Ammonium recovery from waste water using CO
View Patent ↗The processes are utilized to recover ammonium from waste water using CO 2 acidified absorption water. The process is particularly suited for utilization of cellular matter and a CO 2 rich tail gas from a syngas fermentation process and derives significant benefit from the recovery of ammonium bicarbonate and ammonium carbonate. Ammonia and ammonium are recovered from the treatment of the syngas as an ammonium rich solution, at least a portion of which is recycled to the fermentation zone to aid in the production of liquid products. A carbon dioxide rich gas produced by fermentation is used to capture the ammonia and ammonium, forming the ammonium rich solution.
1. A process for recovering ammonium carbonate and ammonium bicarbonate from a liquid solution comprising at least one of ammonia or ammonium, the process comprising the steps of: a. adjusting the pH of the liquid solution comprising ammonium to convert ammonium in the solution to free ammonia and produce a converted solution; b. stripping ammonia from the converted solution in an ammonia stripping vessel to produce a gas phase ammonia stream; c. contacting the ammonia stream with a scrubbing liquid comprising dissolved CO 2 in a scrubbing vessel to produce ammonium bicarbonate and ammonium carbonate; d. withdrawing an ammonium liquid comprising ammonium carbonate and ammonium bicarbonate from the scrubbing vessel; e. recovering a first portion of the ammonium liquid as an ammonium product stream; f. contacting a second portion of the ammonium liquid with a CO 2 containing gas stream and a make-up liquid to produce the scrubbing liquid.
2. The process of claim 1 where the CO 2 mole fraction of the CO 2 containing gas stream is greater than 40%.
3. The process of claim 1 where a vacuum stripper strips ammonia from the converted solution.
4. The process of claim 1 where a membrane distillation system strips ammonia from the converted solution.
5. The process of claim 1 where the CO 2 containing gas is a tail gas from a fermentation process.
6. The process of claim 5 wherein a portion of the ammonium rich liquid passes to the fermentation process.
7. The process of claim 1 wherein a gas phase stripping stream strips ammonia from the converted solution.
8. The process of claim 1 wherein the pH of the scrubbing liquid is adjusted to 8.0 or lower.
9. The process of claim 1 wherein the mole fraction of ammonia exceeds the mole fraction of ammonium in the converted solution of step a.
10. The process of claim 1 wherein the pKa in the ammonia stripping vessel is at least one unit above the pKa of ammonia.
11. A process for recovering ammonium carbonate and ammonium bicarbonate from an ammonium containing solution generated in the treatment of biomass derived syngas, the process comprising the steps of: a. generating a syngas stream by the gasification of biomass; b. scrubbing at least a portion of the syngas stream in a syngas scrubber to generate a syngas scrubbing liquid containing ammonium and a scrubbed syngas stream; c. passing the scrubbed syngas stream to a fermentation zone to produce a fermentation product and a tail gas stream comprising CO 2 ; d. passing the syngas scrubbing liquid to an ammonia stripping vessel and adjusting the pH in the ammonia stripping vessel to at least the pKa of ammonia to maintain free ammonia in the ammonia stripping vessel; e. stripping ammonia from the ammonia stripping vessel with a stripping gas stream to produce an ammonia gas stream; f. contacting the ammonia gas stream with an ammonia scrubbing liquid comprising dissolved CO 2 in a scrubbing vessel to produce an ammonium liquid comprising ammonium bicarbonate and ammonium carbonate; g. recovering a first portion of the ammonium liquid as an ammonium product stream; h. passing a second portion of the ammonium liquid into contact with the tail gas stream and a make-up liquid in a gas contacting vessel to produce the ammonia scrubbing liquid.
12. The process of claim 11 wherein the fermentation zone produces biosolids as a by-product, the biosolids are decomposed in a digester, and an ammonium containing waste stream is recovered from the digester and passed to the ammonia stripping vessel.
13. The process of claim 11 wherein the CO 2 mole fraction of the tail gas stream is greater than 40%.
14. The process of claim 11 wherein a portion of the ammonium liquid passes to a fermentation process to provide a source of nitrogen for microorganisms contained therein.
15. The process of claim 11 wherein the pH of the ammonia scrubbing liquid is at least 8.0 or below.
16. The process of claim 11 wherein the pKa in the ammonia stripping vessel is at least one unit above the pKa of ammonia.
17. The process of claim 11 wherein the syngas contains dissolved volatile compounds including HCN, the syngas scrubbing liquid comprises water, and the syngas scrubbing liquid is treated by at least one of air stripping or contact with activated carbon adsorption to remove HCN and volatile compounds before adjusting the pH of the syngas scrubbing liquid.
18. A process for recovering ammonium carbonate and ammonium bicarbonate from an ammonium containing solution generated in the treatment and fermentation of biomass derived syngas, the process comprising the steps of: a. generating a raw syngas stream by the gasification of biomass; b. cooling and scrubbing the raw syngas stream in a scrubber and a cooler to generate a scrubbed syngas stream and a condensate stream containing volatile compounds and ammonium; c. passing the scrubbed syngas stream to a fermentation zone to produce a fermentation product, a tail gas stream comprising CO 2 , and a biosolids stream; d. passing the biosolids to a digester to decompose the biosolids and recover an ammonium containing solution from the digester; e. removing volatile compounds from the condensate stream to generate a scrubbed condensate stream containing ammonium; f. passing at least a portion of the scrubbed condensate stream and the ammonium containing solution to an ammonia stripping vessel and maintaining the pH in the ammonia stripping vessel at least one unit above the pKa of ammonia to maintain free ammonia in the ammonia stripping vessel; g. stripping ammonia from the ammonia stripping vessel with a stripping gas stream to produce an ammonia gas stream; h. contacting the ammonia gas stream with an ammonia scrubbing liquid comprising dissolved CO 2 in a scrubbing vessel to produce ammonium bicarbonate and ammonium carbonate; i. withdrawing an ammonium liquid comprising ammonium bicarbonate and ammonium carbonate from the scrubbing vessel; j. recovering a first portion of the ammonium liquid as an ammonium product stream and passing at least a portion of the ammonium product stream to the fermentation zone; and, k. contacting a second portion of the ammonium liquid with the tail gas stream and a make-up liquid in a gas contacting vessel to produce the ammonia scrubbing liquid comprising dissolved CO 2 .
19. The process of claim 18 where the CO 2 mole fraction of the tail gas stream is greater than 40%.
20. The process of claim 19 wherein the pH of the ammonia scrubbing liquid is at 8.0 or below.