What is the equations to design Plug Flow Reactor of Adiabatic operation . if the reaction...
What is the equations to design Plug Flow Reactor of Adiabatic operation . if the reaction is in gas phase and first order .Please provide me with all the equation of (volume,material balance for each material,calculate the temperature,Volumetric flowrate,Molar flowrate ,Mass flowrate and conversion )
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What is the equations to design Plug Flow Reactor of Adiabatic
operation . if the reaction...
The biodiesel formation reaction is carried out in a plug flow reactor. Oil is fed at...
The biodiesel formation reaction is carried out in a plug flow reactor. Oil is fed at a flowrate of 10 mol/s. Methanol is fed at a flowrate of 30 mol/s. Determine the volume of the reactor required for a conversion of 95%. Assume that the reaction is irreversible and the reaction is first order with respect to both oil and methanol. Assume that the density of the mixture stays constant along the reactor as 5000 mol/m3. The rate constant for...
QUESTION 5 The following gas-phase reaction takes place in a plug flow reactor (a tubular reactor)...
QUESTION 5 The following gas-phase reaction takes place in a plug flow reactor (a tubular reactor) that has a diameter of 6 inches and cross sectional area of 0.1 ft2. A C.The reaction rate depends only on the concentration of A, CA, and has the following form: rate of destruction of A-k * CA , where k= 0.124 s-1. The feed consists of pure A, and enters the reactor at a volumetric flowrate of 0.22 ft3/s. Determine the required length...
1. A reactor system consists of a series arrangement of a plug flow reactor and a...
1. A reactor system consists of a series arrangement of a plug flow reactor and a mixed flow rector (continuous stirred tank reactor). The mixed flow reactor has 10 times the volume of the plug flow reactor. Assume the rate equation for the reaction that occurs is given by: r = 2.4 C2 where c is the concentration of the reacting species. The reaction occurs to 96% conversion. The inlet concentration of C is Cao1. You may assume the density...
1. A reactor system consists of a series arrangement of a plug flow reactor and a...
1. A reactor system consists of a series arrangement of a plug flow reactor and a mixed flow rector (continuous stirred tank reactor). The mixed flow reactor has 10 times the volume of the plug flow reactor. Assume the rate equation for the reaction that occurs is given by: r = 2.4 C2 where c is the concentration of the reacting species. The reaction occurs to 96% conversion. The inlet concentration of C is Cao1. You may assume the density...
[TOTAL 30 MARKS! A plug flow reactor (C le and reaction is reversible and represented by...
[TOTAL 30 MARKS! A plug flow reactor (C le and reaction is reversible and represented by (0,04 minT)CA - (0,01 min- 2.2. 2.3, Find the equilibrium conversion Find the actual conversion of A in the reactor We wish to achieve 97.5% of the equilibrium n by adding a CSTR in series with the plug flow reactor. What volume must the CSTR be in order to achieve this? TOTAL 20 MARKS Pure gaseous A at about 3 vanous Row rates. There...
Design a CSTR for the elementary consecutive gas-phase reactions A - B C. Specify the reactor...
Design a CSTR for the elementary consecutive gas-phase reactions A - B C. Specify the reactor volume and the area of the heating coil inside the reactor for 50% conversion. a. Calculate the desired operating temperature inside the reactor. b. Calculate the volume of the reactor c. Calculate the area of the heating surface. The effluent stream should contain a ratio CB/Cc of 10. The feed is gas-phase and pure A at 400°C and 4 atm, with a molar flow...
Continuously operated stirred tank reactor has been design on the assumption of perfect mixing to achieve 90% conversion of the first order reaction. Subsequent flow patterns study (flow visualizatio...
Continuously operated stirred tank reactor has been design on the assumption of perfect mixing to achieve 90% conversion of the first order reaction. Subsequent flow patterns study (flow visualization and RTD measurements) indicate that: (i) 65% of the volume is well mixed, (ii) 20%, of the volume locally exhibits plug flow (ii) 15% volume is inactive and 25% of the feed bypass the reactor. The conversion to be expected from this reactor is to be estimated. Design: У, САЗ-0.1 САО...
3. (a) The elementary gas phase reaction: 2A → 3C takes place in a plug flow...
3. (a) The elementary gas phase reaction: 2A → 3C takes place in a plug flow reactor. The reactor operates isothermally at a temperature of 350 K. The inlet to the reactor is made up from A and inert material. The inlet partial pressures of A and inert material are 10 bar and 20 bar respectively. The rate constant for the reaction is given kr = 1 x 10-6 mmol s1 and the flow rate of incoming A = 2...
The elementary gas phase reaction (A <--> 2B) is to be carried out in an adiabatic...
The elementary gas phase reaction (A <--> 2B) is to be carried out in an adiabatic CSTR. The feed which is at a temperature of 27oC, consists of 80% of A and the remainder inerts. The volumetric flow rate entering the reactor at this temperature is 100 l/min. The concentration of A in the feed at 27oC is 0.5 mol/liter. For 80% of the adiabatic equilibrium conversion, calculate the required reactor volume. DATA: CpA=12 J/mol.K; CpB=10 J/mol.K; CpI=15 J/mol.K deltaHrxn=-75000...
PLEASE HELP!! Consider an adiabatic constant pressure batch reactor for the following ideal gas phase reaction:...
PLEASE HELP!!
Consider an adiabatic constant pressure batch reactor for the following ideal gas phase reaction: 2. A—В+С The reactor initial composition is of 50 mol% A and 50 mol% inert material. The initial reactor temperature is 300 K and the pressure is 101.325 kPa. The reaction rate is: -2,500 (-) kCwhere k=exp| Т The enthalpy of reaction can be assumed constant at -5,000 J/mol. The heat capacities are assumed to be constant, with the following values: В: 5 mol...
QUESTION 5 The following gas-phase reaction takes place in a plug flow reactor (a tubular reactor) that has a diameter of 6 inches and cross sectional area of 0.1 ft2. A C.The reaction rate depends only on the concentration of A, CA, and has the following form: rate of destruction of A-k * CA , where k= 0.124 s-1. The feed consists of pure A, and enters the reactor at a volumetric flowrate of 0.22 ft3/s. Determine the required length...
1. A reactor system consists of a series arrangement of a plug flow reactor and a mixed flow rector (continuous stirred tank reactor). The mixed flow reactor has 10 times the volume of the plug flow reactor. Assume the rate equation for the reaction that occurs is given by: r = 2.4 C2 where c is the concentration of the reacting species. The reaction occurs to 96% conversion. The inlet concentration of C is Cao1. You may assume the density...
1. A reactor system consists of a series arrangement of a plug flow reactor and a mixed flow rector (continuous stirred tank reactor). The mixed flow reactor has 10 times the volume of the plug flow reactor. Assume the rate equation for the reaction that occurs is given by: r = 2.4 C2 where c is the concentration of the reacting species. The reaction occurs to 96% conversion. The inlet concentration of C is Cao1. You may assume the density...
[TOTAL 30 MARKS! A plug flow reactor (C le and reaction is reversible and represented by (0,04 minT)CA - (0,01 min- 2.2. 2.3, Find the equilibrium conversion Find the actual conversion of A in the reactor We wish to achieve 97.5% of the equilibrium n by adding a CSTR in series with the plug flow reactor. What volume must the CSTR be in order to achieve this? TOTAL 20 MARKS Pure gaseous A at about 3 vanous Row rates. There...
Design a CSTR for the elementary consecutive gas-phase reactions A - B C. Specify the reactor volume and the area of the heating coil inside the reactor for 50% conversion. a. Calculate the desired operating temperature inside the reactor. b. Calculate the volume of the reactor c. Calculate the area of the heating surface. The effluent stream should contain a ratio CB/Cc of 10. The feed is gas-phase and pure A at 400°C and 4 atm, with a molar flow...
Continuously operated stirred tank reactor has been design on the assumption of perfect mixing to achieve 90% conversion of the first order reaction. Subsequent flow patterns study (flow visualization and RTD measurements) indicate that: (i) 65% of the volume is well mixed, (ii) 20%, of the volume locally exhibits plug flow (ii) 15% volume is inactive and 25% of the feed bypass the reactor. The conversion to be expected from this reactor is to be estimated. Design: У, САЗ-0.1 САО...
3. (a) The elementary gas phase reaction: 2A → 3C takes place in a plug flow reactor. The reactor operates isothermally at a temperature of 350 K. The inlet to the reactor is made up from A and inert material. The inlet partial pressures of A and inert material are 10 bar and 20 bar respectively. The rate constant for the reaction is given kr = 1 x 10-6 mmol s1 and the flow rate of incoming A = 2...
PLEASE HELP!!
Consider an adiabatic constant pressure batch reactor for the following ideal gas phase reaction: 2. A—В+С The reactor initial composition is of 50 mol% A and 50 mol% inert material. The initial reactor temperature is 300 K and the pressure is 101.325 kPa. The reaction rate is: -2,500 (-) kCwhere k=exp| Т The enthalpy of reaction can be assumed constant at -5,000 J/mol. The heat capacities are assumed to be constant, with the following values: В: 5 mol...
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