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Optimum decomposition furnace operating conditions

Decomposition furnace temperatures below 950 °C give undecomposed H2S04(g) in the furnace gas. This  [Pg.53]

Temperatures above 1050 °C tend to damage the furnace structure. [Pg.53]

Furnace temperature is measured with thermocouples. It is controlled to 1000 C by adjusting fuel combustion rate. Feed forward control based on scheduled changes in spent acid composition and feed rate is employed to optimize the process (Rohm and Haas, 2003). [Pg.53]

Low O2 levels in the decomposition furnace may give H2S(g) and COS(g) in the furnace s product gas. These, in turn, may lead to cmitamination of the plant s acid product and to sulfur sublimation in downstream flues and equipment They are avoided by maintaining O2 at 2.0-2.5 volume% (Outotec, 2008). [Pg.54]

Excessive 02-in-gas levels, on the other hand, give SO3 in the decomposition furnace product gas. This SO3 is inadvertently absorbed during gas scrubbing and cooling, thereby  [Pg.54]

Decomposition furnaces are operated to efficiently decompose their spent acid into SO2, O2 and H20(g). Fig. 5.3 suggests optimum conditions for achieving this goal. They are  [Pg.52]

Low O2 levels in the decomposition furnace gas give sulfur vapor in the gas. This sulfur sublimes and plugs downstream cooling and cleaning equipment (Monsanto Enviro-Chem, 2005). It is avoided by keeping 02-in-decomposition furnace gas at 2 to [Pg.53]


See other pages where Optimum decomposition furnace operating conditions is mentioned: [Pg.52]    [Pg.52]    [Pg.52]    [Pg.53]    [Pg.52]    [Pg.52]    [Pg.52]    [Pg.53]    [Pg.19]   
See also in sourсe #XX -- [ Pg.53 ]

See also in sourсe #XX -- [ Pg.53 ]

See also in sourсe #XX -- [ Pg.53 ]




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