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Process Technologies

Once-through C₅/C₆ isomerization

The scheme of once-through C5/C6 Isomerization is based on a permutable reactors design; that is, either reactor can be used in the lead or lag position or it can be operated independently during catalyst servicing. This insures an ultra-high on-stream service.

More than 20 C5/C6 once-through isomerization licenses have been awarded over the last 25 years
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Benfree® RD

The Benfree® RD integrates an external fixed bed hydrogenation reactor with the reformate splitter column, therefore reducing equipment and associated costs to save capital cost and plot area. The light reformate product is withdrawn as a side draw of the column for RVP control. Operating conditions are adjusted to minimize the toluene carry-over to the hydrogenation reactor thus minimizing the octane loss.

Simple integrated reactive distillation concept which ensures a high level of benzene saturation with great operation flexibility
Easy catalyst loading and change-out in a conventional fixed bed instead of proprietary catalytic structured packing
Continuous splitter operation even if the reactor is shutdown to meet market demand or fluctuations
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Benfree® C

When limiting the benzene formation in the reformer is not sufficient to meet gasoline pool specifications, Benfree® C engineering design services will provide a reliable solution to adjust the benzene saturation to requirement. The conventional option consists of a hydrogenation unit downstream of a reformate splitter to saturate the benzene contained in the light reformate stream. The unit utilizes a highly active catalyst that is operated in the liquid phase under mild conditions to minimize investment cost.

Minimize toluene carry-over in the light reformate sent to the hydrogenation reactor to maximize octane retention
Maximize overall benzene conversion by limiting the benzene content in the heavy reformate stream
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Semi-Regenerative Catalytic Reforming

Semi-Regenerative Catalytic Reforming completes Axens portfolio for lower capacities units. Axens has a long experience in conventional fixed bed reformers with over 50 references. Axens offer is related to the use of our Symphony solution of multi-promoted catalysts for semi-reg units.

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Octanizing™ and Aromizing™

The Octanizing™ and Aromizing™ technology offers unrivaled product yields, low investment and operating costs and an exceptional on-stream factor for the production of gasoline and aromatics. Axens has an extensive experience in capacity and severity with over 130 licenses awarded worldwide.

Side-by-side reactor arrangement
Highly integrated energy optimization
Continuous Catalyst Regeneration
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Oil Refining

Is there a route for post-treating gasoline with minimal octane loss?

For the post-treatment of FCC gasoline, fixed-bed HDT is by far the most trusted solution because of its low capex, its ease of operation, and its flexibility.

Written by Olivier BOISIER & Boris HESSE ·
Oil Refining

Hydrogen consumption is higher than we would like in our raw diesel hydrotreater. Can we lower it without loss of throughput?

Hydrogen consumption in a hydrotreater comes from hydrotreatment reactions but also from losses within the process.

Written by Marion Guillevic · Technologist, Axens ·
Natural Gas

Solids in the feed are causing corrosion and erosion problems in our amine system. How do we remove them effectively and economically?

In order to ensure that there are no solids in the amine system, Axens recommends an amine filtration package which filters a slipstream of the lean amine to remove solid particles. The amine filtration package also includes an activated carbon filter for hydrocarbon elimination and a polishing filter to remove any charcoal fines.

Written by Carmella Alfano & Géraldine Laborie · Technologist, Axens ·
Natural Gas Oil Refining

What steps do we need to take to keep our sour water stripper at peak performance following a shutdown?

Shutdown operations of the sour water stripper unit should maximise the removal of H2S and NH3 from water, especially for long duration shutdowns, to minimise the safety concerns and corrosion issues during maintenance. If the sulphur recovery unit is not available, the sour gas should be routed to flare, then start the shutdown by decreasing the sour water feed to the unit manually and slowly.

Written by Carmella Alfano & Guillaume Dalary ·
Oil Refining

How can we minimise gas and coke make with heavy feed to our FCC?

Catalytic systems towards better coke and/or dry gas selectivities will certainly help, especially to face contaminant metals which catalyse side reactions. If not limited by catalyst circulation, low delta coke catalysts will increase cat/oil but coke yield should stay constant.

Written by Pierre Bellet ·