Powder cleaning systems and methods

Patent metadata

Field	Value
Publication number	US-11980880-B2
Application number	US-202117394631-A
Country	US
Kind code	B2
Filing date	Aug 5, 2021
Priority date	Nov 19, 2018
Publication date	May 14, 2024
Grant date	May 14, 2024

Abstract

A powder cleaning system can include a fluidized bed reactor configured to retain powder and fluidize the powder to remove adsorbate and/or other contaminants from the powder, and one or more gas sources configured to be in selective fluid communication with the fluidized bed reactor via at least one inlet line to selectively provide an inlet flow having one or more gases to the fluidized bed reactor to fluidize the powder with the one or more gases within the fluidized bed reactor. The system can include at least one outlet line in fluid communication with the fluidized bed reactor and configured to allow removal of outlet flow which comprises the adsorbate and/or other contaminants from the fluidized bed reactor.

First claim

What is claimed is:

1. A method for cleaning a powder, comprising:
fluidizing powder in a fluidizing bed reactor with an inlet gas to remove adsorbate and/or other contaminants to produce cleaned powder;
providing at least one inlet line;
providing one or more gas sources configured to be in selective fluid communication with the fluidized bed reactor via the at least one inlet line to selectively provide an inlet flow having one or more gases to the fluidized bed reactor to fluidize the powder with the one or more gases within the fluidized bed reactor; and
providing at least one outlet line in fluid communication with the fluidized bed reactor and configured to allow removal of outlet flow which comprises the adsorbate and/or other contaminants from the fluidized bed reactor;
wherein a bypass line is configured to fluidly connect the inlet line and a liquid trap to allow at least some gas in the inlet line to flow to a vent, wherein the bypass line includes a bypass valve configured to selectively allow bypass flow, and
wherein a pressure release valve is disposed in the inlet line to allow bleeding of pressure above a threshold pressure, wherein the pressure release valve is disposed downstream of the bypass line.

2. The method of claim 1 , wherein fluidizing powder includes flowing gas through the powder in a direction opposite to gravity.

3. The method of claim 1 , wherein the inlet gas includes at least one of argon (Ar), ammonia (NH 3 ), nitrogen (N 2 ), hydrogen (H 2 ), or helium (He).

4. The method of claim 1 , wherein fluidizing the powder is performed after at least one
of powder production, powder characterization and/or testing, and/or powder processing.

5. The method of claim 1 , wherein fluidizing powder further includes controlling a temperature and/or pressure of the inlet gas as a function of one or more powder characteristics.

6. The method of claim 5 , wherein the one or more powder characteristics include one or more of: powder type, particle size, powder chemistry, and/or amount of powder.

7. The method of claim 5 , wherein controlling a temperature and/or pressure of the inlet gas, includes:
at start up, controlling the bypass valve to move to an open position before or while controlling one or more fluid source valve and/or an inlet line valve to open to prevent a pressure spike in the fluidization bed reactor; and
at steady state operation, controlling the bypass valve to move to a closed position after steady state operation is reached to regulate pressure to the fluidization bed reactor.

8. The method of claim 5 , further comprising sintering the cleaned powder to form an additively manufactured article.

9. A method for cleaning a powder, comprising:
performing powder characterization to characterize a powder;
fluidizing the powder in a fluidizing bed reactor with an inlet gas to remove adsorbate and/or other contaminants to produce cleaned powder, wherein fluidizing the powder is performed after powder characterization;
providing at least one inlet line;
providing one or more gas sources configured to be in selective fluid communication with the fluidized bed reactor via the at least one inlet line to selectively provide an inlet flow having one or more gases to the fluidized bed reactor to fluidize the powder with the one or more gases within the fluidized bed reactor; and
providing at least one outlet line in fluid communication with the fluidized bed reactor and configured to allow removal of outlet flow which comprises the adsorbate and/or other contaminants from the fluidized bed reactor;
wherein a bypass line is configured to fluidly connect the inlet line and a liquid trap to allow at least some gas in the inlet line to flow to a vent, wherein the bypass line includes a bypass valve configured to selectively allow bypass flow, and
wherein a pressure release valve is disposed in the inlet line to allow bleeding of pressure above a threshold pressure, wherein the pressure release valve is disposed downstream of the bypass line.

10. The method of claim 9 , wherein fluidizing powder further includes controlling a temperature and/or pressure of the inlet gas as a function of one or more powder characteristics.

11. The method of claim 10 , wherein the one or more powder characteristics include one or more of: powder type, particle size, powder chemistry, and/or amount of powder.

Assignees

• Hamilton Sundstrand Corp

Inventors

• Mcgee Randolph Carlton
• She Ying

Classifications

• B01J8/24 Primary

  according to "fluidised-bed" technique (B01J8/20 takes precedence) · CPC title

• B01J8/006

  by filtration · CPC title

• B01J8/1818

  Feeding of the fluidising gas (B01J8/44 takes precedence) · CPC title

• B01J8/44

  Fluidisation grids · CPC title

• B22F1/14

  Treatment of metallic powder (mixing with lubricating or binding agents or with organic material B22F1/10) · CPC title