Reactor types Flashcards

1
Q

What are the 6 factors involved in reactor design?

A

1) Feedstock composition
2) Scale of process, output of product
3) Process kinetics
4) Reactor type
5) Material of construction, instrumentation, safety
6) Economics

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2
Q

Why are bench scale batch reactors initially used?

A
  • At small scale, heat and mass transfer gradients are minimised
  • Better mixing can happen in smaller reactors
  • More accurate determination of key chemical effects
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3
Q

Why are pilot plants used and some issues?

A
  • Significantly larger than bench scale
  • Can collect data and indicate potential difficulties in scale up to help design full scale reactor
  • Works at a higher pressure
  • Can be more difficult to separate reaction effects from heat&mass transfer e.g temperature gradient at the reactor walls
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4
Q

What are the features of batch reactors?

A
  • No addition of reactants, or removal of products during the reaction
  • Vessel is kept perfectly mixed, uniform concentrations throughout-composition will change with time
  • Uniform temperature throughout-although may change with time
  • Generally used for small scale processes, e.g. fine chemical and pharmaceutical manufacturing
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5
Q

What are some advantages and disadvantages of batch reactors?

A
  • Can be repurposed and produce different products
  • Low capital (startup) cost
  • High labour cost
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6
Q

What is the material balance in a batch reactor?

A

Rate of accumulation of A in reactor = - Rate of A loss by reaction in reactor

-No flow in or out of reactor

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7
Q

What is the rate of disappearance of reactant, A?

A

-rA*Vr

rA=moles of A reacting/(unit volume*time)

Vr= volume of fluid in reactor:

   - When liquid/solid=volume of fluid in reactor
   - When gas=total volume in reactor
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8
Q

What type of reactions are plug flow reactors used for?

A

Gas or liquid phase

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9
Q

What are the features of plug flow reactors?

A
  • Steady movement of material along reactor
  • No attempt to induce mixing, it is at steady state

Assume:

  • At a given position perpendicular to flow there is no pressure, temp or composition change
  • No diffusion between fluids
  • All fluids have the same residence time
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10
Q

When do the assumptions in a plug flow reactor hold true?

A
  • When there is good radial mixing (high flowates, Re > 10^4)
  • When axial mixing can be neglected (length divided by diameter of reactor >50)
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11
Q

What are the 3 types of plug flow reactor?

A

Single tubes- used for minimal heat transfer and smal reaction volumes

Shell&tube- resembles a heat exchanger, often packed with granular material to improve turbulence & mixing, or packed with catalyst

Tubular furnaces- used for highly endothermic reactions with intense heating, burn fuel on outside of tubes, large quantities of feedstock used

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12
Q

What is the mass balance equation for a plug flow reactor?

A

Accumulation = input - output - disappearance by reaction

0 = Fa - (Fa+dFa) - (-ra)dVr

Where d is delta

  • Fa,amount of a
  • ra, disappearance of a
  • Vr, reactor volume
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13
Q

What type of reactions are continous stirred tank reactors used for?

A
  • Liquid phase reactions

- Gas phase in lab kinetic studies

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14
Q

What are the features of continuous stirred reactors?

A
  • Perfect mixing occurs, everythings reacts before leaving, mixture in tank has identical properties to mixture leaving
  • Continuous feed in and out of reactor
  • Inlet stream instanteously mixes with bulk of reactor volume
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15
Q

What Vr do you use in continuous stirred reactir dependent on reactir contents?

A

Gas phase, Vr=whole reactor volume

Liquid phase, Vr= volume of liquid

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16
Q

What is the material balance in continuous stirred reactor?

A

Fa0 = Fa + (-ra)Vr

17
Q

How and why are continuous stirred reactors used in industry

A
  • Used extensively in process industries
  • Mechanical and heat transfer sinular to stirred batch reactors
  • Rate of reaction lower than plug flow as reactants are diluted, therefore tank needs to be bigger than equiv. PFR
  • Easier to control than PFR