referring more specifically to the drawings , for illustrative purposes the present invention is embodied in the apparatus generally shown in fig1 and shown in detail in fig2 through fig5 . it will be appreciated that the apparatus may vary as to configuration and as to details of the parts without departing from the basic concepts as disclosed herein . referring to fig1 the nebulizer 10 the present invention generally includes a housing 12 which serves as a reservoir with a lower fluid region 14 for containing fluid and an upper aerosol region 16 for containing nebulized fluid or aerosol generated by the device . the device accepts gas injected into gas inlet port 18 , nebulizes fluid contained in lower fluid region 14 and exhausts the resultant aerosol through aerosol outlet port 20 which communicates with upper aerosol region 16 . referring now to fig2 through fig5 coupled to housing 10 is a primary injector 22 which serves as a flow generating means . primary injector 22 , which serves as a gas injector , generally comprises a cylindrical body in which a primary orifice chamber 24 is interiorly disposed . one end of primary orifice chamber 24 opens toward gas inlet port 18 , while the other end tapers to form a primary orifice 26 which extends from primary orifice chamber 24 to a gas outlet port 28 at the end of primary injector 22 . the exterior diameter of primary injector 22 is reduced in the area of primary orifice 26 to form a nozzle 30 . radially disposed about gas outlet port 28 is a nozzle face 32 which is preferably a substantially planar circularly disposed surface . compressed gas entering gas inlet port 18 is conducted through primary orifice chamber 24 and primary orifice 26 where it exits at gas outlet port 28 as a jet stream at the speed of sound and at a volumetric rate primarily controlled by the gas pressure and the diameter of primary orifice 26 . the central portion of primary injector 22 includes a plurality of splines 34 radially projecting from its outer surface . an annular flange 36 projects outward from primary injector 22 , and is disposed between splines 34 and nozzle 30 . a secondary injector 38 serves as a means to draw fluid from lower fluid region 14 and mix it with gas from primary injector 22 . secondary injector 38 , which serves as a fluid injector , includes a central bore 40 which forms a secondary chamber 42 into which nozzle 30 extends . flange 36 is so constructed as to mate firmly with a surface of secondary injector 38 surrounding bore 40 thereby sealing secondary chamber 42 against the escape of gas or fluid . secondary injector 38 includes a secondary orifice 44 which extends from a secondary orifice inlet port 46 in secondary chamber 42 to a secondary orifice outlet port 48 which opens into upper aerosol region 16 . radially disposed about secondary orifice inlet port 46 is a secondary orifice inlet face 50 which is preferably a generally planar circularly disposed surface . radially disposed about secondary orifice outlet port is a secondary orifice outlet face 52 which is preferably a generally planar circularly disposed surface having a diameter of at least 7 . 6 millimeters . preferably , nozzle face 32 and secondary orifice inlet face 50 are coplanar as shown . in addition , primary orifice 26 and secondary orifice 44 are aligned along a common central axis . as can be seen in fig4 when primary injector 22 is inserted into secondary injector bore 40 , nozzle 30 extends into secondary chamber 42 and is spaced relation thereto thereby forming an inter - orifice gap 54 between nozzle face 32 and secondary orifice inlet face 50 . in this manner , inter - orifice gap 54 separates primary orifice 26 from secondary orifice 44 and creates an area for fluid transfer to occur . therefore , secondary chamber 42 generally comprises the area between nozzle face 32 and secondary orifice inlet face 50 , as well as the area between the circumferential outer surface of nozzle 30 and the circumferential inner surface of bore 40 since the outer diameter of nozzle 30 is less than the inner diameter of bore 40 . secondary injector 38 also includes a fluid inlet port 56 which communicates with secondary chamber 42 . a tube 58 coupled to fluid inlet port 56 and extending into lower fluid region 14 serves as a fluid conduit . a non - spherical stagnation baffle 60 is positioned in upper aerosol region 16 and coupled to secondary injector 38 in proximity to secondary orifice outlet port 48 . preferably , stagnation baffle 60 is a cylindrical - shaped rod which is aligned with secondary orifice outlet port such that its longitudinal axis is perpendicular to the longitudinal axis of secondary orifice 44 . a cap 62 and taper 64 at the upper and lower ends of stagnation baffle 60 , respectively , assist in proper alignment . the distance between the surface of stagnation baffle 60 and secondary orifice outlet face 52 establishes a spray gap 66 which separates secondary orifice outlet port 48 from stagnation baffle 60 . when gas is injected into gas inlet port 18 at pressures ranging from 103 to 343 kilopascals ( 15 to 50 pounds per square inch gauge pressure ) exits primary orifice 26 , it creates a gas jet stream flowing at the speed of sound ( sonic flow ) which passes through the inter - orifice gap 54 and rapidly expands into the larger diameter secondary orifice 44 . it should be noted that , while sonic flow is preferred , the apparatus can also operate at lower pressures which do not result in sonic flow of the gas jet stream . the expanding jet of gas entering the secondary orifice 44 creates a negative pressure in secondary chamber 42 which , being less than atmospheric pressure , creates a vacuum causing fluid to be drawn into secondary chamber . the stream of fluid is sheared in the inter - orifice gap in the area immediately surrounding secondary orifice inlet port 46 and broken into droplets of typically less than 100 micrometers in diameter which become entrained in the gas stream and mixed with the gas flowing through the secondary orifice 44 . the atomized fluid droplets then flow through secondary orifice 44 and spray gap 66 , eventually striking stagnation baffle 60 where the larger droplets are further fragmented . fluid droplets generally smaller than 4 micrometers in diameter are swept in the gas stream which exits spray gap 66 and forms the inhalable aerosol . the larger droplets accumulate on stagnation baffle 60 and fall back into lower fluid region 14 under the urge of gravity . in order to assure the correct operation of the nebulizer and achieve the benefit of scalability to produce a dense cloud of uniformly small droplets at any specified flow rate or output volume , several specifications are required . first , the diameter of stagnation baffle 60 must fall between approximately 1 . 52 millimeters and approximately 4 . 83 millimeters . second , the inter - orifice gap 54 must fall between approximately 0 . 10 millimeters and approximately 0 . 41 millimeters . third , the secondary orifice 44 must have a length to diameter ratio between approximately 0 . 3 and approximately 1 . 7 . fourth , the ratio of the diameter of secondary orifice 44 to primary orifice 26 must be between approximately 1 . 75 and approximately 3 . 25 . lastly , the spray gap 66 must be between approximately 0 . 23 millimeters and approximately 0 . 46 millimeters . by maintaining spray gap 66 within this range , capillarity ( capillary action ) will aid in the removal of droplets which accumulate on stagnation baffle 60 . as a result of capillarity , the droplets will move toward the end of spray gap 66 where the fork - or rabbit ear - shaped standoffs ( fig1 and 5 ) used to couple stagnation baffle 60 to secondary injector 38 , and eventually fall back into lower fluid region 14 under the urge of gravity . by adjusting any of the foregoing parameters its boundaries , the present invention is fully scalable to produce a selected flow rate or output volume for the aerosol generated . a general optimization of the foregoing parameters can be achieved for operation at an input gas pressure of approximately 137 . 5 to 344 kilopascals ( 20 to 50 pounds per square inch gauge pressure ), an output flow rate ranging from less than 1 liter per minute to approximately 2 . 25 liters per minute , and an output density ranging from approximately 35 to 55 microliters of aerosol per liter of gas . that optimization results where inter - orifice gap 54 is approximately 0 . 2 millimeters , spray gap 66 is approximately 0 . 33 millimeters , the diameter of stagnation baffle 60 is approximately 3 . 18 millimeters , the length to diameter ration of secondary orifice 44 is approximately 1 . 38 and the ratio of the diameter of secondary orifice 44 to primary orifice 26 is approximately 2 . 36 . preferably the present invention is fabricated from a lightweight material such as plastic . housing 12 is preferably transparent so that the amount of fluid in lower fluid region 14 can be readily observed . it should also be noted that housing 12 can be fitted with a port for injection of auxiliary medicines , and such a port could be coupled to an intravenous drip line or the like . it can be seen , therefore , that the present invention provides a nebulizer which can produce the lower flow rates required for inhalation therapy of infants and children , and can be directly scaled to provide any flow rate or output volume within any given pressure range . although the description above contains many specificities , these should not be construed as limiting the scope of the invention but as merely providing illustrations of some of the presently preferred embodiments of this invention . thus the scope of this invention should be determined by the appended claims and their legal equivalents .
a nebulizer for generating high concentrations of inhalable medicinal aerosols over a wide range of flow rates and mass outputs for medical inhalation therapy applications . a primary orifice , secondary orifice , inter - orifice gap , stagnation baffle , and spray gap are scalable within defined parameters to provide any desired flow rate or mass output . the nebulizer is ideally suited for inhalation therapy of infants and children and can provide aerosols with flow rates ranging from less than 1 liter per minute to approximately 3 liters per minute at normal compressed gas pressures . the design parameters can also be scaled within defined limits to produce greater flows for treatment of adults or for use in other applications requiring high volumetric flow rates .