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Desulphurisation

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Desulphurisation Hemant Pandit, Ranjan agrawal Fuel Processing Fuel Processor Fuel Processing Fuel Processor The wet FGD process CaCO3(s) + SO2(g) + 2H2O + O2 ... – PowerPoint PPT presentation

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Title: Desulphurisation


1
Desulphurisation
  • Hemant Pandit, Ranjan agrawal

2
Wet Flue Gas Desulphurisation
  • The wet FGD process
  • CaCO3(s) SO2(g) 2H2O ½O2 ? CaSO4?2H2O(s)
    CO2
  • Major reactions (Kiil, 1998)
  • ? Absorption of SO2
  • ? Oxidation of HSO3- to SO42-
  • ? Limestone dissolution
  • ? Gypsum crystallisation
  • Important parameters
  • ? Desulphurisation degree
  • ? Gypsum moisture content
  • ? Gypsum impurity content (limestone etc.)

Courtesy of DONG Energy
1
3
The oxy-fuel concept
Oxy-fuel combustion ? Substitution of fuel air
with oxygen ? Flue gas recycle in order to
control temperature/convective heat transfer ?
Gas phase enriched in CO2 H2O ? Capture and
compression of CO2 Flue gas desulphurization ?
Ensuring a clean product i.e. transport and
geological storage considerations ? Wet FGD
before compression (traditional) ? As part of
the compression (research stage)
Courtesy of Vattenfall
2
4
Fuel Processing
5
Fuel Processor
6
Gasification of solid fuels
Moving bed Fluidized bed Entrained bed
Generic Types
Second generation
BGL Shell Texaco KRW
HT Winkler and many more
7
  • Partial Oxidation
  • CxHy x/2 O2 x CO y/2 H2
  • Advantages
  • Any type of hydrocarbon
  • Direct Heat transfer
  • Disadvantages
  • Low H2 production
  • Dilution of gas with N2
  • Soot formation

8
  • Desulphurisation
  • Gas phase Desulphurisation
  • ZnO H2S ZnS (s) H2O (g)
  • 2 to 3 kg ZnO sufficient for one year
    Automobile operation
  • Liquid Fuel Desulphurisation
  • Gasoline 30-40 ppm 1-2ppm Sulphur
  • For high sulphur Fuels hydro treatment
    followed by gas phase
  • Desulphurisation

Adsorption
Chemical reaction
9
Conclusions
  • Presently liquid fuels like gasoline Diesel
    which
  • contain high aromatic content and sulfur
    are not
  • very suitable for on board applications.
  • Availability of Methanol Ethanol for fuel
    uses are
  • inadequate.
  • For use of natural gas economic and
    environmental
  • benefits are to studied in detail.
  • A multi fuel Reformer needs to be developed
    (For
  • fuels with small range of C/H ratio).
  • Thrust areas for RD
  • Development of reactors/separators (Membrane)
  • Indigenous Catalyst development
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