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Process Technologies

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.

4 AlphaHexol™ units have been licensed
High purity 1-hexene suitable for LLDPE and HDPE
Efficient ethylene feed use
EN CN
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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 %.

40 AlphaButol® licensed with a cumulated capacity of > 1, 000,000 t/y
High purity 1-butene suitable for LLDPE and HPDE
Process simplicity and ease of operation
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Conference
Online - CEST
4 days
Speakers
Varun Ginotra
Business Development Manager – Renewables Business Group

EUBCE 2021

EUBCE is the largest biomass conference and exhibition in the world. Each year, EUBCE brings together the greatest minds and latest advancements in biomass, with the aim of accelerating research and market uptake across the globe.

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.

Low cost means of retrofitting existing MTBE units or debottlenecking existing alkylation units
Almost complete isobutene conversion while preserving N-butenes
20 Selectopol™ and Polynaphtha™ units have been licensed by Axens

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.

Low investment
Low utilities consumption
22 Selectopol™ and Polynaphtha™ units have been licensed by Axens

Isopure™

Axens Isopure™ technology is a solution to produce high purity isobutene from C4’s olefins cuts.

This proven technology relies on a reactive distillation process in combination with hydro isomerization of 1-butene to 2-butenes. This concept eliminates the equilibrium limitations of conventional processes that convert 1-butene to 2-butene. The reactive distillation process occurs on a conventional distillation column combined with external reactors located on pump-around.-This facilitates the catalyst change-out operation and limits consequent unit downtime.

Industrially proven technology
Design conception providing maintenance advantages with external reactor configuration
Avoid the use and management of additives such as chemicals - sulfuric acid – or methanol, respectively used in conventional extraction units and MTBE cracking processes

Butene-1 Superfractionation

Axens Butene-1 Superfractionation technology can be integrated within existing C4’s cut complexes or implemented in grassroot projects (combined or not with Axens Hydrogenation technology BD Lean and/or Axens MTBE technology).

This is a cost-efficient and industrially proven technology, based on a fractionation philosophy to isolate Butene-1 out of the others butenes co-boilers with high efficiency.

Depending on the project specificities, this technology can be featured with a Heat Pump system, providing long-term savings on utility and limiting environmental impact.

Proven Technology
Offer Butene-1 product access to about any C4’s cut olefins sources
Taylored design technology

Total Hydrogenation (C₃, C₄, C₅ cuts)

Axens Total hydrogenation technologies answer the need for olefines bulk removal to produce a co-cracking recycle stream to specification.

A low residual olefins content in co-cracking stream is necessary to mitigate the negative effect of feed olefines in steam cracker furnaces.

Axens Total Hydrogenation technology typically includes a main reactor with an internal recycle. However, for more stringent needs, this technology might be configured with a finishing reactor to comply with very low olefins residual content, mainly when thriving to reach LPG product quality.

Axens total hydrogenation technologies can be configured to operate on alternative operating mode: total or selective. In addition, this technology can be revamped into selective hydrogenation, even after several year of operation, to support a product shift strategy.

References Over 65 references
Versatile technology design for Total or dual Total/Selective mode
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