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Winkler-type gasifier

A 1,000 ton/day methanol plant, using a Winkler type gasifier adapted to burn wood chips and to use the ICI process for synthesis, requires the following consumption of ingredients per ton of methanol ... [Pg.41]

Adopting 4,770 kcal/kg for the low heat value of methanol and considering the case of a Winkler type gasifier, the energy balance of the plant would be as shown in Table III ... [Pg.41]

Figures 1 and 2 show the process routes for methanol synthesis. The first one is based on a fluidized bed and includes a pressurized gasifier (Winkler type) that produces a very clean gas, practically free of tars and other impurities from wood distillation. The second route is based on a fixed bed... Figures 1 and 2 show the process routes for methanol synthesis. The first one is based on a fluidized bed and includes a pressurized gasifier (Winkler type) that produces a very clean gas, practically free of tars and other impurities from wood distillation. The second route is based on a fixed bed...
Combustion occurs over a larger range in the gasifier which is almost homogeneous in temperature at about 1,000°C. Because of the nature of the fluidised bed there is a relatively high level of unconverted carbon present in the ash. The ash and unconverted coal (char) exit the bottom of the vessel. This gasifier is represented by gasifiers of the Winkler type. [Pg.207]

Four gasification processes are currently in large-scale commercial operation the Lurgi moving-bed dry ash system, the Koppers-Totzek (GKT) entrained system, the Texaco entrained-flow system, and the Winkler fluidized-bed system. More detailed discussions of individual installations appear later in this section. Table 3-1 summarizes the total number of gasifiers of each type. [Pg.76]


See other pages where Winkler-type gasifier is mentioned: [Pg.2104]    [Pg.1861]    [Pg.2108]    [Pg.423]    [Pg.223]    [Pg.235]    [Pg.278]    [Pg.15]    [Pg.16]    [Pg.307]    [Pg.888]    [Pg.30]    [Pg.75]   
See also in sourсe #XX -- [ Pg.34 ]




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