The
maleic anhydride process offered by CONSER is a gas phase catalytic
oxidation process using normal butane as feedstock. Thanks to an advanced
reaction system integrated with a patented process of recovery and purification,
the technology can be regarded as highly advanced and modern.
The technology of reaction has been substantially improved resulting
in better yields and high productivity.
The recovery and purification system employs a readily available solvent
and adopts unique features which result in high yield of recovery, low
energy requirements, no regular shutdown and clean-outs, minimum environmental
impact and high and consistent quality of the product.
The process is proven in units in production totaling more than 300.000
T/Y of capacity.
The CONSER/PANTOCHIM
process consists of the following main steps:
Reaction
Maleic anhydride recovery and
purification
Off gas disposal
Reaction
The chemical equation for the main reaction in the catalytic oxidation
of n-butane to maleic anhydride is as follows:
CH3-CH2-CH2-CH3
+ 3.5 O2 -----> C4H2O3
+ 4 H2O
The main side reactions are the oxidation of n-butane to carbon dioxide,
carbon monoxide and water, according to the following equations:
CH3-CH2-CH2-CH3
+ 4.5 O2 ----> 4 CO + 5 H2O
CH3-CH2-CH2-CH3
+ 6.5 O2 ----> 4 CO2
+ 5 H2O
The reactor is of the fixed bed type and can be designed for optimum
conditions of conversion, selectivity and productivity.
Maleic anhydride recovery and purification
The maleic anhydride contained in the reactor off-gases is recovered
by selective absorption in a readily available organic solvent.
Crude maleic anhydride is recovered from the solvent in a stripper.
The crude product is further purified in a proprietary continuous distillation
system.
A portion of the recycled solvent is treated in a simple solvent purification
system where high boiling impurities are removed.
Off gas disposal
After the removal of maleic anhydride, the off gases of reaction may
be sent to an incinerator or to other disposal systems.
A fraction of the off gases may be recycled to the reactor in order
to improve the overall yield of conversion of butane.