초록 ▼

A washing tower for the washing of gases containing particulates comprises a packed bed through which the gases pass upwardly and jets for spraying water into the gas as it rises within the tower. A preferably chevron-shaped coarse droplet separator is provided above the spray nozzles and the bed an

A washing tower for the washing of gases containing particulates comprises a packed bed through which the gases pass upwardly and jets for spraying water into the gas as it rises within the tower. A preferably chevron-shaped coarse droplet separator is provided above the spray nozzles and the bed and consists of upper and lower arrays of oppositely inclined plates. Further spray nozzles are provided above the coarse separator and above these spray nozzles is disposed a fine-particle separator of the baffle type through which the gas is deflected in opposite directions and with passages of smaller width than those of the coarse particle separator. The gas emerges from the upper end of the tower.

대표청구항 ▼

A washing apparatus for removing particulates or soluble components from a gas stream, comprising: an upwardly elongated tower formed with an inlet at the bottom portion thereof for admitting gas to said tower and an outlet at a top portion thereof for discharging clean gas; filling means in said to

A washing apparatus for removing particulates or soluble components from a gas stream, comprising: an upwardly elongated tower formed with an inlet at the bottom portion thereof for admitting gas to said tower and an outlet at a top portion thereof for discharging clean gas; filling means in said tower above said inlet and traversed by gas rising from said inlet; spray means in said tower above said filling means for washing the gas rising within said filling means; a coarse separator spaced above said filling means and between said spray means and said outlet for removing droplets from the gas emerging from said filling means, said coarse separator comprising a plurality of mutually parallel horizontally spaced vertical partitions defining respective flow chambers between them, each of said flow chambers being provideD with a lower row of mutually parallel spaced-apart inclined plates spanned between the partitions defining the respective chamber, and an upper row of correspondingly spaced oppositely inclined plates spanned between the partitions of the respective chamber, the lower edge of each plate of the upper row lying between upper edges of plates of the lower row; and a fine separator spaced above said coarse separator in said tower between said spray means and said outlet, said fine separator comprising a plurality of horizontally spaced mutually parallel vertical partitions defining respective flow chambers between them, and a row of geometrically similar baffle plates spanned between the partitions of each of the chambers of said fine separator, said baffle plates each having a pair of oppositely inclined portions and being spaced apart by a distance of approximately half the spacing between the plates of each row of said coarse separator, each of said baffle plates being formed with an array of chevron-shaped corrugations converging upwardly and having the vertices lying in the vertical median plane of the respective chamber of said fine separator, said corrugations of each baffle plate terminating inwardly of the partitions of the respective chamber of said fine separator to form adjacent the latter partitions respective run-off zones of each baffle plate, said separators being constructed and arranged such that the flow velocity of the gas in said fine separator is substantially 1.5 times the velocity of the gas in said coarse separator.