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Treatment of H2O Stream

As an example, if one would calculate the diagram with saturated liquid water, a shift of the 1500 °C isoline occurs in contrast to the overall diagram calculated with saturated steam. The slurry gasifier points for GE and E-Gas (first stage) remain at the same position and should be situated around 1550 °C. According [Pg.295]

Of course, it is only the illustration in the ternary diagram where this deviation occurs. All calculations for slurry gasifiers were carried out applying the boundary conditions as given in Table 5.11. [Pg.296]


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H2Os

Of stream

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