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Petrochemical
Precursors
Ethylene & Propylene
Petrochemical Precursors
2
Petrochemical is a chemical compound or element recovered
or derived partially or entirely from petroleum or natural gas
and are intended for Chemical markets. Primary
petrochemicals are divided into three groups depending on
their chemical structure.
 Olefins include ethylene ,propylene and butadiene.
 Aromatics include benzene, toluene and xylenes.
 Synthesis gas is a mixture of carbon monoxide and
hydrogen used to make ammonia and methanol.
.
Olefins
Olefins are a class of hydrocarbons with a single double bond
and a chemical formula CnH2n. The two most important olefins
are ethylene and propylene,as they form the backbone of
petrochemicals market.The highly reactive double bond
makes the olefin molecule ideal for conversion to many useful
end products.
Oil refineries produce olefins by fluid catalytic
cracking of petroleum fractions.Chemical plants produce
Olefins by steam cracking of natural gas liquids like ethane
and propane.Olefins and aromatics are the building blocks for
a wide range of materials such as solvents, detergents and
adhesives.
3
Ethylene (CH2=CH2 )
4
Ethylene (ethene), the first member of the alkenes,
is a colorless gas with a sweet odor. It is slightly
soluble in water and alcohol. It is a highly active
compound that reacts easily by addition to many
chemical reagents.
Ethylene is obtained from ,Fermentation alcohol,
Refinery off-gases ,Hydrocarbon steam cracking
Physical properties-
 Mol. Wt. 28.03
 M.P. -169.4 0 C
 B.P. -103.8 0 C
Properties of Ethylene
• Unsaturated
• Non – polar molecule
• A flammable gas
• Participates in Addition reactions
(test of unsaturation)
• Polymerises to form Polyethene
• Very low BP (–104°C)
• Double bond makes it very reactive
• Catalytic oxidation of ethylene produces ethylene oxide, which
is hydrolyzed to ethylene glycol. Ethylene glycol is a
monomer for the production of synthetic fibers.
3/15/2015Footer Text 5
Synthetic chemical intermediates and
products from ethylene
3/15/2015Footer Text 6
Propylene
3/15/2015Footer Text 7
Propylene(propene) is a colourless
unsaturated gas with a weak but
unpleasant smell having the chemical
formula C3H6
Propene is a byproduct of oil refining and natural gas
processing. During oil refining ethylene, propylene and other
compounds are produced ass a result of cracking larger
hydrocarbon molecules to produce hydrocarbons more in
demand. Propene can be separated by fractional distillation
from hydrocarbon mixtures obtained from cracking and other
refining processes.
Properties of Propylene
• Propylene can be polymerized alone or copolymerized with
other monomers
• Many important chemicals are based on propylene such as
isopropanol, allyl alcohol, glycerol, and acrylonitrile
• Highly flammable
• Has higher density and B.P. than ethylene due to its greater
mass
• Lacks strongly polar bonds ,yet the molecule has a small
dipole moment (0.366D) due to its reduced symmetry
3/15/2015Footer Text 8
Synthetic chemical intermediates and
products from propylene
3/15/2015Footer Text 9
Processes in Refinery which gives Ethylene and Propylene
10
 Steam cracking of petroleum from LPG and
naphtha feedstock
 Thermal pyrolysis of ethane and propane
 Refinery off-gases
The main route for producing ethylene and
propylene ,is the steam cracking of
Hydrocarbons
Steam cracking of petroleum hydrocarbons
Steam cracking is a pyrolysis process.The cracking reactions are
principally bond breaking and a substantial amount of energy is
needed to drive the reaction towards olefin production. Cracking can
be visualized as a free radical dehydrogenation reaction, where
hydrogen is a coproduct.
11
A hydrocarbon mixture is heated in a metal tubes inside a furnace
in the presence of steam to a temperature at which hydrocarbon
molecules thermally decompose.
These reactions have a residence time of less than one second and
are endothermic
Principle behind steam cracking
12
Chemical Reaction
CxH2x+2 + H2O + O2  C2H4(4-15 %) + C3H6 + C2H6 + C2H2(7-13%) + H2(25-
30%) + CO + CO2 + CH4 + C3H8 + C4H10 + C4H8 + C4H6 +C +Heavy oil fraction
Co-products formed include acetylene, butylene, butadiene,
aromatics such as benzene ,toluene, xylene heavy oil residues.
Flow diagram of steam cracking unit
13
Process description of a steam cracking unit
The process is a high temperature thermal reforming using ethane,
propane, butane and liquid naphtha. Superheated steam is mixed with the
hydrocarbon and fed through the heated coils of a pyrolysis furnace. The C2-
C4 feed is pyrolyzed in a separate furnace because different residence time-
temperature conditions are required. The pyrolyzed gases are quenched in a
tower and then scrubbed with gas oil to remove solids and heavy
hydrocarbons before sending to compressors to boost pressure to 35atms.
The compression station may also handle refinery off-gases which can
be separated in the same system. Flash vaporization removes C1-C2 fractions
which are caustic-scrubbed to remove carbon dioxide, dried with activated
alumina, and then separated into acetylene and ethylene by a combination of
absorption, extraction and fractionation steps. Ethane is recycled for pyrolysis
and methane ,hydrogen , carbon monoxide can be further processed to obtain
synthesis gas or used as a fuel.
The liquid fraction from the flash chamber is split by fractionation
into ethylene , propylene and a few byproducts
3/15/2015Footer Text 14
Cracking conditions
3/15/2015Footer Text 15
Process design considerations
3/15/2015Footer Text 16
Considerations for feedstock
Major engineering problems
• Choice of process: Numerous process modifications are
possible in the pyrolysis of hydrocarbons. These can be done in
the Feed type ,choice of pyrolysis agent and in the choice of
pyrolysis equipment.
• Product ratio control: The product effluent composition is
controlled by steam-hydrocarbon mole ratio and residence time.
If no acetylene is desired, the light ends gas is split at the C2
level and acetylene is mildly hydrogenated to ethylene.
• Steam economy : Heat added in pyrolysis section can be
recovered in part by incorporating stack and quench boiler ,the
latter recovering heat that would otherwise be wasted in water
or oil quenching.
3/15/2015Footer Text 17
Global consumption of ethylene and
propylene
3/15/2015Footer Text 18
Thank You
3/15/2015Footer Text 19

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04 petrochemical precursor ethylene and propylene

  • 2. Petrochemical Precursors 2 Petrochemical is a chemical compound or element recovered or derived partially or entirely from petroleum or natural gas and are intended for Chemical markets. Primary petrochemicals are divided into three groups depending on their chemical structure.  Olefins include ethylene ,propylene and butadiene.  Aromatics include benzene, toluene and xylenes.  Synthesis gas is a mixture of carbon monoxide and hydrogen used to make ammonia and methanol. .
  • 3. Olefins Olefins are a class of hydrocarbons with a single double bond and a chemical formula CnH2n. The two most important olefins are ethylene and propylene,as they form the backbone of petrochemicals market.The highly reactive double bond makes the olefin molecule ideal for conversion to many useful end products. Oil refineries produce olefins by fluid catalytic cracking of petroleum fractions.Chemical plants produce Olefins by steam cracking of natural gas liquids like ethane and propane.Olefins and aromatics are the building blocks for a wide range of materials such as solvents, detergents and adhesives. 3
  • 4. Ethylene (CH2=CH2 ) 4 Ethylene (ethene), the first member of the alkenes, is a colorless gas with a sweet odor. It is slightly soluble in water and alcohol. It is a highly active compound that reacts easily by addition to many chemical reagents. Ethylene is obtained from ,Fermentation alcohol, Refinery off-gases ,Hydrocarbon steam cracking Physical properties-  Mol. Wt. 28.03  M.P. -169.4 0 C  B.P. -103.8 0 C
  • 5. Properties of Ethylene • Unsaturated • Non – polar molecule • A flammable gas • Participates in Addition reactions (test of unsaturation) • Polymerises to form Polyethene • Very low BP (–104°C) • Double bond makes it very reactive • Catalytic oxidation of ethylene produces ethylene oxide, which is hydrolyzed to ethylene glycol. Ethylene glycol is a monomer for the production of synthetic fibers. 3/15/2015Footer Text 5
  • 6. Synthetic chemical intermediates and products from ethylene 3/15/2015Footer Text 6
  • 7. Propylene 3/15/2015Footer Text 7 Propylene(propene) is a colourless unsaturated gas with a weak but unpleasant smell having the chemical formula C3H6 Propene is a byproduct of oil refining and natural gas processing. During oil refining ethylene, propylene and other compounds are produced ass a result of cracking larger hydrocarbon molecules to produce hydrocarbons more in demand. Propene can be separated by fractional distillation from hydrocarbon mixtures obtained from cracking and other refining processes.
  • 8. Properties of Propylene • Propylene can be polymerized alone or copolymerized with other monomers • Many important chemicals are based on propylene such as isopropanol, allyl alcohol, glycerol, and acrylonitrile • Highly flammable • Has higher density and B.P. than ethylene due to its greater mass • Lacks strongly polar bonds ,yet the molecule has a small dipole moment (0.366D) due to its reduced symmetry 3/15/2015Footer Text 8
  • 9. Synthetic chemical intermediates and products from propylene 3/15/2015Footer Text 9
  • 10. Processes in Refinery which gives Ethylene and Propylene 10  Steam cracking of petroleum from LPG and naphtha feedstock  Thermal pyrolysis of ethane and propane  Refinery off-gases The main route for producing ethylene and propylene ,is the steam cracking of Hydrocarbons
  • 11. Steam cracking of petroleum hydrocarbons Steam cracking is a pyrolysis process.The cracking reactions are principally bond breaking and a substantial amount of energy is needed to drive the reaction towards olefin production. Cracking can be visualized as a free radical dehydrogenation reaction, where hydrogen is a coproduct. 11 A hydrocarbon mixture is heated in a metal tubes inside a furnace in the presence of steam to a temperature at which hydrocarbon molecules thermally decompose. These reactions have a residence time of less than one second and are endothermic
  • 12. Principle behind steam cracking 12 Chemical Reaction CxH2x+2 + H2O + O2  C2H4(4-15 %) + C3H6 + C2H6 + C2H2(7-13%) + H2(25- 30%) + CO + CO2 + CH4 + C3H8 + C4H10 + C4H8 + C4H6 +C +Heavy oil fraction Co-products formed include acetylene, butylene, butadiene, aromatics such as benzene ,toluene, xylene heavy oil residues.
  • 13. Flow diagram of steam cracking unit 13
  • 14. Process description of a steam cracking unit The process is a high temperature thermal reforming using ethane, propane, butane and liquid naphtha. Superheated steam is mixed with the hydrocarbon and fed through the heated coils of a pyrolysis furnace. The C2- C4 feed is pyrolyzed in a separate furnace because different residence time- temperature conditions are required. The pyrolyzed gases are quenched in a tower and then scrubbed with gas oil to remove solids and heavy hydrocarbons before sending to compressors to boost pressure to 35atms. The compression station may also handle refinery off-gases which can be separated in the same system. Flash vaporization removes C1-C2 fractions which are caustic-scrubbed to remove carbon dioxide, dried with activated alumina, and then separated into acetylene and ethylene by a combination of absorption, extraction and fractionation steps. Ethane is recycled for pyrolysis and methane ,hydrogen , carbon monoxide can be further processed to obtain synthesis gas or used as a fuel. The liquid fraction from the flash chamber is split by fractionation into ethylene , propylene and a few byproducts 3/15/2015Footer Text 14
  • 16. Process design considerations 3/15/2015Footer Text 16 Considerations for feedstock
  • 17. Major engineering problems • Choice of process: Numerous process modifications are possible in the pyrolysis of hydrocarbons. These can be done in the Feed type ,choice of pyrolysis agent and in the choice of pyrolysis equipment. • Product ratio control: The product effluent composition is controlled by steam-hydrocarbon mole ratio and residence time. If no acetylene is desired, the light ends gas is split at the C2 level and acetylene is mildly hydrogenated to ethylene. • Steam economy : Heat added in pyrolysis section can be recovered in part by incorporating stack and quench boiler ,the latter recovering heat that would otherwise be wasted in water or oil quenching. 3/15/2015Footer Text 17
  • 18. Global consumption of ethylene and propylene 3/15/2015Footer Text 18