Spray dryer absorber and related processes

US10208951B2 · US · B2

Patent metadata
FieldValue
Publication numberUS-10208951-B2
Application numberUS-85479507-A
CountryUS
Kind codeB2
Filing dateSep 13, 2007
Priority dateSep 13, 2007
Publication dateFeb 19, 2019
Grant dateFeb 19, 2019

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  1. Title

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  2. Abstract

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  3. Assignees and inventors

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  4. Key dates

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  5. First independent claim

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  6. CPC / IPC classifications

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  7. Citations and related patents

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Abstract

Official abstract text for this publication.

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.

First claim

Opening claim text (preview).

I claim: 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 rea

Assignees

Inventors

Classifications

  • F23J15/003Primary

    for supplying chemicals to fumes, e.g. using injection devices · CPC title

  • Sorption with semi-dry devices, e.g. with slurries · CPC title

  • Sulfur; Compounds thereof · CPC title

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Frequently asked questions

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What does patent US10208951B2 cover?
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.
Who is the assignee on this patent?
Maryamchik Mikhail, Babcock & Wilcox Co
What technology area does this patent fall under?
Primary CPC classification F23J15/003. Mapped technology areas include Mechanical Engineering.
When was this patent published?
Publication date Tue Feb 19 2019 00:00:00 GMT+0000 (Coordinated Universal Time) (B2). Legal status and post-grant events are not shown on this page.
What related patents are in patentsdb?
We list 8 related publications on this page (citations in our corpus or others sharing the same primary CPC).