Method to provide accurate fluid delivery
US-2024307907-A1 · Sep 19, 2024 · US
US9827382B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9827382-B2 |
| Application number | US-201615011906-A |
| Country | US |
| Kind code | B2 |
| Filing date | Feb 1, 2016 |
| Priority date | Jul 16, 2010 |
| Publication date | Nov 28, 2017 |
| Grant date | Nov 28, 2017 |
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A medical hand-held device, in particular an atomizer, for dispensing a liquid pharmaceutical preparation from a container with a discharge nozzle for the pharmaceutical preparation and located upstream from the discharge nozzle there is a multiple-stage filter system.
Opening claim text (preview).
The invention claimed is: 1. A device for administering a liquid medical formulation, comprising: at least one nozzle opening ( 12 e ) for receiving the liquid medical formulation in a flow path through the device and expelling the liquid medical formulation from the device, a container ( 3 ) holding and sourcing the liquid medical formulation into the flow path, a very fine filter ( 12 f ) formed by a microstructured component ( 12 ) arranged upstream of the at least one nozzle opening ( 12 e ) in the flow path and operating to filter the liquid medical formulation prior to the at least one nozzle opening ( 12 e ), a fine filter ( 28 ) arranged upstream of the microstructured component ( 12 ) in the flow path of the liquid medical formulation and operating to filter the liquid medical formulation prior to the very fine filter ( 12 f ), a pre-filter ( 27 ) arranged upstream of the fine filter ( 28 ) in the flow path of the liquid medical formulation and operating to filter the liquid medical formulation prior to the fine filter ( 28 ), wherein: the pre-filter ( 27 ) is of a relatively course filtering characteristics as compared with the fine filter ( 28 ) such that the pre-filter ( 27 ) prohibits particles of greater size that a first threshold from passing therethrough but permits particles of less than the first threshold to pass to the fine filter ( 28 ), the fine filter ( 28 ) is of a relatively fine filtering characteristic as compared with the pre-filter ( 27 ) and a relatively course filtering characteristic as compared with the microstructured component ( 12 ) such that the fine filter ( 28 ) prohibits particles of greater size that a second threshold from passing therethrough but permits particles of less than the second threshold to pass to the microstructured component ( 12 ), and the microstructured component ( 12 ) is of a relatively very fine filtering characteristic as compared with the fine filter ( 28 ) such that the microstructured component ( 12 ) prohibits particles of greater size that a third threshold from passing therethrough but permits particles of less than the third threshold to pass to the at least one nozzle opening ( 12 e ), wherein the pre-filter ( 27 ), the fine filter ( 28 ), and the very fine filter ( 12 f ) of the microstructured component ( 12 ) each have a different, respective pore size and are arranged so that the respective pore size decreases in the direction of flow. 2. The according to claim 1 , characterized in that pre-filter ( 27 ), fine filter ( 28 ) and very fine filter ( 12 f ) consist of different materials. 3. The according to claim 1 , characterized in that at least one of the pre-filter ( 27 ) and the fine filter ( 28 ) is made of sintered metal comprising metal particles that have been compressed into a fine-pored structure. 4. The according to claim 3 , characterized in that the sintered metal is titanium. 5. The according to claim 3 , characterized in that the pore sizes of the fine-pored structure are less than 5 microns. 6. The according to claim 1 , characterized in that the pre-filter ( 27 ) is a plastics filter, and the microstructured component ( 12 ) is made of a glass/silicon composite. 7. The according to claim 1 , characterized in that the fine filter ( 28 ) is a filter the mode of action of which is determined predominantly by adsorption effects and less by size exclusion, while particles from a liquid flowing through the fine filter are able to accumulate on the surface of the filter as a result of intermolecular interactions. 8. The according to claim 1 , characterized in that an adsorption filter ( 32 ) is arranged in the flow path between pre-filter ( 27 ) and very fine filter ( 12 f ), the mode of action of the adsorption filter being characterized in that particles from a liquid flowing through the filter are able to accumulate on the surface of the filter as a result of intermolecular interactions. 9. The according to claim 8 , characterized in that the adsorption filter ( 32 ) is embodied as a filter disc which is frictionally secured by its edge. 10. The according to claim 9 , characterized in that the edge of the filter disc is held either by a component that seals off or fixes the microstructured component ( 12 ) or the nozzle in its installed position, or by the microstructured component ( 12 ) or the nozzle itself, or is clamped in position between the pre-filter ( 27 ) and fine filter ( 28 ). 11. The according to claim 8 , characterized in that the adsorption filter ( 32 ) is arranged as an independent component either between the pre-filter ( 27 ) and the fine filter ( 28 ) or between the fine filter ( 28 ) and the very fine filter ( 12 f ). 12. The according to claim 8 , characterized in that the adsorption filter ( 32 ) is made of glass, cellulose, carbon or polymer fibers. 13. The according to claim 8 , characterized in that the adsorption filter ( 32 ) comprises a surface functionalized with aluminium oxide. 14. The according to claim 8 , characterized in that the adsorption filter ( 32 ) has a surface functionalized with quaternary ammonium groups. 15. The according to claim 1 , characterized in that pre-filter ( 27 ) and fine filter ( 28 ) have a circular-cylindrical or at least partially conical configuration. 16. The according to claim 1 , characterized in that the liquid medical formulation that is to be administered contains a substance with a low vapor pressure or an alcoholic compound. 17. The according to claim 1 , characterized in that the liquid medical formulation that is to be administered has a pH of between 3.5 and 9. 18. The according to claim 1 , characterized in that the liquid medical formulation is delivered as an inhalable aerosol. 19. The according to claim 1 , characterized in that the device contains a pressure chamber ( 11 ) and the filters are arranged between the pressure chamber ( 11 ) and the at least one nozzle opening ( 12 e ). 20. The according to claim 1 , characterized in that the device comprises a central part ( 23 ) in which pre-filter ( 27 ) and fine filter ( 28 ) are arranged downstream of a pressure chamber ( 11 ) or a metering chamber. 21. The according to claim 20 , characterized in that pre-filter ( 27 ) and fine filter ( 28 ) are held in the central part ( 23 ) without any additional components for securing them by a reduction in the internal cross-section formed by the central part itself ( 23 ), and/or by a press-fit. 22. A method of assembling a device according to claim 19 , characterized in that fine filter ( 28 ) and pre-filter ( 27 ) are inserted into a central part ( 23 ) through what is to be the pressure chamber ( 11 ) and the insertion opening is closed off by the piston of a pressure generator ( 5 ) or by a connecting element formed as a hollow piston ( 9 ) for subsequently withdrawing liquid ( 2 ) from a container ( 3 ).
Membranes separating the content remaining in the container from the atmospheric air to compensate underpressure inside the container · CPC title
Means for counting the number of dispensing strokes · CPC title
Piston pumps (B05B11/1087, B05B11/1088, B05B11/109 take precedence) · CPC title
being first hold in a loaded state by locking means or the like, then released (B05B11/1092 takes precedence) · CPC title
of the injector type · CPC title
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