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3D model                     Casing structures               Final completed assembly


          Figure 6 – Taranto plant from 3D model to operational in refinery


                             scale production of hydrogen at fuel station for   the assembly, plant operation and pre-commissioning
                             hydrogen vehicles.                       phases (see Figure 6).
                                                                      The Reactor-Syngas cooling process package is the
                                                                      core of SCT-CPO technology and was designed taking
                             Third plant with SCT-CPO                 into account the experience in engineering and
                             technology a commercial scale            construction of the two previous projects (Milazzo, Zero
                                                                      Regio) and the operating experience of the Milazzo pilot
                             demonstration plant                      plant.

                             (Taranto refinery project – 2019/2021)
                             For any innovative technology the final and most  Future Scale-up of the process
                             challenging  experience  is  the  “scale  up”  to  industrial   for higher capacities
                             maturity for commercial operation. Fores has
                             successfully accomplished this step in an integrated  and enabling design features
                             plant-type solution provided for Taranto Refinery, with a
                             production design of 10’000 Nmc/h of hydrogen.  On the basis of engineering and operating experience
                             Based on the positive experience of the syngas cooler   in three CPO plants, in the past years Fores has also
                             proposed by Fores for the pilot plant in Milazzo, the   explored the scale-up potential of the CPO process and
                             Client entrusted Fores with the development of the best   its adaption to various client’s downstream applications
                             solution for syngas cooling and its complete design   in several engineering studies:
                             both from thermal and mechanical point of view.   - a 15,000 Nm3/h unit to produce hydrogen for a 20
                             Also in this case, Fores proposed a coil-type heat   MW  hydrogen  Combined  Cycle gas turbine power
                             exchanger and carried out its complete design (from   plant for an Italian power producer;
                             conceptual to detail engineering) with the objective of   -  a 10,000  Nm3/h  unit  for  debottlenecking  a  steam
                             obtaining the best integration with the SCT-CPO   reformer in a refinery;
                             reactor, which was based on the Client’s IP.   - a 8,000 Nm3/h unit with temperature control and
                             The plant has been contracted on a LSTK basis,   integrated CO-shift heat exchanger;
                             starting from a basic engineering developed by ENI.     - a single stream 600,000 Nm3/h CPO unit for a mega-
                             The activity involved the process and detail engineering,   methanol plant for a Middle East client.
                             the complete engineering and construction of critical
                             process  package (Mixer-Reactor-syngas cooler,  see   For the last on the list, a new single stream “mixer-
                             Figure 5), module engineering and packaged unit   reactor-syngas cooler” concept for a capacity of
                             construction, as well as assistance on the site during   600.000 Nm3/h has been developed. Such large gas

            IndustrIal Plants - May 2024
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