Method and device for producing synthesis by partial oxidation of slurries made from fuels containing ash with partial quenching and waste heat recovery
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[0022] 320 tons / hour of bituminous coal with a composition of
C71.5 wt. % H4.2 wt. %O9.1 wt. %N0.7 wt. %S1.5 wt. %Cl0.03 wt. %,
an ash content of 11.5 wt. %, and a moisture content of 7.8 wt. %, is to be gasified at a pressure of 40 bar. The calorific value of the coal is 25,600 kJ / kg. The gasification takes place at 1,450° C. 245,000 m3 (standard) / h of oxygen is needed for the gasification. The coal is first fed to a state-of-the-art grinder in which it is pulverized to a grain size range between 0 and 200 μm, and is then mixed in a special system 1 according to FIG. 1 with water with added surfactants to make a stable coal dust in water suspension, the so-called slurry. The solids concentration in this slurry is 63 wt. %, and the amount of slurry is 485 tons / hour. The slurry is brought to the desired gasification pressure of 100 bar by means of a pump suitable for pumping solid-liquid suspensions, and is fed to the burner of the gasification reactor 2 of FIG. 1 through the suppl...
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