Two stage circulating fluidized bed reactor and method of operating the reactor

In a method of operating a substantially upright fluidized bed combustion reactor having a combustion chamber and an adjacent gas-solids separator, said chamber containing combustible matter and a bed of granular material fluidized in the circulating regime by a first stream of pressurized air so as to entrain a substantial portion of said granular material, combustion product gases and uncombusted matter upwardly out of said chamber and into said gas-solids separator for separating said entrained portion of the granular material from said gases in said separator and returning the separated granular material to said combustion chamber, said gas-solids separator having a substantially cylindrical interior surface, the improvement comprising:

• creating in said separator a cyclonic flow of turbulent gases, uncombusted matter and granular material having at least one internal reverse flow zone by tangentially introducing a second stream of pressurized air into said separator through a plurality of openings in said interior surface of said separator for cyclonic combustion of the uncombusted matter contained therein, said second stream of air and the geometrical configuration of said interior surface of said separator being jointly adapted to maintain a Swirl number of at least about 0.6 and a Reynolds number of at least about 18,000 within said separator;
• combusting a minor portion of the combustible matter in said chamber and a major portion of the combustible matter in said separator by controlling the flow of said first and second streams of air into said chamber and said separator, respectively, and by controlling the flow of granular bed material and combustible matter to said chamber and said vessel;
• and
• permitting the combustion product gases generated in said chamber and said separator to exit from said separator via a cylindrically shaped exit throat substantially concentrically with, and at the top of, said separator, while retaining substantially all of said granular material and uncombusted matter within said separator.

A method of operating a circulating fluidized bed reactor, comprising:

• providing a substantially enclosed reactor containing a fluidized bed of granular material, said reactor comprising a substantially upright chamber and a substantially upright and cylindrical vessel adjacent to said chamber, the respective upper regions of said chamber and said vessel being connected via a conduit and the respective lower regions of said chamber and said vessel being operatively connected, said vessel having a cylindrically shaped exit throat aligned substantially concentrically with, and at the top of, said vessel;
• feeding matter to be reacted into said reactor;
• supplying a first stream of pressurized reaction-promoting gas to the reactor through a plurality of openings at the bottom of said chamber at a sufficient velocity to fluidize said granular material and said matter in the circulating regime for reacting a minor portion of said matter in said chamber, whereby a substantial portion of said granular bed material, reaction product gases and unreacted matter are continually entrained out of said chamber and into said vessel via said conduit;
• tangentially supplying a second stream of pressurized reaction-promoting gas into the reactor through a plurality of openings in the cylindrically shaped interior side wall of said vessel for reacting a major portion of said matter, said second stream being supplied, and said vessel being constructed and operated, so as to produce a Swirl number of at least about 0.6 and a Reynolds number of at least about 18,000 within said vessel for creating a cyclone of turbulence therein having at least one internal reverse flow zone, thereby increasing the rate of the reaction;
• permitting the reaction product gases generated in the reactor to exit from the reactor via said exit throat in said vessel, while retaining substantially all of said granular material and unreacted matter within the reactor;
• collecting the granular bed material and any reacted matter in the lower region of said vessel and returning it to the lower region of said chamber;
• and
• maintaining the desired reaction in the reactor by controlling the flow of said first and second streams of reaction-promoting gas into said chamber and said vessel, respectively, and by controlling the flow of granular bed material and matter to be reacted in said chamber and in said vessel.

A method of operating a circulating fluidized bed combustion reactor, comprising:

• providing a substantially enclosed combustion reactor comprising:
• (a) a substantially upright and cylindrical combustion chamber containing a fluidized bed of granular material fluidized in the circulating regime, (b) a first cooling chamber adjacent to said combustion chamber and having a first heat exchange surface, (c) a second cooling chamber having a second heat exchange surface, said first and second cooling chambers having a common bubbling fluidized bed in their bottom regions, and (d) a substantially upright and cylindrical cyclonic combustor vessel adjacent and operatively connected to said second cooling chamber and operatively connected to said combustion chamber, said vessel having a cylindrically shaped exit throat aligned substantially concentrically with, and at the top of, said vessel;
• permitting solids from said bubbling fluidized bed to flow into said circulating fluidized bed in said combustion chamber for controlling the temperature of the latter bed;
• feeding combustible matter into said combustion chamber;
• supplying a first stream of pressurized air to the reactor through a plurality of openings at the bottom of said combustion chamber at a sufficient velocity to fluidize said granular material and said matter in the circulating regime for combusting a minor portion of said matter in said combustion chamber, whereby a substantial portion of said granular bed material, combustion product gases and uncombusted matter are continually entrained upward and out of said chamber into said first cooling chamber;
• passing said product gases and entrained solids downward through said first cooling chamber and removing heat therefrom via said first heat exchange surface, and permitting said entrained solids to enter said bubbling fluidized bed;
• then passing said gases from said first cooling chamber to said second cooling chamber and permitting said gases to ascend through said second cooling chamber while removing heat therefrom via said second heat exchange surface;
• entraining the solids containing said uncombusted matter in the ascending gases in said second cooling chamber and passing said gases and entrained solids out of said second cooling chamber and into the upper region of said cyclonic combustor vessel;
• tangentially supplying a second stream of pressurized air into the reactor through a plurality of openings in the cylindrically shaped interior side wall of said vessel for cyclonic combustion of a major portion of the combustible matter fed to the reactor in said vessel, said second stream being supplied, and said vessel being constructed and operated, so as to produce a Swirl number of at least about 0.6 and a Reynolds number of at least about 18,000 within said vessel for creating a cyclone of turbulence therein having at least one internal reverse flow zone, thereby increasing the rate of combustion therein;
• permitting the combustion product gases generated in the reactor to exit from the reactor via said exit throat in said cyclonic combustor vessel, while retaining substantially all of said granular material and uncombusted matter within the reactor;
• collecting the granular bed material and any uncombusted matter in the lower region of said cyclonic combustor vessel and returning it to said combustion chamber;
• and
• controlling the combustion process in the reactor by controlling the flow of said first and second streams of air into said combustion chamber and said cyclonic combustor vessel, respectively, and by controlling the flow of granular bed material and matter to be combusted in said combustion chamber, said first and second cooling chambers, and said vessel.

A circulating fluidized bed combustion reactor, comprising:

• (a) a substantially enclosed combustion reactor for containing a fluidized bed of granular material, said reactor comprising a substantially upright combustion chamber and a substantially upright and cylindrical cyclonic combustor vessel adjacent to said chamber, the respective upper regions of said chamber and said vessel being connected via a conduit and the respective lower regions of said chamber and said vessel being operatively connected;
• (b) means for feeding combustible matter into said combustion chamber;
• (c) means for supplying a first stream of pressurized air to the reactor through a plurality of openings at the bottom of said combustion chamber at a sufficient velocity to fluidize said granular material and said matter in the circulating regime for combusting a minor portion of said matter in said chamber, whereby a substantial portion of said granular bed material, combustion product gases and uncombusted matter are adapted to be continually entrained out of said chamber and into said cyclonic combustor vessel via said conduit;
• (d) means for tangentially supplying a second stream of pressurized air into the reactor through a plurality of openings in the cylindrically shaped interior side wall of said vessel for cyclonic combustion of a major portion of the combustible matter in said vessel, said vessel being constructed for producing a Swirl number of at least about 0.6 and a Reynolds number of at least about 18,000 within said vessel for creating a cyclone of turbulence therein having at least one internal reverse flow zone, thereby increasing the rate of combustion therein;
• (e) a cylindrically shaped exit throat aligned substantially concentrically with, and at the top of said vessel for permitting the combustion product gases generated in the reactor to exit from the reactor, while retaining substantially most of said granular material and uncombusted matter within the reactor;
• and
• (f) means for collecting the granular bed material and any uncombusted matter in the lower region of said cyclonic combustor vessel and returning it to the lower region of said combustion chamber.

A circulating fluidized bed reactor, comprising:

• (a) a substantially enclosed reactor containing a fluidized bed of granular material, said reactor comprising a substantially upright chamber and a substantially upright and cylindrical vessel adjacent to said chamber, the respective upper regions of said chamber and said vessel being connected via a conduit and the respective lower regions of said chamber and said vessel being operatively connected;
• (b) means for feeding matter to be reacted into said reactor;
• (c) means for supplying a first stream of pressurized reaction-promoting gas to the reactor through a plurality of openings at the bottom of said chamber at a sufficient velocity to fluidize said granular material and said matter in the circulating regime for reacting a minor portion of said matter in said chamber, whereby a substantial portion of said granular bed material, reaction product gases and unreacted matter are continually entrained out of said chamber and into said vessel via said conduit;
• (d) means for tangentially supplying a second stream of pressurized reaction-promoting gas into the reactor through a plurality of openings in the cylindrically shaped interior side wall of said vessel for reacting a major portion of said matter, said second stream being supplied, and said vessel being constructed and operated, so as to produce a Swirl number of at least about 0.6 and a Reynolds number of at least about 18,000 within said vessel for creating a cyclone of turbulence therein having at least one internal reverse flow zone, thereby increasing the rate of the reaction;
• (e) a cylindrically shaped exit throat aligned substantially concentrically with, and at the top of said vessel for permitting the reaction product gases generated in the reactor to exit from the reactor, while retaining substantially all of said granular material and unreacted matter within the reactor;
• and
• (f) means for collecting the granular bed material and any unreacted matter in the lower region of said vessel and returning it to the lower region of said chamber.

A substantially enclosed circulating fluidized bed combustion reactor, comprising:

• a substantially upright and cylindrical combustion chamber containing a fluidized bed of granular material fluidized in the circulating regime;
• a substantially upright first cooling chamber adjacent to said combustion chamber and having a first heat exchange surface;
• a substantially upright second cooling chamber adjacent to said first cooling chamber and having a second heat exchange surface, said first and second cooling chambers having a common bubbling fluidized bed in their bottom regions;
• a substantially upright and cylindrical cyclonic combustor vessel adjacent and operatively connected to said second cooling chamber and operatively connected to said combustion chamber, said vessel having a cylindrically shaped exit throat aligned substantially concentrically with, and at the top of, said vessel for permitting the combustion product gases to exit from the reactor, the respective upper regions of said combustion chamber and said first cooling chamber being connected via a conduit and the respective lower regions of said combustion chamber and said first cooling chamber being in solids communication, the respective bottom regions of said first cooling chamber and said second cooling chamber being in open solids and gas communication, and the respective upper regions of said second cooling chamber and said cyclonic combustor vessel being connected via a port;
• means for permitting solids from said bubbling fluidized bed to flow into said circulating fluidized bed in said combustion chamber for controlling the temperature of the latter bed;
• means for feeding combustible matter into said combustion chamber;
• means for supplying a first stream of pressurized air to the reactor through a plurality of openings at the bottom of said combustion chamber at a sufficient velocity to fluidize said granular material and said matter in the circulating regime for combusting a minor portion of said matter in said combustion chamber, for continually entraining a substantial portion of said granular bed material, combustion product gases and uncombusted matter upward and out of said chamber and into said first cooling chamber via said conduit;
• means for entraining the solids containing said uncombusted matter in the ascending gases in said second cooling chamber and passing said gases and entrained solids out of said second cooling chamber and into the upper region of said cyclonic combustor vessel via said port;
• means for tangentially supplying a second stream of pressurized air into the reactor through a plurality of openings in the cylindrically shaped interior side wall of said vessel for cyclonic combustion of a major portion of the combustible matter fed to the reactor in said vessel, said vessel being adapted for producing a Swirl number of at least about 0.6 and a Reynolds number of at least about 18,000 within said vessel for creating a cyclone of turbulence therein having at least one internal reverse flow zone, for increasing the rate of combustion therein;
• means for collecting the granular bed material and any uncombusted matter in the lower region of said cyclonic combustor vessel and returning it to said combustion chamber;
• and
• means for controlling the combustion process in the reactor by controlling the flow of said first and second streams of air into said combustion chamber and said cyclonic combustor vessel, respectively, and by controlling the flow of granular bed material and matter to be combusted in said combustion chamber, said first and second cooling chambers, and said vessel.