Rotary bottom ash regeneration system
View Patent ↗A rotary bottom ash regenerating (RBAR) system [ 100 ] comprises a cylindrical body that receives ash [ 17 ] containing reactant particles [ 10 ] that are partially reacted limestone compounds having unreacted cores [ 13 ] from a furnace. Sensors [ 140 ] sense physical parameters within the cylindrical body [ 110 ]. A controller [ 170 ] receives the output of the sensors [ 140 ] and information indicating the amount of unreacted core [ 13 ] and causes a fluid actuator [ 135 ] to spray a proper amount of regeneration fluid regulator [ 135 ] from a plurality of spray nozzles [ 131 ] to different locations within the cylindrical body [ 110 ] to regulate the temperature and to cause the reactant particles [ 10 ] to have a require content of regeneration fluid. This causes the reactant particles [ 10 ] to be regenerated and reused. This results in a lower limestone costs and less overheating of ash handling systems.
1. A method of processing bottom ash from a circulating fluidized bed furnace having reactant particles, each reactant particle having a partially reacted outer capsule and an unreacted internal core, comprising the steps of:
a) providing said bottom ash into a rotating cylindrical body having a plurality of nozzles for spraying a regeneration fluid along a length of the cylindrical body;
b) sensing physical conditions inside of the cylindrical body;
c) receiving an indication of the mass of the unreacted internal core within the cylindrical body;
d) calculating from the sensed physical conditions and the mass of the unreacted internal core an amount of regeneration fluid to be sprayed to cause the reactant particles to have a regeneration fluid concentration within a ‘required content’ range, wherein the required content range is 5-25% of the stoichiometric amount of regeneration fluid required to totally react all of the unreacted internal cores; and
e) spraying the calculated amount of regeneration fluid onto the bottom ash from the plurality of nozzles within the cylindrical body causing the reacted outer capsules of the reactant particles to open, exposing the unreacted internal core, thereby reactivating the reactant particles.
2. The method of claim 1 , wherein the step of sensing physical conditions comprises the step of:
sensing physical conditions at each nozzle along an inside of the cylindrical body;
the step of calculating comprises the step of:
calculating from the sensed physical conditions and the mass of the unreacted core, an amount of regeneration fluid to be sprayed from each nozzle to cause the reactant particles to have a regeneration fluid concentration within an required content range; and
the step of spraying comprises the step of:
spraying from each of the plurality of nozzles within the cylindrical body, the amount of regeneration fluid calculated for the respective nozzle onto the bottom ash to cause the reactant particles to have a regeneration fluid concentration in the required content range causing the capsules of the reactant particles to open exposing the unreacted internal core, reactivating the reactant particles.
3. The method of claim 1 , wherein the regeneration fluid is water.
4. The method of claim 1 , wherein the regeneration fluid is steam and an aqueous base.
5. The method of claim 1 , wherein the regeneration fluid is an aqueous solution of NaOH having a concentration of less than 1.0 N.
6. The method of claim 5 , wherein the regeneration fluid further comprises steam.
7. The method of claim 1 , wherein the step of spraying the calculated amount of regeneration fluid begins at a location within the cylindrical body having a temperature of less than 700 degrees Fahrenheit (361 degrees Celsius) being a temperature that effective hydration can proceed.
8. The method of claim 1 , wherein the cylindrical body has an inner wall with spiral fins protruding into the cylindrical body to facilitate physical breaking and comminution of reactant particles and to move bottom ash away from an inlet and out of an outlet.
9. A method of processing bottom ash having SO X reactant particles from a circulating fluidized bed furnace comprising the steps of:
providing said bottom ash into a rotating cylindrical body;
spraying regeneration fluid into a first region of the cylindrical body to cool the bottom ash;
spraying an amount of regeneration fluid onto the bottom ash in a second region of the cylindrical body to provide a required content of regeneration fluid to the SO X reactant particles, the required content being in the range of 5-25% of the stoichiometric amount of regeneration fluid required to totally expose all of the unreacted material within the SO X reactant particles.