FIELD: chemistry.
SUBSTANCE: method of burning hydrocarbon fuel involves passing initial fuel through several catalyst zones using a catalyst packet containing two catalystes: Pd-containing catalyst for initiating the combustion process of the fuel-air mixture and a catalyst for stable combustion of the fuel-air mixture. Burning takes place in two catalyst zones, which are distinguished by layer porosity, composition of catalysts and their activity in hydrocarbon oxidation reactions: the catalyst used in the 1st zone has layer porosity between 0.45 and 0.60 and contains PdO and/or Pd, deposited on granular aluminium oxide, modified with oxides of rare-earth elements, particularly cerium and/or lanthanum, with palladium content between 0.5 and 2.5 wt %; the catalyst used in the 2nd zone is a granular oxide catalyst with layer porosity between 0.4 and 0.53, containing active component in form of 3 to 20 wt % manganese oxide or 20 to 90 wt % manganese hexaaluminate, or an oxide catalyst, modified with PdO and/or Pd in amount of 0.1 to 2.5 wt %. Initiation of the combustion process of the fuel-air mixture, which contains 1.0 to 6.0 vol % methane, takes place on the catalyst in the 1st zone at temperature between 250 and 530°C; stable combustion of the fuel-air mixture takes place on the catalyst in the 2nd zone at input temperature between 450 and 800°C, wherein temperature of waste gases at the outlet of the catalyst packet is between 750 and 950°C. The height ratio of the 1st and 2nd catalyst zones in the packet is between 0.1/0.9 and 0.2/0.8. To control the burning of the hydrocarbon fuel, a layer of inert material is placed between the 1st and 2nd zones, where this material can be granular aluminium oxide or corundum. Height of the layer of inert material is 0.025 to 0.15 of the height of the entire packet.
EFFECT: provision for environmental safety of waste gases and stable combustion of natural gas.
17 cl
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Authors
Dates
2009-11-10—Published
2008-01-24—Filed