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4 Applied Chemistry
Helwan university
Introduction
 Synthetic fuel or synfuel is a liquid fuel obtained from
coal , natural gas , oil shale , or biomass .
 It may also refer to fuel derived from other solids such
as plastics or rubber waste.
Methods of producing synthetic
petrol
Polymerization
Fischer-Tropsch
Bergius process
Polymerization
 In this method, smaller molecules of hydrocarbons
are combined to form heavier molecule resembling
gasoline , it is of two type:
A. Thermal polymerization
B. Catalytic polymerization
Thermal polymerization
 Thermal polymerization is carried out at temperature
about 500-600 C and pressure about 70-350 Kg/cm2
Catalytic polymerization
 It is carried out at lower temperature of 150-200 C , in
low pressure and in presence of catalyst like posphoric
acid.
 The rate of reaction is increased.
 The gasoline obtained is of inproved quality and
posses high antiknock properties than the gasoline
obtained from thermal polymerization process.
Fischer-Tropsch Process
 It is indirect coal liquefaction.
 It is a set of chemical reaction that can be used to
produce fuels and chemicles from synthesis gas.
 synthesis gas is mixture of Co and H2 , which can be
derived from natural gas , coal , or biomass.
Optimum conditions:
Feed stock
water gas +
H2
Catalyst
cobalt(100
parts)
magnesia(8
parts)
thoria(5
parts)
Temperature
250 C
Pressure
5-10 atm
It involves two steps:
Production of
synthesis gas.
Hydrogenation
of synthesis gas.
1) Production of synthesis
gas
1. C + H2o [CO + H2]
(coal) (steam) ( water gas)
2. [CO + H2] + H2 [CO + 2H2]
( water gas) (synthesis gas)
The synthesis gas is fed into converter which contains catalyst
under temperature , then occurs it hydrogenation.
1) Hydrogenation of synthesis gas
1. n[CO + (2n+1)H2] Cn H2n+2 + H2o
(synthesis gas ) (Alkanes)
After produce alkanes is fed into fractional
distillation column to produce (The synthetic
petrol)
Disadvantages
1. As implemented today , it is dirty , wastes energy ,
complicated.
2. Burns almost one ton of coal for every ton converted
to liquid fuel
Bergius process
 One of the main methods of direct conversion of coal
to liquids by hydrogenation process is Bergius process.
 In this process , the finely powdered coal is completed
keen on a paste through heavy oil ang a catalyst
powder (tin or nickel oleate) is mixed with it. The
paste is pumped along with hydrogen gas into the
converter. Where the synthetic paste is heated to 400-
450 C under a pressure of 200-250 atm.
Continue……
 During this process hydrogen combines with coal to
form saturated higher hydrocarbons , which
experience additional decay at superior temperature to
acquiesce combination of lesser hydrocarbons.
 The mix is led to a condenser , where the crude oil is
attained . The crude oil then fractionated to yield
A. Gasoline B. Middle oil C. Heavy oil
Synthetic petrol
Synthetic petrol

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Synthetic petrol

  • 2. Introduction  Synthetic fuel or synfuel is a liquid fuel obtained from coal , natural gas , oil shale , or biomass .  It may also refer to fuel derived from other solids such as plastics or rubber waste.
  • 3. Methods of producing synthetic petrol Polymerization Fischer-Tropsch Bergius process
  • 4. Polymerization  In this method, smaller molecules of hydrocarbons are combined to form heavier molecule resembling gasoline , it is of two type: A. Thermal polymerization B. Catalytic polymerization
  • 5. Thermal polymerization  Thermal polymerization is carried out at temperature about 500-600 C and pressure about 70-350 Kg/cm2
  • 6. Catalytic polymerization  It is carried out at lower temperature of 150-200 C , in low pressure and in presence of catalyst like posphoric acid.  The rate of reaction is increased.  The gasoline obtained is of inproved quality and posses high antiknock properties than the gasoline obtained from thermal polymerization process.
  • 7. Fischer-Tropsch Process  It is indirect coal liquefaction.  It is a set of chemical reaction that can be used to produce fuels and chemicles from synthesis gas.  synthesis gas is mixture of Co and H2 , which can be derived from natural gas , coal , or biomass.
  • 8. Optimum conditions: Feed stock water gas + H2 Catalyst cobalt(100 parts) magnesia(8 parts) thoria(5 parts) Temperature 250 C Pressure 5-10 atm
  • 9. It involves two steps: Production of synthesis gas. Hydrogenation of synthesis gas.
  • 10. 1) Production of synthesis gas 1. C + H2o [CO + H2] (coal) (steam) ( water gas) 2. [CO + H2] + H2 [CO + 2H2] ( water gas) (synthesis gas) The synthesis gas is fed into converter which contains catalyst under temperature , then occurs it hydrogenation.
  • 11. 1) Hydrogenation of synthesis gas 1. n[CO + (2n+1)H2] Cn H2n+2 + H2o (synthesis gas ) (Alkanes) After produce alkanes is fed into fractional distillation column to produce (The synthetic petrol)
  • 12.
  • 13. Disadvantages 1. As implemented today , it is dirty , wastes energy , complicated. 2. Burns almost one ton of coal for every ton converted to liquid fuel
  • 14. Bergius process  One of the main methods of direct conversion of coal to liquids by hydrogenation process is Bergius process.  In this process , the finely powdered coal is completed keen on a paste through heavy oil ang a catalyst powder (tin or nickel oleate) is mixed with it. The paste is pumped along with hydrogen gas into the converter. Where the synthetic paste is heated to 400- 450 C under a pressure of 200-250 atm.
  • 15. Continue……  During this process hydrogen combines with coal to form saturated higher hydrocarbons , which experience additional decay at superior temperature to acquiesce combination of lesser hydrocarbons.  The mix is led to a condenser , where the crude oil is attained . The crude oil then fractionated to yield A. Gasoline B. Middle oil C. Heavy oil