A method for generating an aerosol includes the step of guiding a gas which flows at supersonic velocity and which has input particles suspended therein in such a way that a compression shock occurs. The input particles are broken down into smaller output particles upon crossing the compression shoc
A method for generating an aerosol includes the step of guiding a gas which flows at supersonic velocity and which has input particles suspended therein in such a way that a compression shock occurs. The input particles are broken down into smaller output particles upon crossing the compression shock. A device for generating an aerosol is also provided.
대표청구항▼
1. A method for generating an aerosol, the method which comprises:providing a gas supplied with input particles; providing an enclosure having a cross-section continuously widening in a direction of flow and towards, an end of the enclosure to achieve a supersonic velocity; guiding the gas with the
1. A method for generating an aerosol, the method which comprises:providing a gas supplied with input particles; providing an enclosure having a cross-section continuously widening in a direction of flow and towards, an end of the enclosure to achieve a supersonic velocity; guiding the gas with the input particles and causing the gas to flow at the supersonic velocity to cause a compression shock to occur downstream of the end and outside of the enclosure; and breaking the input particles into output particles being smaller than the input particles by passing the input particles through the compression shock, generating the aerosol. 2. The method according to claim 1, which comprises providing the enclosure, as seen in the direction of flow, with the cross-section of the enclosure narrowing prior to widening in order to achieve a sonic velocity.3. The method according to claim 1, which comprises feeding the input particles to the gas while the gas is at rest.4. The method according to claim 1, which comprises feeding the input particles to the gas while the gas flows at subsonic velocity.5. The method according to claim 1, which comprises:providing the enclosure with a narrowing cross-section upstream of a widening cross-section as seen in a direction of flow; and providing the gas such that a pressure of the gas in a resting state upstream of the narrowing cross-section is between 1·105 Pa and 2.5·107 Pa. 6. The method according to claim 1, which comprises:providing the enclosure with a narrowing cross-section upstream of a widening cross-section as seen in a direction of flow; and providing the gas such that a pressure of the gas in a resting state upstream of the narrowing cross-section is between between 2·105 Pa and 2·106 Pa. 7. The method according to claim 1, which comprises:providing the enclosure with a narrowing cross-section upstream of a widening cross-section as seen in a direction of flow; and providing the gas such that a pressure of the gas in a resting state upstream of the narrowing cross-section is between 3·105 Pa and 1·106 Pa. 8. The method according to claim 1, which comprises:providing the enclosure with a narrowing cross-section upstream of a widening cross-section as seen in a direction of flow; and providing the gas such that a pressure of the gas in a resting state upstream of the narrowing cross-section is substantially 5·105 Pa. 9. The method according to claim 1, which comprises:providing the enclosure with a narrowing cross-section upstream of a widening cross-section as seen in a direction of flow; and providing the gas such that a temperature of the gas in a resting state upstream of the narrowing cross-section is between ?20° C. and 400° C. 10. The method according to claim 1, which comprises:providing the enclosure with a narrowing cross-section upstream of a widening cross-section as seen in a direction of flow; and providing the gas such that a temperature of the gas in a resting state upstream of the narrowing cross-section is between 0° C. and 50° C. 11. The method according to claim 1, which comprises:providing the enclosure with a narrowing cross-section upstream of a widening cross-section as seen in a direction of flow; and providing the gas such that a temperature of the gas in a resting state upstream of the narrowing cross-section is between 10° C. and 30° C. 12. The method according to claim 1, which comprises:providing the enclosure with a narrowing cross-section upstream of a widening cross-section as seen in a direction of flow; and providing the gas such that a temperature of the gas in a resting state upstream of the narrowing cross-section is between 20°0 C. and 25° C. 13. The method according to claim 1, which comprises providing the gas such that the gas includes at least one element selected from the group consisting of air, N2, O2, and CO2.14. The method according to claim 1, which comprises providing the input particles such that an average size of the input particles is between 20 μm and 200 μm.15. The method according to claim 1, which comprises providing the input particles such that an average size of the input particles is between 40 μm and 100 μm.16. The method according to claim 1, which comprises providing the input particles such that an average size of the input particles is between 45 μm and 60 μm.17. The method according to claim 1, which comprises providing the output particles such that an average size of the output particles is between 1 μm and 10 μm.18. The method according to claim 1, which comprises providing the output particles such that an average size of the output particles is between 2 μm and 5 μm.19. The method according to claim 1, which comprises providing the output particles such that an average size of the output particles is substantially 3 μm.20. The method according to claim 1, which comprises providing the input particles as droplets of a liquid.21. The method according to claim 20, which comprises providing water as the liquid.22. The method according to claim 20, which comprises providing the liquid as a carrier liquid for an agent.23. The method according to claim 22, which comprises providing the agent as a pharmacologically active agent.24. The method according to claim 22, which comprises providing the agent as a pharmacologically active inhalation therapy agent.25. The method according to claim 22, which comprises providing a solvent as the liquid.26. The method according to claim 25, which comprises providing an alcohol as the solvent.27. The method according to claim 20, which comprises providing a combustible liquid as the liquid.28. The method according to claim 27, which comprises providing a fuel as the combustible liquid.29. The method according to claim 1, which comprises providing at least some of the input particles as loosely linked particles selected from the group consisting of solid particles and semi-solid particles.
연구과제 타임라인
LOADING...
LOADING...
LOADING...
LOADING...
LOADING...
이 특허에 인용된 특허 (14)
Wagner William R. (Los Angeles CA), Atomizing shock wave precombustor.
Newhouse Michael T. (436 Queen Street South Hamilton ; Ontario CAX L8N 4A6) Baines W. Douglas (1675 Wedmore Way Mississauga ; Ontario CAX), Dry powder inhaler and process that explosively discharges a dose of powder and gas from a soft plastic pillow.
Von Rosenberg ; Jr. Charles W. (Belmont MA) Stickler David B. (Carlisle MA) Gannon Richard E. (Andover MA), Very-high-velocity entrained-bed gasification of coal.
Reilly, William J.; Ballard, Robert J.; Blease, Kevin J.; Ide, Stephen R., Dual extinguishment fire suppression system using high velocity low pressure emitters.
※ AI-Helper는 부적절한 답변을 할 수 있습니다.