Direct chlorination of ethylene is generally
conducted in liquid EDC in a bubble column reactor. Ethylene and
chlorine dissolve in the liquid phase and combine in a homogeneous
catalytic reaction to form EDC.
C2H4 + Cl2 C2H4Cl2
Ferric chloride (FeCl3) is an efficient
and highly selective catalyst for this reaction, and is widely
used commercially.
The direct chlorination process may be run with a slight
excess of either reactant, depending on how effluent gases are
treated. For instance, the vent stream could be sent to an oxychlorination process if ethylene is in excess.
Conversion of the limiting reactant is essentially 100%, and selectivity
to EDC is >99%. The principal byproduct is 1,1,2-trichloroethane,
which most likely forms through free-radical reactions. Consequently,
oxygen is often added to a level of about 0.5% of the chlorine
feed. This increases selectivity to EDC by inhibiting formation
of the free-radicals that lead to 1,1,2-trichloroethane.
The direct chlorination reaction is very exothermic
(”Hrxn = -180 kJ/mol EDC made) and requires heat
removal for temperature control. Operation at moderate temperatures
(50-65°C) gives lower by-product formation, but limits the
choice of heat transfer method to air or water cooling. Heat recovery
requires higher reactor temperatures. One possibility is to operate
the reactor at the boiling point of EDC, allowing the pure product
to vaporize, and then either recovering heat from the condensing
vapor, or replacing one or more EDC Purification column reboiler(s)
with the reactor itself. Another option is to run the reactor at
higher pressure to raise the boiling point. In this case, the reactor
operates without boiling, but at higher temperatures (75-200°C)
to allow heat transfer to some other part of the process. If the
EDC product is not withdrawn as a vapor, it must be treated to
remove ferric chloride, which would otherwise foul the EDC cracking furnace. This is usually achieved through
washing with water or adsorption onto a solid.
|
|