System and method for recovering nutrients from a high nitrogenous liquid waste
US-2024083791-A1 · Mar 14, 2024 · US
US10640428B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10640428-B2 |
| Application number | US-201715421265-A |
| Country | US |
| Kind code | B2 |
| Filing date | Jan 31, 2017 |
| Priority date | Sep 16, 2009 |
| Publication date | May 5, 2020 |
| Grant date | May 5, 2020 |
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The invention relates to a method for recovery of urea dust and ammonia from a gas stream by contacting said gas stream with an aqueous sulphuric acid solution, thus forming an acid solution of ammonium sulphate and urea, characterized in that the acid solution is concentrated to a melt comprising less than 5 wt % of water, which melt is subsequently transferred into solid particles comprising urea and ammonium sulphate.
Opening claim text (preview).
The invention claimed is: 1. A method for converting urea dust and ammonia from a waste air stream comprising urea dust and ammonia into particles comprising urea and ammonium sulphate which method comprises (i) scrubbing said waste air stream comprising air, urea dust and ammonia with an aqueous sulphuric acid solution, thus forming an acidic solution of ammonium sulphate and urea; (ii) adding ammonia to the acid solution, thus forming a neutralized solution of urea and ammonium sulphate in water; (iii) concentrating the neutralized solution of (ii) to a melt comprising less than 5 wt % of water, and (iv) transforming the melt into solid particles comprising urea and ammonium sulphate; wherein the waste air stream is from urea granulation or urea prilling; and wherein step (iv) is performed in a pelletizer. 2. The method of claim 1 , wherein the concentrating of the neutralized solution from step (ii) in step (iii) is performed by vaporization of at least part of the water phase, thus forming water vapor and said melt comprising less than 5 wt % of water. 3. The method of claim 2 , wherein the vaporization is performed in more than one step. 4. The method of claim 1 , wherein the melt is mixed with an additional amount of ammonium sulphate. 5. The method of claim 1 wherein the neutralized solution of step (ii) is mixed with an additional amount of ammonium sulphate before said concentrating of step (iii). 6. The method of claim 1 , wherein said pelletizer comprises a feeding device, a belt and a device to remove the formed pellets from the belt, whereby droplets of the urea/ammonium sulfate comprising liquid are dosed to the belt, whereon the urea/ammonium sulfate-comprising droplets solidify; and removing the formed urea/ammonium sulfate comprising particles from the belt. 7. The method of claim 1 , wherein said solid particles obtained in step (iv) are a solid UAS fertilizer product. 8. The method of claim 1 , wherein the scrubbing of step (i) is carried out in a scrubber that circulates said acidic solution of ammonium sulphate and urea over the scrubber, and make-up water is provided to the scrubber, wherein cleaned air from said waste air stream leaves the scrubber.
Organic compounds not provided for in groups B01D2257/00 - B01D2257/602 · CPC title
Ammonia · CPC title
Sulfuric acid · CPC title
Ammonia · CPC title
Post-treatment · CPC title
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