Page 18 - Industrial Plant 2020
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cause of CO formation, was proposed, however the   therefore minimizing shut-down time.
                             client decided not to carry on due to the plot plan   Wood created a process study to cover the analysis
                             limitation for the new equipment installation and the   and  feasibility evaluation for  the  installation of  a CO
                             shut-down  duration,  which  would  be  too  short  to   oxidation catalyst package.
                             introduce the modifications.              The study was developed according to the client’s
                                                                       requests and complying with the following requirements:
                                 The alternative option was the        •   no impact on the footprint,
                             installation of a CO Oxidation catalytic   •   minimum shut-down duration,
                                converter system on the flue gas        •   catalyst packages on three parallel flue gas ducts,

                               ducting which was discussed and            with the possibility to isolate each bed
                              agreed between the client and Wood          independently for catalyst replacement.
                                  to overcome the limitations.
                                 This solution was designed and        Catalyst vendors as BASF, Johnson Matthey, Emission
                                  provided as a full package to        Partner, UMICORE were contacted.
                              shorten the installation period during   All of them were not prepared for this type of request,
                              turnaround and therefore minimizing      as normally a CO oxidation catalyst is provided for
                                        shut-down time                 smaller (engines) or bigger (boilers, incinerators)
                                                                       systems, and not for clean and fully controllable
                             The alternative option was the  installation of a CO   combustion.
                             Oxidation catalytic converter system on the flue gas
                             ducting which was discussed and agreed between the   Nevertheless, all were strongly committed to this
                             client and Wood to overcome the limitations. This   challenge. The flue gas was proved dust free and
                             solution was designed and provided as a full package   combustion was with fuel gas only. On this basis
                             to shorten the installation period during turnaround and   catalyst system was designed to achieve (Figure 2):
                                                                       •   CO content decrease from 685 mg/Nm3 to 40
                                                                          mg/Nm3
                                                                       •   guaranteed catalyst life of 2 years, expected
                                                                          catalyst life longer than 3 years depending on the
                                                                          actual operating conditions
                                                                       •   no need of cleaning or maintenance
                                                                       •   minimized flue gas pressure drop
                                                                       Wood’s FW Fired Heaters team engineered the
                                                                       package which include catalyst support, guillotines to
                             Figure 2: conceptual catalyst system      allow single catalyst bed isolation, regulation dampers


































                             Figure 3: engineered catalyst package

            INDUSTRIAL PLANTS - May 2020
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