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DESIGN AND FABRICATION OF
PLUG FLOW REACTOR
BY:
19F-CH-86 ( SAMEER AHMED)
19F-CH-30 (IMAM DIN) INSTRUCTOR: MISS AZKA
INTRODUCTION:
The plug flow reactor (PFR, sometimes called
continuous tubular reactor, CTR) is a tubular
reactor where the feed is continuously
introduced at one end and the products
continuously removed from the other end.
The concentration / temperature in the
reactor is not uniform.
APPLICATIONS:
Common industrial uses of tubular reactors
are in gasoline production, oil cracking,
synthesis of ammonia from its elements,
and the oxidation of sulfur dioxide to sulfur
trioxide.
ADVANTAGES:
 HIGH CONVERSION
GOOD HEAT TRANSFER DURING PROCESS
CONTINUOUS PROCESSING
ECONOMICAL
DISADVANTAGES:
 POOR TEMPERATURE CONTROL
SHUTDOWN AND CLEANING IS EXPENSIVE
DESIGN CALCULATIONS
MATERIAL: PVC PIPE
DIA: 1 Inch = 2.54 cm
TOTAL VOLUME = 155 ml
NUMBER OF INLETS = 2
NUMBER OF OUTLET = 1
WORKING TEMPERATURE = UPTO 40 C
FABRICATION VIDEO:
CALCULATIONS:
The elementary, liquid-phase, irreversible reaction
A + B C
is to be carried out in a flow reactor. A 0.155 𝑑𝑚3
PFR that can only be
operated at 300k ( 27 degree centigrade) . The two feed streams to the
reactor mix to form a single feed stream that is equal molar in A and B, with
a total volumetric flow rate of 10 dm3/min. What is the conversion?
Additional Information: at 300 K, k = 0.07 dm3/mol-min
E = 85000 J/mol-K
CA0 = CB0 = 1 mole/dm 3
vA0 = vB0 = 0.5*v0 = 5 dm3/min
CONT….
Independent Variable: V, FA0, T
Dependent Variable: X
Known: k0, E, V, n0, CA0B, CB0B
Unknowns: X
Assumptions:
1. Isothermal
1. no pressure drop
1. There are no radial variations in the PFR
CONT….
MOLAR BALANCE:
RATE LAW:
STOITIOMETRY – LIQUID , v = vo; EQUAL MOLAR:
CA = CA0(1-X)
CB = CA0(1-X)
CONT….
Evaluate
v A0 = 5 dm3/min
Before mixing
CA0B = 2 mol/dm3
FA0 = CA0B* vA0
FA0 = (5 dm3/min)(2 mol/dm3) = 10 mol/min
After mixing
v0 = vA0 + vB0 = 5 dm3/min + 5 dm3/min = 10 dm3/min
CA0 = 1 mol/dm3
CONT….
INTRODUCTION:
The plug flow reactor model (PFR, sometimes
called continuous tubular reactor, CTR) is
normally the name given to a model used in
chemical engineering to describe chemical
reactions in continuous, flowing systems of
cylindrical geometry.
THANK YOU

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CRE.pptx

  • 1. DESIGN AND FABRICATION OF PLUG FLOW REACTOR BY: 19F-CH-86 ( SAMEER AHMED) 19F-CH-30 (IMAM DIN) INSTRUCTOR: MISS AZKA
  • 2. INTRODUCTION: The plug flow reactor (PFR, sometimes called continuous tubular reactor, CTR) is a tubular reactor where the feed is continuously introduced at one end and the products continuously removed from the other end. The concentration / temperature in the reactor is not uniform.
  • 3. APPLICATIONS: Common industrial uses of tubular reactors are in gasoline production, oil cracking, synthesis of ammonia from its elements, and the oxidation of sulfur dioxide to sulfur trioxide.
  • 4. ADVANTAGES:  HIGH CONVERSION GOOD HEAT TRANSFER DURING PROCESS CONTINUOUS PROCESSING ECONOMICAL
  • 5. DISADVANTAGES:  POOR TEMPERATURE CONTROL SHUTDOWN AND CLEANING IS EXPENSIVE
  • 6. DESIGN CALCULATIONS MATERIAL: PVC PIPE DIA: 1 Inch = 2.54 cm TOTAL VOLUME = 155 ml NUMBER OF INLETS = 2 NUMBER OF OUTLET = 1 WORKING TEMPERATURE = UPTO 40 C
  • 8. CALCULATIONS: The elementary, liquid-phase, irreversible reaction A + B C is to be carried out in a flow reactor. A 0.155 𝑑𝑚3 PFR that can only be operated at 300k ( 27 degree centigrade) . The two feed streams to the reactor mix to form a single feed stream that is equal molar in A and B, with a total volumetric flow rate of 10 dm3/min. What is the conversion? Additional Information: at 300 K, k = 0.07 dm3/mol-min E = 85000 J/mol-K CA0 = CB0 = 1 mole/dm 3 vA0 = vB0 = 0.5*v0 = 5 dm3/min
  • 9. CONT…. Independent Variable: V, FA0, T Dependent Variable: X Known: k0, E, V, n0, CA0B, CB0B Unknowns: X
  • 10. Assumptions: 1. Isothermal 1. no pressure drop 1. There are no radial variations in the PFR
  • 11. CONT…. MOLAR BALANCE: RATE LAW: STOITIOMETRY – LIQUID , v = vo; EQUAL MOLAR: CA = CA0(1-X) CB = CA0(1-X)
  • 12. CONT…. Evaluate v A0 = 5 dm3/min Before mixing CA0B = 2 mol/dm3 FA0 = CA0B* vA0 FA0 = (5 dm3/min)(2 mol/dm3) = 10 mol/min After mixing v0 = vA0 + vB0 = 5 dm3/min + 5 dm3/min = 10 dm3/min CA0 = 1 mol/dm3
  • 14. INTRODUCTION: The plug flow reactor model (PFR, sometimes called continuous tubular reactor, CTR) is normally the name given to a model used in chemical engineering to describe chemical reactions in continuous, flowing systems of cylindrical geometry.