The Basics

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The Basics

EFT has embraced a philosophy of “employ the best, develop the rest” in order to provide a solution based on “commercially proven” components that are sound, verifiable and project financeable as described herein.  Key technology components are outlined below:

Ft Basics

Production of Synthesis Gas (Syngas)

For GTL projects, EFT has negotiated an agreement with a global leader in synthesis gas production from natural gas allowing us to offer a modular version of their syngas technology on a sub-license basis to EFT licensees as part of the total GTL technology package.

For XTL projects, we can work with a client specified gasifier or recommend one for the application.  EFT can then provide the FT Synthesis and product upgrading and, in some cases, the syngas clean-up design, to be incorporated into the overall plant process design.


Syngas Clean-up

For GTL applications EFT incorporates a well established proprietary, patented clean-up step in its design to bring key contaminants down to ppb (parts per billion) levels.  This step is critical for protecting the FT catalysts and can extend their useful life significantly.


Air Separation

Methods to produce oxygen (required for syngas production) have changed significantly in the last 10 years, bringing the cost, and size, down to a range that fits a small scale GTL project well.  Cryogenic oxygen and Vacuum Pressure Swing Adsorption (VPSA) are both viable options for small scale GTL.  Multiple vendors (Praxair, Air Products, Air Liquide, Matheson) can supply the oxygen unit for purchase or provide oxygen “over the fence” for a processing fee.  EFT maintains working relationships with key suppliers in this field to support our design activities.


Advanced Fixed Bed FT Catalyst/Reactor System

The EFT Advanced Fixed Bed FT Catalyst/Reactor System is the result of over 5 years of R&D targeting the optimum integration of catalyst and reactor geometry while maintaining the simplicity and scalability of a conventional fixed bed tubular reactor.  The result is a highly cost effective design with improvements in performance that are at the high end of, or exceed, all historically demonstrated performance for conventional tubular reactors:

Methane Selectivity less than 8%
Alpha Schultz Flory Alpha greater than 0.92
Productivity 2 to 3 times more than a conventional fixed bed reactor system

Methane Selectivity – Methane selectivity refers to that portion of the FT product stream that is converted back into methane. The less methane made, the more useful products are made per unit of feedstock.  Conventional fixed bed tubular reactors tend to produce high methane selectivity (12 to 16%).  EFT has demonstrated consistent performance well below 8% selectivity over thousands of hours of runtime.

Alpha – A parameter used in FT technology to indicate the chain growth probability where a higher number approaching 1 means a higher percentage of heavy waxy product that is easily hydrocracked into the middle distillates range. The higher the alpha, the higher the potential yield of middle distillates.

Productivity – This refers to the amount of products made per unit of time per unit of reactor volume. The higher the productivity, the smaller the reactor volume and FT catalyst volume, for a given throughput.

Conventional tubular fixed bed reactors are heat transfer limited. With a target productivity significantly higher than of a conventional tubular fixed bed reactor, the new reactor design required a different approach.  To accomplish this, EFT’s catalyst and reactor development occurred in parallel and was demonstrated as an integrated unit.  Over 250 catalyst variations and several reactor configurations were tested to optimize the FT catalyst/reactor system.  This system is based on fundamental principles used in multiple commercial applications and has proven to be highly cost effective.  EFT has filed patents on the unique geometry employed in both the reactor and catalyst in this system.

EFT has accumulated over 250,000 hours of catalyst performance data.  Our database of proprietary FT catalysts, some with multiple runs of 5,000 to 25,000+ hours, has demonstrated performance that meets or exceeds our targeted objectives.  This database also demonstrates not only initial or “start of run” performance but also transient responses to upset conditions as well as rejuvenations and regenerations over the catalyst life cycle.  Validation of these procedures is an essential part of commercializing the technology.


Catalyst Regeneration

A key operating issue (and cost) with all FT catalysts is how often the catalyst must be regenerated and what conditions are required to accomplish the regeneration.  EFT has committed thousands of hours of development and testing to improve catalyst regeneration procedures.  EFT’s FT catalysts have demonstrated continuous runs of 1 year without regeneration making it possible to schedule regeneration with annual plant downtime for routine maintenance. More important, the catalyst can be regenerated “in situ” at temperatures below 500F.  Above 500F, the catalyst must be removed from the reactor for regeneration or the reactor shell must be designed for pressures in the range of 1000 PSI or higher in order to reach the desired temperature with a typical steam system common to FT reactors.  We believe the result of this effort is the lowest FT catalyst cost per barrel of product in the industry.