Coupled medium-low temperature flue gas processing apparatus for fly ash washing
US-2024390959-A1 · Nov 28, 2024 · US
US11439962B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-11439962-B2 |
| Application number | US-202016811689-A |
| Country | US |
| Kind code | B2 |
| Filing date | Mar 6, 2020 |
| Priority date | Mar 7, 2019 |
| Publication date | Sep 13, 2022 |
| Grant date | Sep 13, 2022 |
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.
A system for continuously making-down a dry powder material is provided. The system may include a liquid supply system, a material feed system, a vessel, a filter, and an agitator. The vessel may receive a continuous supply of liquid from the liquid supply system and a continuous supply of dry powder from the material feed system. The liquid and material may be discharged continuously from the vessel. A filter may sealingly extend across the outlet to filter the solution exiting the vessel. The filter may include an upstream surface in contact with the inner volume of the vessel. The agitator may be disposed within the vessel and may be configured to agitate the contents of the vessel. The agitator may include a wiping member configured to contact the upstream surface of the filter while agitating the contents.
Opening claim text (preview).
We claim: 1. An apparatus for continuous make-down of a material, the apparatus comprising: a liquid supply system including a pump operative to provide a continuous supply of liquid; a material feed system operative to provide a continuous supply of dry powder of the material; a vessel defining an inner volume configured to contain a volume of liquid, the vessel including an inlet and an outlet, the inlet being in fluid communication with the liquid supply system and the inner volume, the inlet being configured to receive liquid from the liquid supply system and the dry powder from the material feed system, the outlet being in fluid communication with the inner volume; a filter sealingly extending across the outlet whereby liquid exiting the vessel through the outlet passes through the filter, the filter having an upstream surface in contact with the inner volume; and an agitator disposed within the vessel and configured to agitate the inner volume, the agitator including a wiping member configured to contact the upstream surface of the filter while agitating the inner volume. 2. The apparatus of claim 1 , wherein the wiping member comprises at least one strip of flexible material. 3. The apparatus of claim 2 , wherein the agitator includes a motor operatively connected to a drive shaft and a plurality of blades mounted on the drive shaft. 4. The apparatus of claim 3 , wherein the agitator includes an upper impeller and a lower impeller, the lower impeller including the wiping member. 5. The apparatus of claim 4 , wherein the upper impeller includes a first plurality of spaced apart blades and the lower impeller includes a second plurality of spaced apart blades. 6. The apparatus of claim 5 , wherein the wiping member is mounted to a lower portion of at least one of the second blades. 7. The apparatus of claim 1 , further including a first pressure sensor disposed within the vessel and a second pressure sensor disposed on a discharge member adjacent and in fluid communication with a downstream surface of the filter. 8. The apparatus of claim 7 , wherein the discharge member has an inverted frusto-conical shape. 9. The apparatus of claim 1 , wherein the inlet is positioned at a top end of the vessel such that the substances delivered to the inner volume are gravity-fed. 10. The apparatus of claim 1 , wherein the outlet is positioned at a bottom end of the vessel. 11. The apparatus of claim 1 , wherein the wiping member is constructed of a friction-tempering substance. 12. The apparatus of claim 11 , wherein the friction-tempering substance comprises a fluoropolymer. 13. The apparatus of claim 1 , further comprising a wetting unit for continuously wetting the dry powder with liquid from the liquid supply system. 14. The apparatus of claim 13 , wherein the wetting unit comprises an eductor, the eductor being configured to receive the continuous supply of dry powder from the material feed system and receive the continuous supply of liquid from the liquid supply system, the eductor having an outlet in fluid communication with the inlet of the vessel. 15. The apparatus of claim 1 , further comprising a concentration-measuring detector configured to detect a concentration of the material present in the liquid exiting the inner volume through the outlet. 16. The apparatus of claim 15 , wherein the concentration measuring detector is a reflectometer. 17. An apparatus for continuous make-down of a material, the apparatus comprising: a liquid supply system including a pump operative to provide a continuous supply of liquid; a material feed system operative to provide a continuous supply of dry powder of the material; a wetting unit for continuously wetting the dry powder with liquid from the liquid supply system to form a mixture, the wetting unit comprising an outlet; a vessel defining an inner volume for containing a volume of liquid, the vessel including an inlet and an outlet, the inlet being in fluid communication with the liquid supply system and the inner volume, the inlet being configured to receive the mixture from the wetting unit, the outlet being in fluid communication with the inner volume and configured to continuously deliver a dilute aqueous solution of the polymer formed in the inner volume; a filter sealingly extending across the outlet whereby the dilute aqueous solution exiting the vessel through the outlet passes through the filter, the filter having an upstream surface within the inner volume; and an agitator disposed within the vessel and configured to agitate the inner volume, the agitator including a wiping member configured to contact the upstream surface of the filter while agitating the inner volume. 18. The apparatus of claim 17 , wherein the wetting unit comprises an eductor, the eductor being configured to receive the continuous supply of dry powder from the material feed system and receive the continuous supply of liquid from the liquid supply system, the eductor having an outlet in fluid communication with the inlet of the vessel. 19. A method of continuous make-down of material, the method comprising: continuously delivering a liquid to a wetting unit; continuously delivering a dry powder of the material to the wetting unit; wetting the dry powder with the liquid to form a mixture of liquid and the material; delivering the mixture to an inner volume of a vessel; continuously agitating the mixture contained in the inner volume of the vessel to form a solution; continuously removing a discharge volume of the solution contained in the inner volume of the vessel while passing the discharge volume through a filter and through an outlet of the vessel, the filter having an upstream surface in contact the inner volume of the vessel; and wiping the upstream surface of the filter while agitating the mixture. 20. The method of claim 19 , further comprising determining a pressure differential between the upstream surface of the filter and a downstream surface of the filter. 21. The method of claim 20 , further comprising determining an upstream pressure adjacent the upstream surface of the filter with a first pressure sensor disposed within the vessel and determining a downstream pressure adjacent the downstream surface of the filter with a second pressure sensor disposed on a discharge member adjacent and in fluid communication with the downstream surface of the filter. 22. The method of claim 20 , further comprising controlling an amount of mixture entering or discharge volume of the solution exiting the vessel based upon the pressure differential. 23. The method of claim 19 , wherein the wiping step includes rotating at least one impeller blade having a wiping member thereon, and the wiping member contacting the upstream surface of the filter. 24. The method of claim 19 , further comprising detecting a concentration of the material present in the discharge volume of the solution exiting the inner volume through the outlet. 25. The method of claim 24 , wherein the detecting step is performed with a reflectometer.
using scrapers for cleaning mixers · CPC title
Mixing plastics, polymer material ingredients, monomers or oligomers · CPC title
Methods · CPC title
by introducing solids in liquids, e.g. dispersing or dissolving · CPC title
Speed of feeding of at least one component to be mixed · CPC title
Related publications grouped by family.
Answers are generated from the same data shown on this page.