System and method for multi-functional slurry processing
A multi-functional slurry processing system (“VARCOR”) and associated methods is disclosed. The present examples provide a multi-functional slurry processing system incorporating systems and methods for separating liquid and solid components in slurries. In particular the systems and methods described herein produce clean water, dried solids, and potential concentration of desirable constituents with a boiling point lower than water. At least one example of the multi-functional slurry processing system provides a self-contained processing facility configured to efficiently convert high water-content slurries into its constituent solid and liquid fractions and subsequently generating and collecting clean water and concentrating desirable constituents with a boiling point lower than water. The multi-functional slurry processing system advantageously applies thermodynamic principles in a system which may include various combinations of a preheater, a degassing unit, a dryer, a steam filter, a compressor, a concentrating tower, and a condensation unit.
1. A system for the processing of waste comprising:
a dryer;
a preheater coupled to the dryer;
a compressor receiving slurry vapor from the dryer, and returning a pressurized slurry vapor to the dryer; and
a concentrating tower comprising a hot side and a cold side coupled to the dryer;
wherein a degassing sub-assembly is disposed between the dryer and the preheater.
2. The system for the processing of waste of claim 1 , further comprising a steam filter disposed between the compressor and the dryer.
3. The system for the processing of waste of claim 1 , in which a slurry is fed into input to the dryer.
4. The system for the processing of waste of claim 3 , in which the slurry feed to the dryer is preheated by the preheater.
5. The system for the processing of waste of claim 1 , in which a concentration of the pressurized slurry vapor first occurs in the dryer creating a concentrated slurry vapor that is fed into the concentrating tower.
6. A system for the processing of waste, the system comprising:
a preheater configured to receive a wet slurry and producing a heated wet slurry;
a degassing sub-assembly configured to receive the heated wet slurry from the preheater;
a dryer comprised of at least a cold side, and a hot side, the hot side including: one or more drying discs with an axial shaft, wherein each of the one or more drying discs is at least partially hollow and contains one or more disc condensate tubes and one or more disc condensate scoops configured to output a dryer condensate; and
a compressor configured to receive a slurry vapor from the dryer and output a pressurized slurry vapor into the hot side of the dryer.
7. The system for the processing of waste of claim 6 , wherein the dryer is configured to concentrate the pressurized slurry vapor to produce a first concentrated slurry vapor,
the system further comprising:
a concentrator apparatus having at least a hot side configured to receive the first concentrated slurry vapor from the dryer and to further concentrate the first concentrated slurry vapor into a second concentrated slurry vapor, and a cold side configured to output water.
8. The system for the processing of waste of claim 6 , further comprising a steam filter subassembly disposed between the compressor and the dryer.
9. The system for the processing of waste of claim 6 , in which the dryer includes at least one scraper to remove a dried slurry from a drying disc surface.
10. The system for the processing of waste of claim 6 , in which the one or more drying discs rotate about the axial shaft.
11. The system for the processing of waste of claim 10 , in which the axial shaft is hollow forming a common cavity with the one or more drying discs.
12. A system comprising:
a dryer including:
a plurality of heated rotating hollow drying discs;
a horizontal hollow spindle coupling each of the plurality of heated rotating hollow drying discs and forming a pathway for an input flow of a pressurized slurry vapor, and an input for a counter flow pathway for a concentrating tower condensate; and
a compressor with a compressor input coupled to a dryer cold side of the dryer, and a compressor output coupled to the pathway for the input flow of the pressurized slurry vapor in the dryer.
13. The system of claim 12 , further comprising, a concentrating tower sub-assembly coupled to the pressurized slurry vapor pathway of the dryer for accepting a first concentrated slurry vapor from the dryer, the concentrating tower sub-assembly including a concentrating tower that passes the concentrating tower condensate to the input of the dryer, the concentrating tower having an output coupled to the input of the dryer, and a second output for a second concentrated slurry vapor.
14. A dryer comprising:
a slurry trough;
a horizontally disposed rotating tube;
a plurality of rotating discs coupled to the rotating tube and positioned so that a portion of a respective flat disc surface is in contact with a slurry disposed in the slurry trough; and
a plurality of scrapers pressed against the respective flat disc surface, wherein the plurality of scrapers are disposed in a scraping sub-assembly drawer.
15. The dryer of claim 14 , in which at least one of the plurality of rotating discs is heated producing a dried slurry coating on a corresponding flat disc surface.
16. The dryer of claim 15 , in which the plurality of scrapers remove the dried slurry from each flat disc surface.
17. The dryer of claim 16 , in which the dried slurry removed from each flat disc surface is collected in a solids removal chute.
18. The dryer of claim 14 , in which the scraping sub-assembly drawer comprises:
at least one blade having a disc end and a retraction spring end, pivotally coupled to a scraper frame about a pivot point;
a retraction spring coupling the retraction spring end to the scraper frame; and
a bladder disposed between the pivot point and the retraction spring.
19. The dryer of claim 14 , in which the horizontally disposed rotating tube is hollow forming a tube interior.
20. The dryer of claim 19 , in which at least one of the plurality of rotating discs is hollow forming a disc interior.
21. The dryer of claim 20 , in which the tube interior is open to the disc interior.
22. The dryer of claim 21 , in which the disc interior includes one or more disc condensate tubes, and one or more disc condensate scoops configured to output dryer condensates.
23. The dryer of claim 14 , in which the horizontally disposed rotating tube receives a concentrating tower concentrate and outputs a concentrated slurry vapor.