introducing pricat pd 608 introducing pricat pd 608 series
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Introducing PRICAT PD 608 Introducing PRICAT PD 608 series Johnson - PowerPoint PPT Presentation

Introducing PRICAT PD 608 Introducing PRICAT PD 608 series Johnson Matthey have an mature legacy in base and precious metal catalysis Over the past few years we have leveraged our expertise to develop a full range of selective


  1. Introducing PRICAT PD 608

  2. Introducing PRICAT PD 608 series Johnson Matthey have an mature legacy in • base and precious metal catalysis Over the past few years we have leveraged • our expertise to develop a full range of selective hydrogenation catalysts for olefins PRICAT TM PD 608 series developed for tail • end acetylene hydrogenation Catalyst properties optimized to give stable • performance over time, which has been proven at an industrial scale 2

  3. Reference plant operation Make-up hydrogen De-ethaniser overhead feed Pre-heater Feed-product interchanger Pd 608/1 Pd 608/1 Position Acetylene Feed 1.6 – 2.0 mol% 608/1 Pd Inter-bed Inter-bed Bed 1 exit <1 mol% coolers coolers Bed 2 exit <100 ppmv Bed 3 exit <1 ppmv To product splitter Product cooler 3

  4. Feedback on performance Cycle 1 Cycle 2 Cycle 3 Move towards more Cycle 1 run within selective operation. Forced Challenging conditions due General expectations from previous to return to conservative to continuous changes in catalyst. operation due to issues not hydrogen supply. related to the catalyst. Activity <1 ppmv performance specification achieved during steady state operation. Move towards more Catalyst operated selective operation. Forced Selectivity profile matched Selectivity conservatively. Selective to return to conservative cycle 2 despite challenging operation not targeted. operation due to issues not conditions related to the catalyst. Stable operation. Copes well with changes in feed conditions including varying Operability hydrogen sources. No green oil observed at start of run. Some green No measurable green oil Normal amount of green Green oil oil collected towards end seen. oil seen. of cycle. Catalyst was successfully regenerated at the end of the cycle using standard Regeneration procedures. Collaboration to Fortnightly optimization Technical support provided demonstrate improved Technical service correspondence to tune throughout operation. selectivity via selectivity performance. optimisation. 4

  5. Ethylene gain PRICAT PD 608/1 plant performance Ethylene gain 19% improvement Cycle 3 • Further process optimisation Cycle 2 • Selective operation 343% improvement targeted Cycle 1 • Selective operation not targeted 5

  6. Summary PRICAT PD 608 series developed from core science and advance • screening to deliver a robust formulation Catalyst has been demonstrated at a laboratory and industrial scale • Cycle on cycle improvements in ethylene gain have been realised • through close collaboration with the customer by a dedicated technical service team Second installation of PRICAT PD 608 is due to start-up in 2018 • Dedicated R&D continues to innovate to deliver market driven • solutions to meet expectations for the next generation of catalyst Find out what Johnson Matthey can do for you • Contact us at chemcat@matthey.com 6

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