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 PONNALA SWATHI-B130896CH
 RAHUL CR-B130746CH
 REGHURAM V-B130245CH
CONTENTS
 Raw Materials
 Chemical Reactions
 Properties
 Flow Chart
 Process descriptions
 Engineering Problems
 Alternate Process for Productions
RAW MATERIALS (HYDRODEALKYLATION )
 Hydrodealkylation is the named process for the conversion of
toluene to benzene through reaction with hydrogen gas .
The principal raw materials for the process are obviously:
TOLUENE
HYDROGEN
 Note: The above process can be used for preparing naphtha from
alkyl naphthalenes.
CHEMICAL REACTIONS
 Toluene adds hydrogen gas to produce benzene
and methane.
2C6H5CH3 + H2 --------------> C6H6 + CH4
 Dimethyl benzenes undergo similar reactions with
2 moles of hydrogen.
C6H4(CH3)2 + 2H2-------------> C6H6+2CH4
Properties of benzene
 Molar mass : 78.11g/mole
 Appearance: It is a colourless liquid with an odour
similar to that of most gasoline compounds.
 Density: 0.8765 g/ cu.cm
 Melting point: 278.68K
 Boiling point:353.2K
 Solubility: Soluble in chloroform, alcohols and
organic solvents.
Flow chart:
PROCESS DESCRIPTION:
 Hydrodealkylation of toluene can be operated under
catalytic or thermal conditions. Catalytic process requires
milder conditions of 600-650oC and lower pressures
whereas the thermal process requires temperatures above
800oC.
 Toluene is mixed with heavier aromatics or paraffins from
the benzene fractionation column.
 The make up gas rich in hydrogen is compressed with
recycle gas and mixed with the liquid toluene stream.
 The combined feed is then preheated using heat
exchange and then into a fired preheater before being
charged into the reactor.
 The reactor effluents are cooled by heat exchange
and then by water before being sent to a separator.
 The liquid and gas components are separated here.
The gas containing methane and remaining hydrogen
is either used directly as fuel or as a source of
methane.
 The liquid is then sent to a stripping column where
residual gases are also removed.
 The gas free liquid is then sent into the fractionator
where benzene is separated out.
Engineering Problems:
 Reactor design: Catalytic processes were first utilised first
,operating at 600-650oC and pressure 35-40 atms.
Economic balances in yield include residence
time,temperature and reaction rates.Comparitive yields
were obtained at higher temperatures and pressures.
 Hydrogen problems: The use of hydrogen requires
explosion-proof plant construction and its use at high
reaction conditions need use of chrome steel to avoid
embrittlement.
Other processes
 Catalytic Reforming: Catalytic reforming involves
the dehydrogenation of naphthenes to aromatics,
or the isomerization of alkyl naphthenes and the
dehydrogenation of them.
 Toluene disproportionation: Alkylated aromatics are
trans alkylated to produce benzene and alkylated
benzenes.
 Pyrolysis gasoline distillation to remove benzene
and diolefins.
USES OF BENZENE
 Benzene is mainly used as intermediate to make
their chemicals, most important of which include
cumene, ethyl benzene and cyclohexane.
 It finds extensive use in producing precursors for
plastics, resins, rubber, pesticides, explosive
lubricant, detergents and fibres.
EXPOSURE AND HEALTH HAZARDS
• Benzene increases the risk of cancer and other illnesses, also
causing bone marrow failure ,aplastic anaemia, acute leukaemia
and related diseases in substantial amounts.
• It targets liver, kidney,lung,heart and the brain and can cause
DNA strand breaks.
 Vapours from products that contain benzene such as
glues,paints,furniture,detergents etc. can also be a source of
exposure.
 Exposure of the general population to benzene occurs while
breathing ,the major sources being tobacco smoke and
automobile service stations .
 Certain batches of soft drinks manufactured across various
parts of the world have been found to contain benzene levels
above the limits prescribed by the world health organisation.
THANK
YOU

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Benzene manufacturing

  • 1.  PONNALA SWATHI-B130896CH  RAHUL CR-B130746CH  REGHURAM V-B130245CH
  • 2. CONTENTS  Raw Materials  Chemical Reactions  Properties  Flow Chart  Process descriptions  Engineering Problems  Alternate Process for Productions
  • 3. RAW MATERIALS (HYDRODEALKYLATION )  Hydrodealkylation is the named process for the conversion of toluene to benzene through reaction with hydrogen gas . The principal raw materials for the process are obviously: TOLUENE HYDROGEN  Note: The above process can be used for preparing naphtha from alkyl naphthalenes.
  • 4. CHEMICAL REACTIONS  Toluene adds hydrogen gas to produce benzene and methane. 2C6H5CH3 + H2 --------------> C6H6 + CH4  Dimethyl benzenes undergo similar reactions with 2 moles of hydrogen. C6H4(CH3)2 + 2H2-------------> C6H6+2CH4
  • 5. Properties of benzene  Molar mass : 78.11g/mole  Appearance: It is a colourless liquid with an odour similar to that of most gasoline compounds.  Density: 0.8765 g/ cu.cm  Melting point: 278.68K  Boiling point:353.2K  Solubility: Soluble in chloroform, alcohols and organic solvents.
  • 7. PROCESS DESCRIPTION:  Hydrodealkylation of toluene can be operated under catalytic or thermal conditions. Catalytic process requires milder conditions of 600-650oC and lower pressures whereas the thermal process requires temperatures above 800oC.  Toluene is mixed with heavier aromatics or paraffins from the benzene fractionation column.  The make up gas rich in hydrogen is compressed with recycle gas and mixed with the liquid toluene stream.  The combined feed is then preheated using heat exchange and then into a fired preheater before being charged into the reactor.
  • 8.  The reactor effluents are cooled by heat exchange and then by water before being sent to a separator.  The liquid and gas components are separated here. The gas containing methane and remaining hydrogen is either used directly as fuel or as a source of methane.  The liquid is then sent to a stripping column where residual gases are also removed.  The gas free liquid is then sent into the fractionator where benzene is separated out.
  • 9. Engineering Problems:  Reactor design: Catalytic processes were first utilised first ,operating at 600-650oC and pressure 35-40 atms. Economic balances in yield include residence time,temperature and reaction rates.Comparitive yields were obtained at higher temperatures and pressures.  Hydrogen problems: The use of hydrogen requires explosion-proof plant construction and its use at high reaction conditions need use of chrome steel to avoid embrittlement.
  • 10. Other processes  Catalytic Reforming: Catalytic reforming involves the dehydrogenation of naphthenes to aromatics, or the isomerization of alkyl naphthenes and the dehydrogenation of them.  Toluene disproportionation: Alkylated aromatics are trans alkylated to produce benzene and alkylated benzenes.  Pyrolysis gasoline distillation to remove benzene and diolefins.
  • 11. USES OF BENZENE  Benzene is mainly used as intermediate to make their chemicals, most important of which include cumene, ethyl benzene and cyclohexane.  It finds extensive use in producing precursors for plastics, resins, rubber, pesticides, explosive lubricant, detergents and fibres.
  • 12. EXPOSURE AND HEALTH HAZARDS • Benzene increases the risk of cancer and other illnesses, also causing bone marrow failure ,aplastic anaemia, acute leukaemia and related diseases in substantial amounts. • It targets liver, kidney,lung,heart and the brain and can cause DNA strand breaks.
  • 13.  Vapours from products that contain benzene such as glues,paints,furniture,detergents etc. can also be a source of exposure.  Exposure of the general population to benzene occurs while breathing ,the major sources being tobacco smoke and automobile service stations .  Certain batches of soft drinks manufactured across various parts of the world have been found to contain benzene levels above the limits prescribed by the world health organisation.