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Boreskov Institute of Catalysis of the Siberian Branch of Russian ...

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PP-V-11reactor we can see that its concentration increases after 4 hours <strong>of</strong> reaction at WHSV > 4 h –1which means that <strong>the</strong> catalysts loses selectivity in its oligomerization reaction leading toC 4 -hydrocarbons and liquid products.Water addition to ethanol flow decreases <strong>the</strong> amount <strong>of</strong> liquid hydrocarbons formedduring ethanol conversion on ZnO/FeO x /HZSM-5. The conversion <strong>of</strong> ethanol also decreasesto 90% at 1:5 ethanol-water (e/w) conversion with <strong>the</strong> increase <strong>of</strong> diethyl e<strong>the</strong>r concentration.At ratios lover than 1:4 e/w diethyl e<strong>the</strong>r formation was also observed consuming up to 10%<strong>of</strong> ethanol. The rise <strong>of</strong> ethylene concentration within 4 hours <strong>of</strong> reaction has been found withwater concentrations higher than 25%. High concentration <strong>of</strong> C 4 products means thatoligomerization <strong>of</strong> ethylene ei<strong>the</strong>r stops at this stage or leads to C 6 -species which aretransformed to <strong>the</strong> mixture <strong>of</strong> C 2 , C 3 and C 4 via cracking routes.In our opinion <strong>the</strong> main deactivation role <strong>of</strong> water in this zeolite catalyst is blocking <strong>of</strong>activation site for oligomerization and aromatics production. The high concentration <strong>of</strong> watermolecules inside <strong>the</strong> pores <strong>of</strong> zeolite lowers <strong>the</strong> acidity <strong>of</strong> <strong>the</strong> catalyst and moves adsorbedethylene species from active centers back to gaseous phase before <strong>the</strong>ir oligomerization. Inproving this conception it is necessary to mention that after short activation <strong>of</strong> <strong>the</strong> catalyst(1hr) in air stream, its properties regenerate almost completely.But if we are concerned with optimizing yields <strong>of</strong> C 3 -C 4 or ethylene instead <strong>of</strong> liquidproducts we can conclude that water addition to ethanol plays an important role in changingcatalyst selectivity without altering <strong>the</strong> catalyst and technological equipement.Table 2. The influence <strong>of</strong> water on product composition <strong>of</strong> ethanol conversion onZnO/FeO x /HZSM-5 catalyst (T = 350 °C, P = 1 atm)WHSVethanol,h –1WHSVwater,h –1LiquidHC, %C 2 (1) ,% massC 2 (2) ,% massC 3 (1) ,% massC 3 (2) ,% massC 4 (1) ,% massC 4 (2) ,% mass2 2 2 27 44 21 16 50 352 4 0 44 47 15 15 35 332 6 0 45 60 10 8 18 122 10 0 50 70 22 10 22 104 2 10 25 27 19 17 51 496 2 5 20 50 20 11 55 331) after 1 hour <strong>of</strong> reaction2) after 4 hours <strong>of</strong> reaction478

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