Nitrogen oxides and sulfur oxides removal utilizing transport line adsorber

Claim 1

Process for utilizing cooled regenerated sorbent particles to substantially remove nitrogen oxides and sulfur oxides from pressurized flue gas, comprising the steps of: providing sorbent particles suitable for adsorbing nitrogen oxides and sulfur oxides from said flue gas and providing said sorbent particles of a size in the range of about 70 to about 140 mesh; transporting said sorbent particles in a fluidized state through a transport line adsorber utilizing said pressurized flue gas to cause said sorbent particles to substantially adsorb said nitrogen oxides and said sulfur oxides from said flue gas while said sorbent particles are being transported through said transport line adsorber by said pressurized flue gas, upon said sorbent particles adsorbing said nitrogen oxides and said sulfur oxides said sorbent particles becoming saturated sorbent particles; separating said saturated sorbent particles from said flue gas to provide a stream of substantially nitrogen oxide and sulfur oxide free flue gas; providing a source of heated gas; passing said saturated sorbent particles through a plurality of interconnected cyclones utilizing said heated gas and gravity to heat said sorbent particles to remove therefrom said nitrogen oxides and to separate said sorbent and remove nitrogen oxides and to produce an off gas stream of heated gas carrying away said nitrogen oxides; contacting said heated sorbent with a regenerant gas to substantially remove said sulfur oxides from said sorbent particles and to produce heated regenerated sorbent and an off gas stream of regenerant gas carrying away said sulfur oxides removed from said heated regenerated sorbent; providing a cooling gas; passing said heated regenerated sorbent through a second plurality of interconnected cyclones utilizing said cooling gas and gravity to cool said sorbent particles and to separate said sorbent particles from said cooling gas to produce cooled regenerated sorbent; and returning said cooled regenerated sorbent to said transport line adsorber to repeat said steps for removing said nitrogen oxides and said sulfur oxides from said pressurized flue gas.