11.07.2015 Views

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

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

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

SHOW MORE
SHOW LESS

Create successful ePaper yourself

Turn your PDF publications into a flip-book with our unique Google optimized e-Paper software.

STUDY ON CATALYTIC ESTERIFICATION OF METHANE INOLEUM CATALYZED BY IODINEBeata Michalkiewicz, Monika JarosińskaPP-I-9Szczecin University <strong>of</strong> Technical, <strong>Institute</strong> <strong>of</strong> Chemical and Environment Engineering,ul. Pulaskiego 10, 70-322 Szczecin, Poland,E-mail: beata.michalkiewicz@ps.pl, Telephone: (+4891) 4494730, Fax: (+4891) 4494686Conventional conversions <strong>of</strong> methane into o<strong>the</strong>r useful chemical, such as methanol andhigher hydrocarbons, require <strong>the</strong> energy-intensive step <strong>of</strong> syn<strong>the</strong>sis gas formation. Recently,substantial research activity has been conducted in <strong>the</strong> area <strong>of</strong> methane conversion without <strong>the</strong>use <strong>of</strong> syn<strong>the</strong>sis gases. One <strong>of</strong> <strong>the</strong> most promising processes in this field is <strong>the</strong> oxidation <strong>of</strong>methane to methanol via methyl bisulfate using ei<strong>the</strong>r sulfuric acid or oleum. The reaction iscatalyzed by mercury [1, 2], platinum [3], palladium [4], iodine [5, 6] ions. This process hassome obvious advantages: (i) bypassing syn<strong>the</strong>sis gas formation; (ii) low reactiontemperature; (iii) high methane conversion.In present paper, we focus on <strong>the</strong> study <strong>of</strong> <strong>the</strong> methane esterification rate under differentexperimental conditions for iodine catalysts. Systematic experiments were applied to define<strong>the</strong> equation describing <strong>the</strong> reaction rate. The reaction rate depends on <strong>the</strong> concentration <strong>of</strong> <strong>the</strong>catalyst, temperature, <strong>the</strong> sulfur trioxide concentration, and <strong>the</strong> methane pressure. The processwas run in an autoclave under 2 – 7 MPa pressure, at 90 – 180 °C. We examine oleumconcentrations 0 – 25 wt% SO 3 . Bjerrum at al. [5] investigated iodine as catalysts forconversion <strong>of</strong> methane to methyl bisufate in 65 wt% oleum to optimize <strong>the</strong> reaction. It is veryuseful to use weaker oleum than Bjerrum. The focus <strong>of</strong> <strong>the</strong> publication by Periana et al. withiodine as catalyst [6] in weak oleum (2 – 3 wt% SO 3 ) was <strong>the</strong> reaction mechanism and notreaction rate.We have found that <strong>the</strong> following reactions took place:CH 4 + SO 3 + H 2 SO 4 → CH 3 OSO 3 H + SO 2 + H 2 O [1]CH 4 + 4SO 3 → CO 2 + 4SO 2 + 2H 2 O [2]H 2 O + SO 3 → H 2 SO 4 [3]The selectivity <strong>of</strong> methane oxidation to methyl bisulphate was close to 100%. The carbondioxide yield was below 1%. Practically, <strong>the</strong> only product <strong>of</strong> methane oxidation isCH 3 OSO 3 H.In <strong>the</strong> reactor a phenomenon <strong>of</strong> mass transfer with chemical reaction takes place. Thesystem <strong>of</strong> differential equations which represents <strong>the</strong> process can not be solved analytically sowe decided to find empirical equation <strong>of</strong> <strong>the</strong> ester formation.227

Hooray! Your file is uploaded and ready to be published.

Saved successfully!

Ooh no, something went wrong!