Removing particulates

• US 10,646,843 B2
• Filed: 09/07/2017
• Issued: 05/12/2020
• Est. Priority Date: 09/08/2016
• Status: Active Grant

• Current Assignee: Wilson Bio-Chemical Limited
• Original Assignee: Wilson Bio-Chemical Limited
• Inventors: Wilson, Thomas Steven
• Primary Examiner(s): Bui, Dung H
• Application Number:
  US15/697,611
• Publication Number:
  US 20180065099A1
• Time in Patent Office: 978 Days
• CPC Class Codes: B01D 29/00 Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor
• CPC Class Codes: B01D 45/08 by impingement against baffle separators
• CPC Class Codes: B01D 49/00 Separating dispersed particles from gases, air or vapours by other methods
• CPC Class Codes: B01J 3/002 Component parts of these vessels not mentioned in B01J3/004, B01J3/006, B01J3/02 - B01J3/08; Measures taken in conjunction with the process to be carried out, e.g. safety measures
• CPC Class Codes: B01J 3/04 Pressure vessels, e.g. autoclaves
• CPC Class Codes: B09B 3/45 Steam treatment, e.g. supercritical water gasification or oxidation

Abstract

In a solid waste treatment system comprising an autoclave (201) not having a particulate filter at its outlet, a method of removing particulates suspended in steam discharged from the autoclave following processing of solid waste is disclosed. The method includes discharging steam from the autoclave; routing the steam to the inlet (301) of a separation vessel (209) that further includes an outlet (303) and a baffle (302) between the inlet and the outlet; and collecting particulates (304) that drop from suspension in the steam at the bottom of the separation vessel. The baffle is configured so that steam is incident upon the baffle to reduce its flow velocity.

Claims

1. A method comprising providing a solid waste treatment system, further comprising providing an autoclave having a steam outlet, a particulate filter, removing particulates suspended in steam discharged from the steam outlet of the autoclave following processing of solid waste, the method comprising the steps of:

discharging steam from the autoclave via the steam outlet;

routing the discharged steam to an inlet of a separation vessel that further includes an outlet and a baffle between said inlet and said outlet, whereby the baffle is so configured so that steam is incident upon the baffle to reduce its flow velocity, and therein the particulate filter is provided after the outlet of the separation vessel to catch particulates in the steam exiting the separation vessel;

charging the autoclave with steam routed from a steam storage system via the steam outlet and then the inlet of the separation vessel, thereby forcing particulates caught in the filter to be removed therefrom and to drop to a bottom of the separation vessel; and

collecting particulates that drop from suspension in the steam and from said filter at the bottom of the separation vessel.

2. The method of claim 1, in which the baffle is configured to extend perpendicularly with respect to the flow of the steam at the inlet.

3. The method of claim 2, in which the baffle extends downwardly to force the steam on a U-shaped path.

4. The method of claim 1, in which the separation vessel further comprises a valve at the outlet of the separation vessel, and the method further comprises the step of:

closing the valve after charging the autoclave, so that the separation vessel is at the same pressure as the autoclave.

5. The method of claim 4, in which the separation vessel further comprises a pressure gauge to allow readings to be taken from the separation vessel, rather than the autoclave during processing of solid waste.

6. The method of claim 5, in which the separation vessel further comprises a purge valve at its base, and the method further comprises:

charging the separation vessel with steam; and

opening the purge valve to achieve blowdown of particulates collected at the bottom of the separation vessel.

7. The method of claim 6, in which a purge valve is located between the separation vessel and a blowdown vessel maintained at atmospheric pressure.

8. The method of claim 1, in which the solid waste is municipal solid waste and the particulates are glass.

9. A system comprising:

a solid waste treatment system, further comprising;

an autoclave having a steam outlet without a particulate filter;

a separation vessel having an inlet, an outlet, and a baffle between the inlet and the outlet;

piping between said steam outlet of said autoclave and the inlet of said separation vessel;

a steam storage system connected to the outlet of the separation vessel; and

a filter after the outlet of the separation vessel;

wherein;

steam exhausted from said autoclave is routed from said steam outlet of said autoclave through said piping, and through said separation vessel via the inlet and then the outlet;

the baffle is configured so that said steam exhausted from said autoclave is incident upon the baffle to reduce the flow velocity thereof, thereby causing particulates to drop from suspension in the steam and collect at a bottom of the separation vessel, whereafter any remaining particulates are caught in said filter; and

steam from said steam storage system to charge said autoclave is routed through the separation vessel via the filter and outlet and then the inlet, and through said piping to said steam outlet, whereby particulates caught in the filter are removed therefrom and drop to the bottom of the separation vessel.

10. The solid waste treatment system of claim 9, in which the baffle extends perpendicularly with respect to the flow of the steam at the inlet.

11. The solid waste treatment system of claim 10, in which the baffle extends downwardly to force the steam on a U-shaped path.

12. The solid waste treatment system of claim 9, in which the separation vessel further comprises a valve at the outlet of the separation vessel which is closed after charging the autoclave, so that the separation vessel is at the same pressure as the autoclave.

13. The solid waste treatment system of claim 12, in which the separation vessel further comprises a pressure gauge to allow pressure readings to be taken from the separation vessel, rather than the autoclave during processing of solid waste.

14. The solid waste treatment system of claim 13, in which the separation vessel further comprises a purge valve at its base, which, following charging of the separation vessel with steam, is opened to achieve blowdown of particulates collected at the bottom of the separation vessel.

15. The solid waste treatment system of claim 14, in which purge valve is located between the separation vessel and a blowdown vessel maintained at atmospheric pressure.

16. The solid waste treatment system of claim 9, in which the solid waste is municipal solid waste and the particulates are glass.