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correlation with speed.                      The positive result of all tests
            In plot 1 we can see the performance of the he-  confirmed that Flowserve seal
            ating  rods.  The heating  rods  need  to  implement
            additional energy into the cavity up to a test speed “technology can be safely
            of 28.350 rpm, as the inner energy, produced by   operated at multiphase CO
                                                                                      2
            the seal due to windage, is not sufficient to keep   conditions for turbomachinery
            the cavity at 210 °C. That changes, as the seal is
            operated at trip speed of 29.768 rpm, where the
            heating rods turn off, as the inner energy of the seal   Flowserve FLS is undoubtedly a pioneer in this field
            is high enough to keep the cavity at 210 °C by the   and the Gaspac  seal was designed to meet the
                                                                   ®
            seal’s windage.                           actual sCO  requirements according to Flowserve
                                                               2
                                                      design standard and based on existing experience
            To simulate a prolonged, pressurized stop of the   in CO  pump & compressor industrial applications,
                                                          2
            compressor at ambient to cold housing tempera-  where Flowserve cumulated experiences in sCO 2
            tures, the inboard seal cavity was fully flooded with   applications for pilot projects.
            liquid CO  during static conditions. After the static   The seal shows overall stable and repeatable per-
                    2
            test sequence, the seal was started up until the li-  formance,  with  a  very  low  leakage  level  which  is
            quid phase changed into transient / supercritical-  fundamental for the Close Loop Process to mini-
            CO . Beside the seal performance, also the star-  mize emission and reducing refilling needs. At the
               2
            tup torque was measured to indicate the impact   same time, the low leakage reduces risk of ice for-
            of liquids and potential ice formation at the primary   mation on the primary-vent-side, improving seal
            vent.                                     reliability, as well minimizes seal system complexity.
                                                      The extensive DGS test campaign included seve-
            The start/up sequences were several times repea-  ral operational and transient conditions at the most
            ted. The torque development during start/up was   severe scenario for a dry gas seal, such as liquid
            stable, uncritical and comparable to the startup   phase CO  @ DGS. The positive result of all tests
                                                              2
            measurements at sCO  condition.           confirmed that Flowserve seal technology can be
                              2
                                                      safely operated at multiphase CO  conditions for
                                                                                 2
            Conclusions                               turbomachinery.
                                                      The Gaspac  seal test data available are being
                                                                ®
                                                      analyzed by FLS and are of extreme importance to
            The high demand from the emerging renewable   validate numerical calculation programs and ther-
            energy industry, utilizing sCO , is closely related to   mal models for the prediction of seal performance
                                   2
            the availability of high-end shaft sealing solutions   for high temperature turbomachinery, where the
            for the turbomachinery equipment. DGS techno-  DGS is a key element to ensure efficiency, safety
            logy development was driven in the past mainly by   and reliability for emerging renewable energy indu-
            Oil& Gas Industry – i.e. higher operating pressures -   stry.
            but it is a key partner also for the success of energy   The test highlighted the robustness and reliability
            transition process.                       of the Gaspac® seal under extreme conditions, le-
            The paper gave a brief insight regarding analytical   aving surprising scope for subsequent even more
            & design process and final performance testing of   severe tests. The seal Gaspac  nimbly supported
                                                                              ®
            a DGS for a sCO  Re-compression Closed Brayton   both temperatures of around 300°C, peripheral ve-
                         2
            Cycle (RCBC) pilot plant.                 locities in excess of 200m/s, and pressures greater
            The conducted test campaign mirrored as close as   than 200bar, but most importantly, the Gaspac
                                                                                            ®
            possible the operational conditions in the compres-  seal has been proven to withstand all these con-
            sors and provided needed information and perfor-  ditions at simultaneous ensuring an unpreceden-
            mance results to close the gap between analytical   ted and unique reliability in the market not at the
            studies and real application testing, allowing to   expense of emissions and consumption that were
            improve knowledge and experience for both Com-  have nevertheless proved predictable and further
            pressor and DGS OEMs.                     reduced thanks to the new construction design.





















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