Temperature controlled nitrogen generation system
US-2016361684-A1 · Dec 15, 2016 · US
US9429274B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9429274-B2 |
| Application number | US-201113233344-A |
| Country | US |
| Kind code | B2 |
| Filing date | Sep 15, 2011 |
| Priority date | Dec 22, 2010 |
| Publication date | Aug 30, 2016 |
| Grant date | Aug 30, 2016 |
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A system for regulating an amount of fresh lime slurry introduced to a spray dry absorber. The control system includes a controller configured to receive input from a continuous emissions monitoring system (CEMS), a valve in communication with the controller and a spray dry absorber suction pump, the valve adapted to regulate an amount of fresh lime slurry provided to the spray dry absorber suction pump and a valve in communication with the controller and a pre-mix tank, the valve adapted to regulate an amount of fresh lime slurry provided to the pre-mix tank.
Opening claim text (preview).
What is claimed is: 1. Apparatus for supplying recycled ash into a dry flue gas desulfurization (DFGD) system, the apparatus comprising: a pre-mix tank configured to receive and combine recycled ash, water, and a fresh lime slurry from a slurry storage tank to form a slurry; an ash make-up tank configured to receive and combine the slurry from the pre-mix tank with a returned non-atomized reagent slurry from the DFGD system to form a feed slurry; a feed tank configured to receive the feed slurry from the ash make-up tank for combination with fresh lime slurry from the slurry storage tank downstream of the feed tank to form the reagent slurry supplied into the DFGD system; a continuous emissions monitoring system arranged in a stack of the DFGD system operative to measure flue gas SO x concentrations; and a controller operable to receive input from the continuous emissions monitoring system and operable to regulate a supply of fresh lime slurry from the slurry storage tank to the pre-mix tank based on the input. 2. Apparatus according to claim 1 , further comprising: a suction pump in fluid communication with the feed tank and a spray dry absorber (SDA) of the DFGD system, the suction pump configured to receive and combine the feed slurry from the feed tank and the fresh lime slurry from the slurry storage tank to form a reagent slurry supplied to the SDA. 3. Apparatus according to claim 2 , wherein the controller regulates an amount of fresh lime slurry supplied to the suction pump based on the input as compared to a SO x concentration setpoint. 4. Apparatus according to claim 1 , wherein the returned non-atomized reagent slurry flows downwardly through a duct, tube, chute or piping into the ash make-up tank to combine with the slurry from the pre-mix tank to form the feed slurry. 5. Apparatus according to claim 1 , wherein the controller regulates an amount of fresh lime slurry supplied to the pre-mix tank based on the input as compared to a SO x concentration setpoint. 6. Apparatus for supplying recycled ash into a dry flue gas desulfurization (DFGD) system comprising: a collector for ash separated from flue gas downstream of a spray dry absorber of the DFDG system; a pre-mix tank configured to receive and combine recycled ash from the collector, water, a fresh lime slurry from a slurry storage tank and a returned non-atomized reagent slurry from the spray dry absorber to form a feed slurry; a feed tank configured to receive the feed slurry from the pre-mix tank for supply to and combination with fresh lime slurry in a suction pump to form a reagent slurry supplied into the spray dry absorber; a continuous emissions monitoring system arranged in a stack of the DFGD system operative to measure flue gas SO x concentrations; and a controller operable to receive input from the continuous emissions monitoring system and operable to regulate a supply of fresh lime slurry from the slurry storage tank to the pre-mix tank based on the input.
Arrangements of devices for treating smoke or fumes · CPC title
Flue gases · CPC title
Hydrochloric acid · CPC title
Multi-step processes · CPC title
Hydrofluoric acid · CPC title
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