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CFD of Underground Coal Gasification Presented By Himanshu Arora
26

CFD of Underground Coal Gasification

Mar 04, 2015

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Page 1: CFD of Underground Coal Gasification

CFD of Underground Coal Gasification

Presented By Himanshu Arora

Page 2: CFD of Underground Coal Gasification

What is UCG ?

• Coal is converted insitu into a combustible gas.

• Out coming gases used as fuel

Source : www.coal-ucg.com

Page 3: CFD of Underground Coal Gasification

Why UCG ?

• Mining and conversion accomplished in a single step.

• Eliminates the cost of mining, transportation etc.

• Exploit resources, uneconomic to work by conventional underground coal extraction.

Page 4: CFD of Underground Coal Gasification

Overview of the process

• Chemical reactions occurs in 3 steps

1. Oxidation2. Reduction3. Pyrolysis

Source:www.coal-ucg.com

Page 5: CFD of Underground Coal Gasification

Overview of the process…(contd.) • Cavity Growth

1. Growth occurs between injection well and production well.

2. Cavity consists of four zones.

Source :Britten et al, 1989

Page 6: CFD of Underground Coal Gasification

Objective of the project

• Study the flow pattern and RTD of UCG.

• Reactions not included.• Compare RTD with network of

reactors.• Predict conversion of UCG on

the basis of network model.• Get conversion from

experiments.• Compare experimental and

modeling results.

Page 7: CFD of Underground Coal Gasification

CFD study of a model UCG reactor • Geometric details.• Length = 1m• Width = 0.226m• Depth = 0.226m• Diameter of inlet = 0.02m

Page 8: CFD of Underground Coal Gasification
Page 9: CFD of Underground Coal Gasification

CFD modeling …(contd.)

• Meshing Details

• Mixture of tetragonal and hexagonal cells.

• 2,50,000 volume cells in the whole volume.

• Volume of reactor = 0.0365m3

Page 10: CFD of Underground Coal Gasification
Page 11: CFD of Underground Coal Gasification

CFD modeling …(contd.)

• Boundary conditions.

• Mass flow rate = 0.012kg/hr• Outlet Pressure = 1 atm.• Fluid Porosities

Ash = 0.2 Char = 0.4 Coal = 0.6 Void = 1

Page 12: CFD of Underground Coal Gasification

Flow Pattern

• Steady state velocity profile.

Velocity vectors at plane y=0

Page 13: CFD of Underground Coal Gasification

Flow Pattern…(contd.)

• Tracer named Air1 with mole fraction = 0.05 introduced at the inlet.

• F curve and E curve are studied.

Page 14: CFD of Underground Coal Gasification
Page 15: CFD of Underground Coal Gasification
Page 16: CFD of Underground Coal Gasification

Comparison of RTD with network of reactors.

• Different networks were tried.

• PFR and CSTR in series.• PFR and CSTR in parallel.• Tank in series.

• Tanks in series fitted the best with

n=3 and τ = 5.50e+4 sec

• Τ of UCG = 109062.66sec

Page 17: CFD of Underground Coal Gasification

Comparison of E(t) curvesimulated vs. fitted

0 0.2 0.4 0.6 0.8 1 1.2 1.4 1.6 1.8 2

x 106

0

0.5

1

1.5

2

2.5

3

3.5

4

4.5

5x 10

-6

time(sec)

E(t

)E(t) vs. t

simulationfit

Page 18: CFD of Underground Coal Gasification

CFD study of more complicated geometry

• Geometry details.• Length = 9m• Depth = 5.5m• Diameter of inlet = 0.2m

Page 19: CFD of Underground Coal Gasification
Page 20: CFD of Underground Coal Gasification

CFD modeling…(contd.)

• Meshing Details• Mixture of tetrahedral and

hexagonal cells.• Total of 2,26,330 volume cells.• Volume of UCG = 36.3m3

Page 21: CFD of Underground Coal Gasification
Page 22: CFD of Underground Coal Gasification

Flow pattern

• Due to complexity of the geometry steady state was not achieved.

Page 23: CFD of Underground Coal Gasification

Conclusion

• Studied the velocity profiles in UCG.

• RTD of the UCG. • Compared it with network

of reactors.

Page 24: CFD of Underground Coal Gasification

Future Work

• A comprehensive model that includes a network of CSTR’s and PFR’s which has same RTD as the UCG has to be developed.

• RTD results should be compared with the experiments.

Page 25: CFD of Underground Coal Gasification

Thank You!

Page 26: CFD of Underground Coal Gasification

Equations solved

For n tanks in series, E(t) is