Gas injection for de-agglomeration in particle coating reactor
A method of coating particles includes dispensing particles into a vacuum chamber to form a particle bed in at least a lower portion of the chamber that forms a half-cylinder, evacuating the chamber through a vacuum port in an upper portion of the chamber, rotating a paddle assembly such that a plurality of paddles orbit a drive shaft to stir the particles in the particle bed, injecting a reactant or precursor gas through a plurality of channels into the lower portion of the chamber as the paddle assembly rotates to coat the particles, and injecting the reactant or precursor gas or a purge gas through the plurality of channels at a sufficiently high velocity such that the reactant or precursor a purge gas de-agglomerates particles in the particle bed.
1. A method of coating particles, comprising:
dispensing particles into a vacuum chamber to form a particle bed in at least a lower portion of the vacuum chamber that forms a half-cylinder;
evacuating the vacuum chamber through a vacuum port in an upper portion of the vacuum chamber;
rotating a paddle assembly such that a plurality of paddles orbit a drive shaft to stir the particles in the particle bed; and
injecting a first gas through a plurality of channels into the lower portion of the vacuum chamber at a first flow rate and through the particle bed as the paddle assembly rotates to coat the particles,
wherein the particles substantially stay in the particle bed during the injecting of the first gas through the plurality of channels and through the particle bed and the rotating of the paddle assembly such that the plurality of paddles orbit the drive shaft to stir the particles in the particle bed.
2. The method claim 1 , wherein the first gas is a precursor or reactor gas, and wherein the first flow rate is sufficient to de-agglomerate the particles in the particle bed during a deposition process.
3. The method of claim 1 , further comprising:
injecting a second gas through the plurality of channels into the lower portion of the vacuum chamber at a second flow rate and through the particle bed as the paddle assembly rotates.
4. The method of claim 3 , wherein the second gas is an inert carrier gas, and wherein the second flow rate of the inert carrier gas through the plurality of channels into the lower portion of the vacuum chamber prevents back-streaming of particles into the plurality of channels.
5. The method of claim 4 , wherein the second flow rate of the inert carrier gas causes de-agglomeration of the particles in the particle bed during a purging process.
6. The method of claim 3 , wherein a direction of rotation of the plurality of paddles as the plurality of paddles orbit the drive shaft comprises a component in a same direction as respective flows of the first gas and second gas into the lower portion of the vacuum chamber.
7. The method of claim 3 , wherein injecting the first gas and the second gas through the plurality of channels into the lower portion of the vacuum chamber comprises injecting the first gas and the second gas such that a flow of the first gas and the second gas is toward a bottom portion of the vacuum chamber.
8. A reactor for coating particles, comprising:
a stationary vacuum chamber to hold particles to be coated in a particle bed;
a paddle assembly including a rotatable drive shaft and one or more paddles in the vacuum chamber, the one or more paddles connected to the drive shaft such that rotation of the drive shaft by a motor stirs the particles in the particle bed;
a gas injection assembly to a deliver a first gas into a lower portion of the vacuum chamber;
at least one flow regulator to control a first flow rate of the first gas into the lower portion of the vacuum chamber; and
a controller configured to:
cause gas injection assembly to inject the first gas into the lower portion of the vacuum chamber and through the particle bed at a first flow rate as the paddle assembly rotates to coat the particles,
wherein the particles substantially stay in the particle bed during the injecting of the first gas through the lower portion of the vacuum chamber and during the rotating of the paddle assembly such that the one or more paddles stir the particles in the particle bed.
9. The reactor of claim 8 , wherein the first gas injected by the gas injection assembly is a precursor or reactor gas, and
wherein the flow regulator is operable to control the flow rate of the precursor or reactor gas into the lower portion of the vacuum chamber that is sufficient to de-agglomerate the particles in the particle bed during a deposition process.
10. The reactor of claim 8 , wherein the gas injection assembly is configured to inject a second gas through a plurality of channels into the lower portion of the vacuum chamber at a second flow rate and through the particle bed as the paddle assembly rotates.
11. The reactor of claim 10 , wherein the second gas is an inert carrier gas, and
wherein the flow regulator is operable to control a second flow rate of the inert carrier gas through the plurality of channels into the lower portion of the vacuum chamber prevents back-streaming of particles into the plurality of channels.
12. The reactor of claim 11 , wherein the second flow rate of the inert carrier gas causes de-agglomeration of the particles in the particle bed during a purging process.
13. The reactor of claim 10 , wherein a direction of rotation of the one or more paddles as the one or more paddles orbit the drive shaft comprises a component in a same direction as respective flows of the first gas and second gas into the lower portion of the vacuum chamber.
14. The reactor of claim 10 , wherein the gas injection assembly is configured to inject the first gas and the second gas through the plurality of channels into the lower portion of the vacuum chamber such that a flow of the first gas and a flow of the second gas is toward a bottom portion of the vacuum chamber.