# US 5,347,953 A · Fluidized bed combustion method utilizing fine and coarse sorbent feed > Agents: this data is available as JSON from the patentgrep API and MCP server — see https://patentgrep.com/llms.txt - Number: US 5,347,953 A - Document ID: US5347953A - Status: Granted - Kind: A - Application number: 07/709,243 - Filed: 1991-06-03 - Granted: 1994-09-20 - Earliest claimed: 1991-06-03 - Assignees: Foster Wheeler Energy Corporation - Inventors: Igbal F. Adbulally - Web page: https://patentgrep.com/patent/US5347953A ## CPC - F23C 10/10: the separation apparatus being located outside the combustion chamber - F22B 31/0084: {with recirculation of separated solids or with cooling of the bed particles outside the combustion bed} - F23C 2206/101: Entrained or fast fluidised bed - F23C 2206/103: Cooling recirculating particles - F23C: METHODS OR APPARATUS FOR COMBUSTION USING FLUID FUEL OR SOLID FUEL SUSPENDED IN {A CARRIER GAS OR} AIR (burners F23D) - F22B: METHODS OF STEAM GENERATION; STEAM BOILERS ## Abstract A fluidized bed combustion method utilizing fine and coarse sorbent feed to control the temperature of a cooling fluid such as water or steam circulating through a fluid flow circuit of a fluidized bed combustor. Fuel particles, such as coal, along with relatively fine and relatively coarse sorbent material, such as limestone, are fed into the furnace section of a fluidized bed reactor. The fuel is combusted, and a fluidizing gas such as air is introduced into the furnace section. Flue gases and entrained material pass from the furnace section, and the entrained material is separated from the flue gases. The separated entrained material passes to a recycle heat exchange section and is cooled before being passed to the furnace section. The recycle heat exchange section is provided with heat exchange surfaces which form part of a fluid flow circuit to transfer heat from the separated entrained material to a cooling fluid such as water or steam which is circulating through the circuit. The ratio of fine to coarse sorbent feed is controlled to control the heat transfer from the separated entrained material in the recycle heat exchange section to the cooling fluid, thereby controlling the temperature of the cooling fluid and enabling the temperature of the cooling fluid to be held constant over a range of fluidized bed reactor loads. ## Claims ### Claim 1 A fluidized bed combustion method comprising: (a) forming a furnace section and a recycle heat exchange section; (b) introducing fuel particles into said furnace section; (c) combusting said fuel particles to form gaseous and solid products of combustion; (d) introducing relatively fine and relatively coarse sorbent material into said furnace section at a ratio of said fine to said coarse sorbent material; (e) fluidizing said furnace section with a fluidizing gas so that said fluidizing gas combines with said gaseous products of combustion to form flue gases which entrain portions of said fuel particles, said solid products of combustion, and said fine and said coarse sorbent materials; (f) passing said flue gases and said entrained material from said furnace section; (g) separating said entrained material from said flue gases; (h) passing said separated entrained material to said recycle heat exchange section to cool said separated entrained material; (i) passing said cooled entrained material to said furnace section; (j) establishing a fluid flow circuit to transfer heat from said separated entrained material in said recycle heat exchange section to a fluid passing through said circuit, thereby heating said fluid; and (k) varying said heat transfer to said fluid; (l) adjusting said ratio of fine to coarse sorbent feed in response to said variation in said heat transfer to offset said variation in said heat transfer. ### Claim 2 (depends on 1) The method of claim 1 wherein said ratio of fine to coarse sorbent feed is adjusted by increasing said ratio of fine to coarse sorbent feed in response to a decrease in said heat transfer to said fluid to offset said decrease in said heat transfer. ### Claim 3 (depends on 1) The method of claim 1 wherein said ratio of fine to coarse sorbent feed is adjusted by decreasing said ratio of fine to coarse sorbent feed in response to an increase in said heat transfer to said fluid to offset said increase in said heat transfer. ### Claim 4 (depends on 3) The method of claim 3 further comprising removing heat from said fluid to further offset said increase in said heat transfer to said fluid. ### Claim 5 (depends on 4) The method of claim 4 further comprising forming a heat recovery section, and passing said separated flue gases to said heat recovery section. ### Claim 6 (depends on 1) The method of claim 1 further comprising removing heat from said fluid to control the temperature of said fluid. ### Claim 7 (depends on 1) The method of claim 1 further comprising forming a heat recovery section, and passing said separated flue gases to said heat recovery section. ### Claim 8 (depends on 1) The method of claim 1 wherein said step of varying said heat transfer to said fluid is in response to changes in load demands. ### Claim 9 A method for controlling a steam generating system comprising: (a) forming a furnace section and a recycle heat exchange section; (b) introducing fuel particles into said furnace section; (c) combusting said fuel particles to form gaseous and solid products of combustion; (d) introducing relatively fine and relatively coarse sorbent material into said furnace section at a ratio of said fine to said coarse sorbent material; (e) fluidizing said furnace section with a fluidizing gas so that said fluidizing gas combines with said gaseous products of combustion to form flue gases which entrain portions of said fuel particles, said solid products of combustion, and said fine and said coarse sorbent materials; (f) passing said flue gases and said entrained material from said furnace section; (g) separating said entrained material from said flue gases; (h) passing said separated entrained material to said recycle heat exchange section to cool said separated entrained material; (i) passing said cooled entrained material to said furnace section; (j) establishing a fluid flow circuit having a cooling fluid passing through said circuit; (k) transferring heat from said furnace section and said recycle heat exchange section to said fluid in response to load demands on said system; (l) increasing said heat transfer to said fluid in response to increases in said load demands up to a predetermined value of said load demands; (m) further increasing said heat transfer to said fluid in response to increases in said load demands above said predetermined value; and (n) decreasing said ratio of fine to coarse sorbent feed in response to increases in said load demands above said predetermined value to offset said further increase in said heat transfer to said fluid. ### Claim 10 (depends on 9) The method of claim 9 further comprising removing heat from said fluid in response to increases in said load demands above said predetermined value to further offset said increase in said heat transfer to said fluid. ### Claim 11 (depends on 9) The method of claim 9 further comprising forming a heat recovery section, and passing said separated flue gases to said heat recovery section. ### Claim 12 A method for controlling a steam generating system comprising: (a) forming a furnace section and a recycle heat exchange section; (b) introducing fuel particles into said furnace section; (c) combusting said fuel particles to form gaseous and solid products of combustion; (d) introducing relatively fine and relatively coarse sorbent material into said furnace section at a ratio of said fine to said coarse sorbent material for adsorbing sulfur generated by combustion of said fuel particles; (e) fluidizing said furnace section with a fluidizing gas so that said fluidizing gas combines with said gaseous products of combustion to form flue gases which entrain portions of said fuel particles, said solid products of combustion, and said fine and said coarse sorbent materials; (f) passing said flue gases and said entrained material from said furnace section; (g) separating said entrained material from said flue gases; (h) passing said separated entrained material to said recycle heat exchange section to cool said separated entrained material; (i) passing said cooled entrained material to said furnace section; (j) establishing a fluid flow circuit having a cooling fluid passing through said circuit; (k) transferring heat from said furnace section and said recycle heat exchange section to said fluid in response to load demands on said system; (l) increasing said heat transfer to said fluid in response to increases in said load demands to cause an increase in temperature of said fluid to a predetermined temperature; and (m) decreasing said ratio of said fine to said coarse sorbent material introduced into said furnace section in response to increases in temperature of said fluid above said predetermined temperature to offset said increase in said temperature. ### Claim 13 (depends on 12) The method of claim 12 further comprising removing heat from said fluid in response to increases in temperature of said fluid above said predetermined temperature to further offset said increase in said temperature. ### Claim 14 (depends on 12) The method of claim 12 further comprising forming a heat recovery section, and passing said separated flue gases to said heat recovery section. ### Claim 15 A fluidized bed combustion method comprising: (a) forming a furnace section and a recycle heat exchange section; (b) introducing fuel particles into said furnace section; (c) combusting said fuel particles to form gaseous and solid products of combustion; (d) introducing relatively fine and relatively coarse sorbent material into said furnace section at a ratio of said fine to said coarse sorbent material; (e) fluidizing said furnace section with a fluidizing gas so that said fluidizing gas combines with said gaseous products of combustion to form flue gases which entrain portions of said fuel particles, said solid products of combustion, and said fine and said coarse sorbent materials; (f) passing said flue gases and said entrained material from said furnace section; (g) separating said entrained material from said flue gases; (h) passing said separated entrained material to said recycle heat exchange section to cool said separated entrained material; (i) passing said cooled entrained material to said furnace section; (j) establishing a fluid flow circuit to transfer heat from said separated entrained material in said recycle heat exchange section to a fluid passing through said circuit; (k) achieving a desired temperature for said fluid; (l) increasing said heat transfer to said fluid after said fluid achieves said desired temperature; and (m) decreasing said ratio of fine to coarse sorbent feed introduced into said furnace section to offset said increase in said heat transfer to said fluid. ### Claim 16 (depends on 15) The method of claim 15 further comprising removing heat from said fluid to further offset said increase in said heat transfer to said fluid. ### Claim 17 (depends on 15) The method of claim 15 further comprising forming a heat recovery section, and passing said separated flue gases to said heat recovery section. ### Claim 18 (depends on 15) The method of claim 15 wherein said step of increasing said heat transfer to said fluid is in response to increases in load demands. ### Claim 19 A fluidized bed combustion method comprising: (a) forming a furnace section and a recycle heat exchange section; (b) introducing fuel particles into said furnace section; (c) combusting said fuel particles to form gaseous and solid products of combustion; (d) introducing relatively fine and relatively coarse sorbent material into said furnace section at a ratio of said fine to said coarse sorbent material for adsorbing sulfur generated by combustion of said fuel particles; (e) fluidizing said furnace section with a fluidizing gas so that said fluidizing gas combines with said gaseous products of combustion to form flue gases which entrain portions of said fuel particles, said solid products of combustion, and said fine and said coarse sorbent materials; (f) passing said flue gases and said entrained material from said furnace section; (g) separating said entrained material from said flue gases; (h) passing said separated entrained material to said recycle heat exchange section to cool said separated entrained material; (i) passing said cooled entrained material to said furnace section; (j) establishing a fluid flow circuit to transfer heat from said separated entrained material in said recycle heat exchange section to water or steam or a water-steam mixture passing through said circuit; (k) heating said water or steam or water-steam mixture so that said water or steam or water-steam mixture is converted to superheated steam having a desired temperature; (l) increasing said heat transfer to said superheated steam, thereby causing an increase in temperature of said superheated steam above said desired temperature; and (m) decreasing said ratio of fine to coarse sorbent feed introduced into said furnace section to offset said increase in temperature of said superheated steam. ### Claim 20 (depends on 19) The method of claim 19 further comprising removing heat from said superheated steam to further offset said increase in temperature of said superheated steam. ### Claim 21 (depends on 19) The method of claim 19 further comprising forming a heat recovery section, and passing said separated flue gases to said heat recovery section. ### Claim 22 (depends on 19) The method of claim 19 wherein said step of increasing said heat transfer to said superheated steam is in response to increases in said load demands.