Statement:
Determine the fractional yield of ethylene (\(\text{C}_2\text{H}_4\)).
### Calculations:
**Answers:**
- \( n_1 = 423 \) mol \(\text{C}_2\text{H}_4\)
- \( n_2 = 400 \) mol \(\text{C}_2\text{H}_6\)
- \( n_3 = 162 \) mol of another substance
### Notes:
- Use the atomic species balance for N2 and N4.
- Ensure precise calculations for optimal yield assessment.
Expert Solution

Step 1: Moles of hydrogen and methane at reactor exit
Two chemical reactions are occurring.
Given, total number of moles entering the reactor
There is 0.850 mol ethane per mole feed.
There is n1, n2, n3 & n4 moles of ethane, ethylene, hydrogen and methane respectively at the reactor exit.
Now we will write atomic species balance for carbon (C)
Similarly, atomic species balance for hydrogen (H)
Step by step
Solved in 3 steps with 11 images

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