on 1: 2A The gas phase decomposition (k = 0.001 s) is carried out in a plug flow reactor at 300°C and 10 atm. Reactor feed rate of A is 2 mol/s, and contains 75 mol% inert. Determine the length of 0.0254 m diameter pipe needed to reach 99% conversion. Question 2: A+2B C+D 2028.616 The liquid-phase reaction is first order in both A and B with k=0.0017m³/mol.min at 461°K with E-11273Cal/mol. The initial entering concentrations of A and B are 1.8 mol/m³ and 6.6mol/m³, respectively. What is the rate of reaction (X=90) at 298°K? Question 3: For The following reaction A-1.2611X10-5 Calculate the equilibrium conversion and concentration for the gas phase reaction A+B 2C The reaction carried out in a flow reactor with no pressure drop. the feed is equal molar which is 3 at a temperature of 400 K and 10 atm. At this temperature, Kc= 8(dm³/mol)². Question 4: PA+B C + 2D ll in the following table for CB and X.assuming as a liquid phase & initial concentration of CA-1N CA 1 CB 0.15 X 0.9 0.8 0.7 0.7 0.7 Sectional Area = πD²/4 t 0 1 2 3 4 5
on 1: 2A The gas phase decomposition (k = 0.001 s) is carried out in a plug flow reactor at 300°C and 10 atm. Reactor feed rate of A is 2 mol/s, and contains 75 mol% inert. Determine the length of 0.0254 m diameter pipe needed to reach 99% conversion. Question 2: A+2B C+D 2028.616 The liquid-phase reaction is first order in both A and B with k=0.0017m³/mol.min at 461°K with E-11273Cal/mol. The initial entering concentrations of A and B are 1.8 mol/m³ and 6.6mol/m³, respectively. What is the rate of reaction (X=90) at 298°K? Question 3: For The following reaction A-1.2611X10-5 Calculate the equilibrium conversion and concentration for the gas phase reaction A+B 2C The reaction carried out in a flow reactor with no pressure drop. the feed is equal molar which is 3 at a temperature of 400 K and 10 atm. At this temperature, Kc= 8(dm³/mol)². Question 4: PA+B C + 2D ll in the following table for CB and X.assuming as a liquid phase & initial concentration of CA-1N CA 1 CB 0.15 X 0.9 0.8 0.7 0.7 0.7 Sectional Area = πD²/4 t 0 1 2 3 4 5
Chapter30: Kinetic Methods Of Analysis
Section: Chapter Questions
Problem 30.9QAP
Related questions
Question
Transcribed Image Text:on 1:
2A
The gas phase decomposition (k = 0.001 s) is carried out in a plug flow reactor at 300°C and 10 atm. Reactor
feed rate of A is 2 mol/s, and contains 75 mol% inert. Determine the length of 0.0254 m diameter pipe needed
to reach 99% conversion.
Question 2:
A+2B
C+D
2028.616
The liquid-phase reaction is first order in both A and B with k=0.0017m³/mol.min at 461°K with
E-11273Cal/mol. The initial entering concentrations of A and B are 1.8 mol/m³ and 6.6mol/m³, respectively.
What is the rate of reaction (X=90) at 298°K?
Question 3:
For The following reaction
A-1.2611X10-5
Calculate the equilibrium conversion and concentration for the gas phase reaction
A+B
2C
The reaction carried out in a flow reactor with no pressure drop. the feed is equal molar which is 3 at
a temperature of 400 K and 10 atm. At this temperature, Kc= 8(dm³/mol)².
Question 4:
PA+B C + 2D
ll in the following table for CB and X.assuming as a liquid phase & initial concentration of CA-1N
CA
1
CB
0.15
X
0.9
0.8
0.7
0.7
0.7
Sectional Area = πD²/4
t
0
1
2
3
4
5
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