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

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Laboratory experimentsPP-III-22Studies were carried out on <strong>the</strong> influence <strong>of</strong> methanol concentration and temperature <strong>of</strong><strong>the</strong> gas flow entering <strong>the</strong> adiabatic reactor on <strong>the</strong> operation efficiency <strong>of</strong> <strong>the</strong> adiabatic layer ata space velocity <strong>of</strong> <strong>the</strong> gas flow <strong>of</strong> 6000, 8000, 14000 and 24000 h –1 . Analyzing <strong>the</strong> resultspresented we can conclude that <strong>the</strong> influence <strong>of</strong> <strong>the</strong> temperature, methanol concentration andspace velocity <strong>of</strong> <strong>the</strong> feed gas entering <strong>the</strong> adiabatic layer on <strong>the</strong> total methanol oxidation andselectivity <strong>of</strong> <strong>the</strong> process is complex. Methanol concentration and space velocity are <strong>the</strong> mostimportant factors. Their increase leads to rapid decrease <strong>of</strong> <strong>the</strong> borders <strong>of</strong> applicability <strong>of</strong> <strong>the</strong>adiabatic layer. Temperature influence is limited by <strong>the</strong> operating conditions <strong>of</strong> <strong>the</strong> mainreactor. At low inlet temperatures <strong>the</strong> limiting factor is methanol conversion, while at highertemperatures <strong>the</strong> selectivity is more important.Industrial experimentA fifteen months’ industrial experiment was carried out. The industrial installationmonitored consists <strong>of</strong> two pseudo-iso<strong>the</strong>rmal reactors. An adiabatic layer with a thickness <strong>of</strong>50 – 60 mm was located under <strong>the</strong> reactors.Mössbauer spectrometry, XRD and chemical analysis were used to characterize fresh andpost reaction iron molybdate catalyst. Catalytic measurements were performed too. Nodifferences were found between sample <strong>of</strong> fresh catalyst and samples discharged from <strong>the</strong>adiabatic layer.Conclusions1. Using an adiabatic layer under <strong>the</strong> main reactor leads in all cases to a loss <strong>of</strong>formaldehyde due to its secondary oxidation to CO. Carefully controlling <strong>the</strong> processparameters allows full compensation <strong>of</strong> <strong>the</strong>se losses by <strong>the</strong> oxidation <strong>of</strong> <strong>the</strong> methanolentering from <strong>the</strong> main reactor and <strong>the</strong> secondary oxidation <strong>of</strong> DME, mainly t<strong>of</strong>ormaldehyde.2. The results from <strong>the</strong> Mössbauer spectroscopy, XRD and <strong>the</strong> chemical analyses reveal noirreversible change in <strong>the</strong> chemical and phase content <strong>of</strong> <strong>the</strong> catalyst. The catalyticproperties <strong>of</strong> <strong>the</strong> catalyst used in <strong>the</strong> adiabatic layer remain virtually unchanged.AcknowledgementThis work is supported by Bulgarian Ministry <strong>of</strong> Education, Project VU- X-305/07.References1. Ana Paula Vieira Soares, Manuel Farinha Portela, Alain Kiennemann, Catal. Rev. 47 (2004) 125.2. G. Sioli, EP 1 166 864 A1, (2002).3. K. Ivanov, BG patent No 60779 B1 (1993).345

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