Spray dryer absorber and related processes
A spray dryer absorber (SDA) system used to reduce the concentration of at least one acid compound in a gas utilizes low or no alkali-containing particulate compounds to prevent cementing during operation. The low or no-alkali-containing compounds may be supplied from external sources and/or from a particulate collection device located downstream of the SDA.
1. A system for reducing the tendency for cementing in a spray dryer absorber, comprising:
at least one source of at least one gas, such at least one gas containing at least one acid compound, the concentration of which in the at least one gas has to be reduced;
at least one spray dryer absorber for receiving the at least one gas and using at least one alkali-containing reagent for reacting with the at least one acid compound;
at least one as-is particulate recycle line designed to supply an as-is particulate from another combustor;
a particulate collection device located downstream of the at least one spray dryer absorber; and
at least two means for injecting at least one particulate compound into the at least one gas in combination with the at least one alkali-containing reagent, wherein the at least one particulate compound is comprised of a low or no alkali particulate from the as-is particulate recycle line and has an alkali content that is low enough not to cause cementing in the spray dryer absorber during operation,
wherein a first means of the at least two means for injecting the at least one particulate compound into the at least one gas is individually located upstream of the spray dryer absorber and wherein a second means of the at least two means for injecting the at least one particulate compound into the at least one gas is individually located in the at least one spray dryer absorber so that a combination with the individually injected at least one alkali-containing reagent is formed within the at least one spray dryer absorber due to the at least one second injection means, and
wherein the low or no alkali content particulate compound is solely composed of as-is fly ash recycled directly from the particulate collection device and another combustor.
2. The system of claim 1 , wherein the at least one gas comprises gas from a combustion process generated from a combustor located upstream of the at least one spray dryer absorber.
3. The system of claim 2 , wherein the combustion process is conducted in a fluidized bed boiler.
4. The system of claim 3 , wherein the combustion process is conducted in a circulating fluidized bed boiler.
5. The system of claim 1 , wherein the alkali-containing reagent comprises a mixture of a reactivated reagent from a reactivating particulate line and a fresh reagent.
6. A method of operating a system with a spray dryer absorber to reduce the tendency for cementing in the spray dryer absorber, comprising the steps of:
(A) providing at least one gas stream from at least one source, wherein the at least one gas stream contains at least one acid compound, the concentration of which in the at least one gas stream has to be reduced;
(B) providing at least one spray dryer absorber designed to receive the at least one gas stream from the at least one gas source, the at least one spray dryer absorber using at least one alkali-containing reagent for reacting with the at least one acid compound;
(C) providing a particulate collection device located downstream of the at least one spray dryer absorber;
(D) at least one as-is particulate recycle line designed to supply an as-is particulate from the particulate collection device; and
(E) providing at least two means for injecting at least one particulate compound into the at least one gas stream, wherein the at least one particulate compound is comprised of a low or no alkali particulate from the as-is particulate recycle line and has an alkali content that is low enough not to cause cementing in the spray dryer absorber during operation,
wherein a first means of the at least two means for injecting the at least one particulate compound into the at least one gas is individually located upstream of the at least one spray dryer absorber, and wherein a second means of the at least two means for injecting the at least one particulate compound into the at least one gas is individually located within the at least one spray dryer absorber simultaneously with the at least one alkali-containing reagent or within the at least one spray dryer absorber downstream of the point at which the at least one alkali-containing reagent is provided the at least one spray dryer absorber so that a combination with the individually injected at least one alkali-containing reagent is formed within the at least one spray dryer absorber due to the at least one second injection means, and
wherein the low or no alkali content particulate compound is solely composed of as-is fly ash recycled directly from the particulate collection device.
7. The method of claim 6 , wherein there the at least one second injection means of Step (E) is located both within the at least one spray dryer absorber and thus the injection of the at least one particulate compound occurs simultaneously with providing the at least one alkali-containing reagent and within the at least one spray dryer absorber downstream of the point at which the at least one alkali-containing reagent is provided to and thus the injection of the at least one particulate compound occurs after providing the at least one alkali-containing reagent.
8. The method of claim 6 , wherein the at least one gas stream comprises gas from a combustion process generated from a combustor located upstream of the at least one spray dryer absorber.
9. The method of claim 6 , wherein the combustion process is conducted in a fluidized bed boiler.
10. The method of claim 9 , wherein the combustion process is conducted in a circulating fluidized bed boiler.
11. The method of claim 6 , wherein the alkali-containing reagent comprises a mixture of a reactivated reagent from the reactivating particulate line and a fresh reagent.
12. The method of claim 6 , wherein the method further comprises a third injection means in Step (E) that is located within the at least one spray dryer absorber downstream of the point at which the at least one alkali-containing reagent is provided to and thus the injection of the at least one particulate compound occurs after the reaction of the at least one alkali-containing reagent with the at least one acid compound.
13. A system for reducing the tendency for cementing in a spray dryer absorber, comprising:
at least one source of at least one gas, such at least one gas containing at least one acid compound, the concentration of which in the at least one gas has to be reduced;
at least one spray dryer absorber for receiving the at least one gas and using at least one alkali-containing reagent for reacting with the at least one acid compound;
a particulate collection device located downstream of the at least one spray dryer absorber;
at least one as-is particulate recycle line designed to supply an as-is particulate from a another combustor; and
at least two means for injecting at least one particulate compound into the at least one gas in combination with the at least one alkali-containing reagent, wherein the at least one particulate compound is comprised of a low or no alkali particulate from the as-is particulate recycle line and has an alkali content that is low enough not to cause cementing in the spray dryer absorber during operation,
wherein one of the at least two means for injecting the at least one particulate compound into the at least one gas is individually located in the at least one spray dryer absorber so that a combination with the individually injected at least one alkali-containing reagent is formed within the at least one spray dryer absorber,
wherein one of the at least two means for injecting the at least one particulate compound into the at least one gas in combination with the at least one alkali-containing reagent is located upstream of the spray dryer absorber, and
wherein the low or no alkali content particulate compound is solely composed of as-is fly ash recycled directly from the particulate collection device and another combustor.
14. The system of claim 13 , wherein the at least one gas comprises gas from a combustion process generated from a combustor located upstream of the at least one spray dryer absorber.
15. The system of claim 14 , wherein the combustion process is conducted in a fluidized bed boiler.
16. The system of claim 13 , wherein the alkali-containing reagent comprises lime slurry, fly ash, or a mixture thereof.
17. The system of claim 13 , wherein the system further comprises:
at least three means for injecting at least one particulate compound into the at least one gas in combination with the at least one alkali-containing reagent, wherein the at least one particulate compound is comprised of a low or no alkali particulate from the as-is particulate recycle line to prevent cementing in the spray dryer absorber during operation,
wherein one of the at least three means for injecting the at least one particulate compound into the at least one gas in combination with the at least one alkali-containing reagent is located upstream of the spray dryer absorber, wherein one of the at least three means for injecting the at least one particulate compound into the at least one gas in combination with the at least one alkali-containing reagent is located within the spray dryer absorber, and wherein one of the at least three means for injecting the at least one particulate compound into the at least one gas in combination with the at least one alkali-containing reagent is located downstream of the spray dryer absorber.
18. A system for reducing the tendency for cementing in a spray dryer absorber, comprising:
at least one source of at least one gas, such at least one gas containing at least one acid compound, the concentration of which in the at least one gas has to be reduced, wherein the at least one gas comprises a gas from a combustion process;
at least one spray dryer absorber for receiving the at least one gas and using at least one alkali-containing reagent for reacting with the at least one acid compound;
a particulate collection device located downstream of the at least one spray dryer absorber;
at least one as-is particulate recycle line designed to supply an as-is particulate from a another combustor; and
at least one means for injecting at least one particulate compound into the at least one gas in combination with the at least one alkali-containing reagent, wherein the at least one particulate compound is comprised of a no alkali particulate from the as-is particulate recycle line and has no alkali content so as to not cause cementing in the spray dryer absorber during operation,
wherein one of the at least one means for injecting the at least one particulate compound into the at least one gas is individually located in the at least one spray dryer absorber so that a combination with the individually injected at least one alkali-containing reagent is formed within the at least one spray dryer absorber, and
wherein the low or no alkali content particulate compound is solely composed of as-is fly ash recycled directly from the particulate collection device and another combustor.
19. A system for reducing the tendency for cementing in a spray dryer absorber, comprising:
at least one source of at least one gas, such at least one gas containing at least one acid compound, the concentration of which in the at least one gas has to be reduced;
at least one spray dryer absorber for receiving the at least one gas and using at least one alkali-containing reagent for reacting with the at least one acid compound;
a particulate collection device located downstream of the at least one spray dryer absorber;
at least one as-is particulate recycle line designed to supply an as-is particulate from a another combustor; and
at least three means for injecting at least one particulate compound into the at least one gas in combination with the at least one alkali-containing reagent, wherein the at least one particulate compound is comprised of a low or no alkali particulate from the as-is particulate recycle line and has an alkali content that is low enough not to cause cementing in the spray dryer absorber during operation,
wherein one of the at least three means for injecting the at least one particulate compound into the at least one gas in combination with the at least one alkali-containing reagent are individually located near to one another in the at least one spray dryer absorber so that a combination with the individually injected at least one alkali-containing reagent is formed within the at least one spray dryer absorber,
wherein one of the at least three means for injecting the at least one particulate compound into the at least one gas in combination with the at least one alkali-containing reagent is located upstream of the spray dryer absorber,
wherein one of the at least three means for injecting the at least one particulate compound into the at least one gas in combination with the at least one alkali-containing reagent is located within the at least one spray dryer absorber downstream of the point at which the at least one alkali-containing reagent is provided to and thus the injection of the at least one particulate compound occurs after the providing of the at least one alkali-containing reagent,
wherein the low or no alkali content particulate compound is solely composed of as-is fly ash recycled directly from the particulate collection device and another combustor, and
wherein the alkali-containing reagent comprises lime slurry, fly ash, or a mixture thereof.