Process Technologies

Morphylane® - ParamaX® Suite

In extractive distillation, the addition of a selective solvent modifies the vapor pressures of the hydrocarbons in the feed in such a way that paraffinic and naphthenic components can be separated from the aromatics by distillation.

Morphylane® technology is the most cost effective solution for production of high purity benzene and toluene from C₇- aromatics fractions thanks to the recognized superior characteristics of its patented solvent (N-Formylmorpholine).

Arofining® - ParamaX® Suite

Arofining® innovative solution overcomes difficulties found with historical treatments such as Clay treatment, by implementing selective hydrogenation on the full reformate or any individual aromatics fraction depending on specific needs.

It either eliminates the need for activated clay or allows a major increase in clay lifetime. In both cases, it enhances aromatics complex operation and improves end-user revenue compared to non-selective solutions.

Dimersol™-X – C₄ dimerization

Axens’ Dimersol™-X process transforms butenes to octenes that are ultimately used in the manufacture of plasticizers via isononanol (isononyl alcohol), and diisononyl phthalate units.

AlphaHexol™ - Trimerization to 1-Hexene

AlphaHexol™ process produces high purity 1-hexene by ethylene trimerization suitable as comonomer for Linear Low-Density PolyEthylene (LLDPE) or High-Density PolyEthylene (HDPE) production.

This oligomerization process similar to AlphaButol® technology operates in the liquid phase using a soluble catalyst system.

AlphaButol® - Dimerization to 1-Butene

The AlphaButol® process is the industry’s benchmark for the production of high purity 1-butene via ethylene dimerization producing at date 32 % of butene-1 world capacity.

Using homogeneous catalysis, this technology produces the highest butene-1 purity on the market with a yield higher than 90 %.

ISO-5

ISO-5™ is Axens technology for the isomerization of n-pentenes into isopentenes. It combines efficiently with Axens etherification technology to produce TAME.

As stringent regulations divert C5 olefins away from the gasoline pool, ISO-5™ offers an attractive scheme to solve RVP and olefins problems while at the same time producing valuable ethers. Axens first reference, the first of this kind in the world as well, started up in 2002.

Selectopol™

The Selectopol™ process is a variant of the Polynaphtha™ process using the same catalyst but at lower severity:

• To convert selectively the isobutene portion of an olefinic C4 fraction to high octane, low RVP gasoline blending stock,
• or to enrich Trimethyl Pentene stream for petrochemical applications.

Selectopol™ technology is an alternative scheme to avoid or reduce MTBE production in C4 complex.

Enriched n-butenes raffinate of Selectopol™ is ideally sent to Alkylation, Methyl Ethyl Ketone (MEK), Metathesis or Dimersol-X™ process unit, without any pretreatment.

Polynaphtha™

In the Polynaphtha™ process, propylene and/or mixed butenes are oligomerized catalytically in a series of fixed bed reactors. Conversion and selectivity are controlled by reactor temperature adjustment while the heat of reaction is removed by feed effluent heat exchange and intermediate reactor cooling. The reactor section effluent is fractionated producing LPG raffinate, gasoline and middle distillate fractions such as kerosene or diesel.

The Polynaphtha™ technology is well suited for revamping existing phosphoric acid polymerization units.