IP Library Granted Patent US 11,261,560
Granted Patent B2
US 11,261,560 · App. 16/728,793 · Granted Mar 1, 2022

Method and system of thermo-vacuum drying and processing

Inventors: Yaroslav Chudnovsky (Skokie, IL); Dmytro Buyadgie (Pleasant Hill, CA); Olexiy Buyadgie (Walnut Creek, CA)
Assignee: UTILIZATION TECHNOLOGY DEVELOPMENT, NFP
D06F58/206D06F58/10D06F58/26D06F58/30D06F58/24
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Quick Facts
Patent No.
US 11,261,560
App. No.
16/728,793
Granted
Mar 1, 2022
Kind
B2
Abstract

Methods and systems for the thermo-vacuum drying and processing of objects such as clothes. A vacuum ejector driven by high-pressure steam is employed to evacuate evaporated moisture mixed with air from a dryer vessel producing an intensification of the drying process such as can significantly reduce the energy and time requirements for the drying process and increase water utilization.

Claims (41)

1. A method for thermo-vacuum drying an object, the method comprising:

receiving the object into a thermo-vacuum dryer vessel;

passing a high-pressure steam through a vacuum ejector, from an inlet of the vacuum ejector to and outlet of the vacuum ejector;

evacuating evaporated moisture mixed with air from the dryer vessel via a second inlet of the vacuum ejector driven by a vacuum created by the high-pressure steam passing through the vacuum ejector, wherein steam and the evaporated moisture mixed with air from the dryer vessel exit the outlet of the vacuum ejector; and

applying heat extracted from at least a portion of the steam exiting from the outlet of the vacuum ejector to the object in the thermo-vacuum dryer vessel for evaporating further moisture from the object within the dryer vessel.

2. The method of claim 1 additionally comprising:

generating the high-pressure steam in a boiler/steam generator.

3. The method of claim 2 additionally comprising:

directing at least a first portion of the generated high-pressure steam to the vacuum ejector to provide a motive flow to drive the vacuum ejector to affect the evacuating of the evaporated moisture mixed with air from the dryer vessel and

directing a second portion of the generated high-pressure steam to a heat exchanger for heating the object inside the dryer vessel.

4. The method of claim 1 additionally comprising:

directing at least a portion of the evacuated evaporated moisture mixed with air mixture from the dryer vessel to a heat exchanger to condense moisture and separate at least a portion of the condensed moisture from the air.

5. The method of claim 4 wherein the heat exchanger acts on at least a portion of the evaporated moisture to form a condensate stream, the method additionally comprising:

feeding at least a first portion of the condensate stream to a boiler/steam generator to form the high-pressure steam.

6. The method of claim 5 additionally comprising:

feeding at least a second portion of the condensate stream to a washer device or other condensate consuming service to form a second object for the thermo-vacuum drying.

7. The method of claim 1 wherein the object comprises an item of clothing and the method additionally comprises post-drying treatment of freezing the item of clothing to free the item of clothing of materials whose byproducts induce severe allergic reactions.

8. The method of claim 7 wherein materials whose byproducts induce severe allergic reactions are selected from the group consisting of bacteria, saprophytes, dust mites and combinations thereof.

9. The method of claim 1 wherein the object comprises an item of clothing and the method additionally comprises post-drying treatment of low-temperature cooling.

10. The method of claim 9 wherein the low-temperature cooling supports at least one of whitening effect and improved smell to the item of clothing.

11. The method of claim 10 wherein the treatment of low-temperature cooling comprises utilizing low-grade heat from thermo-vacuum drying process residuals to produce in an ejector refrigerating machine cooling processing at a temperature of no more than 30° F. to 14° F.

12. A system for thermo-vacuum drying an object, the system comprising:

a thermo-vacuum dryer vessel to apply heat to an object therein contained to evaporate moisture from the object; and

a vacuum ejector in communication with the thermo-vacuum dryer vessel, the vacuum ejector having a steam passage, including a steam inlet and a steam outlet, and a moisture inlet connected to the thermo-vacuum dryer vessel, and the vacuum ejector, upon actuation, to affect evacuation of at least a portion of the evaporated moisture from the thermo-vacuum dryer vessel through the moisture inlet.

13. The system of claim 12 additionally comprising:

a boiler/steam generator to generate high-pressure steam, the boiler/steam generator at least in pressurized steam transfer communication with the vacuum ejector to affect the evacuation of evaporated moisture mixed with air from the dryer vessel; and

a heat exchanger surrounding the dryer vessel configured to receive outlet steam from the vacuum ejector and transfer heat to the dryer vessel from the outlet steam, wherein no outlet steam from the outlet of the vacuum ejector contacts the object within the dryer vessel.

14. The method of claim 1 wherein the high-pressure steam does not pass through the thermo-vacuum dryer vessel.

15. A method for thermo-vacuum drying an object, the method comprising:

receiving the object into a thermo-vacuum dryer vessel;

generating a high-pressure steam;

introducing the high-pressure steam through a vacuum ejector, from a first inlet of the vacuum ejector to an outlet of the vacuum ejector, to create a vacuum though a second inlet of the vacuum ejector, the second inlet connected to the thermo-vacuum dryer vessel;

evacuating evaporated moisture from the dryer vessel through the second inlet of the vacuum ejector, wherein each of the steam and the evaporated moisture from the dryer vessel exit the outlet of the vacuum ejector.

16. The method of claim 15 additionally comprising:

applying heat to the object in the thermo-vacuum dryer vessel for evaporating moisture from the object within the dryer vessel.

17. The method of claim 16 wherein the heat is indirectly applied through a heat exchanger in combination with the dryer vessel.

18. The method of claim 17 wherein the heat exchanger surrounds the dryer vessel and receives the steam from the outlet of the vacuum ejector, and no high-pressure steam nor steam or evaporated moisture from the outlet of the vacuum ejector contacts the object within the dryer vessel.

19. The method of claim 15 additionally comprising:

directing at least a portion of the evacuated moisture from the thermo-vacuum dryer vessel to a recuperative heat exchanger to condense moisture and separate at least a portion of the condensed moisture, wherein the recuperative heat exchanger acts on at least a portion of the evaporated moisture to form a condensate stream, the method additionally comprising feeding at least a first portion of the condensate stream to a boiler/steam generator to form the high-pressure steam for introduction to the vacuum ejector.

20. The method of claim 15 additionally comprising:

post-drying treatment of the object within the dryer vessel by condensing of a portion of the steam mixed with evaporated moisture from the outlet of the vacuum ejector with a refrigerant and at a high-pressure to generate a cooling capacity to cool and/or freeze the object within the dryer vessel.

Assignments (4)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jan 23, 2020
From: CHUDNOVSKY, YAROSLAV
To: UTILIZATION TECHNOLOGY DEVELOPMENT, NFP
Reel/Frame 051598/0452 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jan 23, 2020
From: BUYADGIE, DMYTRO; BUYADGIE, OLEXIY
To: WILSON ENGINEERING TECHNOLOGIES, INC.
Reel/Frame 051598/0481 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jan 23, 2020
From: WILSON ENGINEERING TECHNOLOGIES, INC.
To: GAS TECHNOLOGY INSTITUTE
Reel/Frame 051598/0505 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jan 23, 2020
From: GAS TECHNOLOGY INSTITUTE
To: UTILIZATION TECHNOLOGY DEVELOPMENT, NFP
Reel/Frame 051598/0531 →
Continuity (2)
Provisional Application 62785769 · Dec 28, 2018
Related Publication 20200208335A1 · Jul 2, 2020
Cited By (2)
US 12,577,716 US 12,655,571