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Table 2 – Summary of Study Cases Data used within the R&D Research Program by Saipem

            neering disciplines involved in pipeline design, to
            develop recommendations and guidelines or pro-
            cedures and fit for purpose design tools, to con-
            solidate a network of suppliers ready for the new
            scenarios, to elaborate and conduct experimental
            tests for the qualification of Saipem offshore pipe-
            line systems for the new transport conditions and
            scenarios.

            Know your partners:
            Hydrogen and CO
                                  2
            The two fluids have some peculiar properties quite
            relevant to pipeline transport (Picture 4).

            They are both gases at standard conditions, ho-
            wever CO  in the typical transport conditions of a
                    2
            gas pipeline, can be very close to a phase chan-
            ge from gas to liquid or to a supercritical state
            depending on the selected operating pressure   Picture 4 – Hydrogen and CO  Transport Scenario and Key Properties Highlights
                                                                          2
            and temperature. This behaviour is magnified if
            the CO  includes impurities because it behaves
                  2
            like a mixture. Picture 5 groups and directly com-
            pares in one graph the phase envelopes for pure
            methane, a typical natural gas composition, pure
            CO  and some CO  mixtures making it clear how
               2
                           2
            CO  liquid, supercritical or 2-phases protrude in
               2
            the typical transport region for gas pipelines. It
            is to be noted that exceeding the critical point
            CO  has the density of a liquid and the viscosity
               2
            of a gas which is an advantage from a transport
            point of view.
                 Saipem Offshore Engineering
                 Team promoted first and then
            “joined the JIP H2Pipe by DNV             Picture 5 – CO  phase diagram (pure and with impurities) vs. pure methane and natural gas
                                                                2
                 to write a Guideline on design,      phase diagram (from DNV-RP-F-104, 2021)
                 construction and operation
                 of hydrogen pipelines that           If CO  is 1.5 heavier than air, Hydrogen is much
                                                          2
                 supplement the standard DNV-         lighter. It has the highest energy content per unit
                                                      mass, so, much more than the most common
                 ST-F101 on submarine pipeline        fuels, however it has a very low energy density
                 systems                              which is a drawback as it is transported via pipeli-
                                                      ne in gaseous form, even if compressed. Another



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