Mercury re-emission control
US-2015209725-A1 · Jul 30, 2015 · US
US10195562B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10195562-B2 |
| Application number | US-201415303195-A |
| Country | US |
| Kind code | B2 |
| Filing date | Apr 9, 2014 |
| Priority date | Apr 9, 2014 |
| Publication date | Feb 5, 2019 |
| Grant date | Feb 5, 2019 |
A practical reading order for non-experts. Skip the full description unless you need deep technical detail.
What the patent document calls the invention.
A short plain-language summary of the technical disclosure.
Who owns or filed the patent and who is credited as inventor.
Filing, priority, publication, and grant dates set the timeline.
The legal scope of protection — read this for what is actually claimed.
Technology tags used to group this patent with similar filings.
Prior art links and similar publications in this corpus.
Official abstract text for this publication.
Systems and methods for reducing a target molecule in a fluid are described. A fluid, such as a gas, may be contacted with a fluid capable of binding with the target molecules and removing the target molecules from the fluid. For example, emissions from a production process may be contacted with water to remove volatile organic compound (VOCs), thereby reducing the VOCs in the emissions. The fluid with bound target molecules may form a target fluid that may be discharged from the system or may be reused until the concentration of the target molecules in the target fluid reaches a threshold concentration. An illustrative production process is the fermentation of wine, which produces an off-gas that includes VOCs, such as ethanol. The systems and methods for reducing a target molecule may significantly reduce or even eliminate the amount of ethanol in the fermentation off-gas.
Opening claim text (preview).
What is claimed is: 1. An apparatus configured to remove ethanol from a gas, the apparatus comprising: at least one fluid discharge component configured to discharge fluid particles capable of forming a hydrogen bond with ethanol, wherein the at least one fluid discharge component comprises a plurality of conical spray nozzles, and wherein the plurality of conical spray nozzles create a conical or substantially conical spray pattern; at least one reaction vessel configured to receive the gas, the at least one fluid discharge component being positioned within the at least one reaction vessel such that the fluid particles form a hydrogen bond with ethanol in the gas to form a target fluid, thereby reducing a concentration of ethanol in the gas; at least one collection container in fluid communication with the at least one reaction vessel and configured to receive the target fluid; and a concentration monitor configured to monitor the concentration of ethanol in the target fluid disposed within the at least one collection container. 2. The apparatus of claim 1 , wherein the fluid discharge component is in fluid communication with the at least one collection container, and wherein at least a portion of the fluid particles discharged by the fluid discharge component comprises target fluid received from the at least one collection container. 3. The apparatus of claim 1 , further comprising a target fluid discharge component configured to discharge the target fluid responsive to the concentration of ethanol reaching a threshold concentration. 4. The apparatus of claim 1 , further comprising at least one outlet in fluid communication with the at least one reaction vessel and configured to discharge the gas having a reduced concentration of ethanol from the apparatus. 5. The apparatus of claim 1 , wherein the fluid particles comprise one or more of water droplets and hydrophilic solvent droplets. 6. The apparatus of claim 1 , wherein the fluid particles comprise fluid droplets having an average diameter of about 10 μm to about 100 μm. 7. The apparatus of claim 1 , wherein the concentration of ethanol in the gas is reduced by about 100%. 8. The apparatus of claim 1 , wherein the concentration of ethanol in the gas is reduced by about 50% to about 100%. 9. The apparatus of claim 1 , wherein the at least one reaction vessel comprises a first reaction vessel in fluid communication with a second reaction vessel, the first reaction vessel being configured to transfer the gas to the second reaction vessel, and wherein the concentration of ethanol in the gas is reduced to a first reduction level within the first reaction vessel and to a second reduction level within the second reaction vessel. 10. The apparatus of claim 9 , wherein the first reduction level is at least about a 50% reduction of ethanol in the gas and the second reduction level is at least about a 90% reduction of ethanol in the gas. 11. The apparatus of claim 1 , wherein the gas is a by-product of a fermentation process. 12. The apparatus of claim 1 , wherein the at least one reaction vessel comprises a dielectric reaction vessel, and wherein a dielectric interaction occurs between fluid particles and ethanol in the dielectric reaction vessel. 13. A method of removing ethanol from a gas, the method comprising: receiving the gas within at least one reaction vessel; reducing a concentration of ethanol in the gas by discharging fluid particles in a conical or substantially conical pattern, wherein the fluid particles are capable of forming a hydrogen bond with ethanol within the at least one reaction vessel such that the fluid particles contact the gas to form a target fluid comprising ethanol bound to the fluid particles; collecting the target fluid within at least one collection container in fluid communication with the at least one reaction vessel; and monitoring ethanol concentration in the target fluid disposed within the at least one collection container. 14. The method of claim 13 , wherein reducing the concentration of ethanol comprises discharging fluid particles including water droplets. 15. The method of claim 13 , wherein reducing the concentration of ethanol comprises discharging fluid droplets having an average diameter of about 10 μm to about 100 μm. 16. The method of claim 13 , wherein receiving the gas comprises receiving the gas in the at least one reaction vessel as a continuous gas stream. 17. The method of claim 13 , wherein reducing the concentration of ethanol comprises reducing the concentration by about 50% to about 100%. 18. The method of claim 13 , further comprising discharging the target fluid responsive to ethanol concentration reaching a threshold concentration. 19. The method of claim 13 , further comprising: configuring the at least one reaction vessel as a first reaction vessel in fluid communication with a second reaction vessel, the first reaction vessel being configured to transfer the gas to the second reaction vessel; reducing the concentration of ethanol in the gas to a first reduction level within the first reaction vessel; and reducing the concentration of ethanol in the gas to a second reduction level within the second reaction vessel. 20. The method of claim 19 , wherein reducing the concentration of ethanol in the gas to a first reduction level comprises reducing to a level of at least about a 50% reduction of ethanol in the gas, and reducing the concentration of the ethanol in the gas to a second reduction level comprises reducing to a level of at least about a 90% reduction of ethanol in the gas. 21. The method of claim 13 , wherein receiving the gas comprises receiving by-product of a fermentation process in an alcohol production process.
Multiple stage absorption · CPC title
from food processing plants or kitchens · CPC title
Volatile organic compounds V.O.C.'s · CPC title
Controlling the absorption process · CPC title
Removing acid components · CPC title
Related publications grouped by family.
Answers are generated from the same data shown on this page.