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.

PP-II-12INITIAL CONDITIONS OF NON-CATALYTIC PARTIAL METHANEOXIDATION PROCESS IN ADIABATIC REACTORAnasov A.S.Moscow State Academy <strong>of</strong> Fine Chemical Technologies named by M.V. Lomonosov, MoscowThere are some factors, which have an influence on kinetics conditions for hightemperaturemethane conversion. One <strong>of</strong> those is spontaneous combustion characterized byinduction period, which depends <strong>of</strong> process pressure and temperature <strong>of</strong> reagents. Noncatalyticpartial methane oxidation process is carried out in millisecond residence time. In thatcase conversion goes by in adiabatic conditions, and process temperature depends <strong>of</strong> reagentsinitial temperature and adiabatic heating <strong>of</strong> mixture. Different data <strong>of</strong> induction perioddependencies is given in literature. In [1] suggested carrying out <strong>the</strong> process with initialtemperature equal 400°С at pressure 1 MPa. In [2] process was investigated at pressure3 MPa, initial temperature <strong>of</strong> methane equal 350-450°С and initial temperature <strong>of</strong> O 2 equal120°C. Besides, <strong>the</strong>re are some sources [3,4] suggested heating <strong>of</strong> reagents mixture up to500°C. To predict <strong>of</strong> spontaneous combustion it is necessary to create conditions withresidence time extremely less than induction period. The process parameters dependence <strong>of</strong>reagents initial temperature was calculated in research work for optimal reagents ratio andpressure 5.0 MPa. Reported that rise <strong>of</strong> initial temperature provokes increase <strong>of</strong> adiabaticheating temperature, increase <strong>of</strong> CO content, decrease <strong>of</strong> CO 2 content and H 2 /CO ratio.Calculated optimal value <strong>of</strong> initial temperature equals 227°С, adiabatic heating temperatureequals 1313°С, СО 2 content is 4.8 % vol.References:1. Anisopyan А.А., Volod’ko N.P. Mechanism <strong>of</strong> methane conversion, 1962, V. 145, #. 1, P. 140- 143.2. Bodrov I.М., Apelbaum L.O., Kinetics <strong>of</strong> carbon dioxide methane conversion, Kinetics & catalysis, 1967,V. 8, #. 4, P. 379 - 384.3. Proc. Roy. Soc., 1936 A, v. 154, 95.4. J. Chem. Soc., 1937, 436.293

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

Saved successfully!

Ooh no, something went wrong!