Nebulizer

• US 4,268,460 A
• Filed: 03/05/1980
• Issued: 05/19/1981
• Est. Priority Date: 12/12/1977
• Status: Expired due to Term

• Current Assignee: Warner-Lambert Company (Pfizer Inc.)
• Original Assignee: Warner-Lambert Company (Pfizer Inc.)
• Inventors: Boiarski, Anthony A., Luce, Ross G.
• Primary Examiner(s): Lutter, Frank W.
• Assistant Examiner(s): Clements, Gregory N.
• Application Number:
  US06/127,350
• Time in Patent Office: 440 Days
• Field of Search: 261/1, 261/78 A, 261/DIG. 48, 261/DIG. 65, 128/200.16, 128/200.21, 239/338
• US Class Current: 261/1
• CPC Class Codes: A61M 11/001 Particle size control
• CPC Class Codes: A61M 11/06 of the injector type
• CPC Class Codes: A61M 16/14 by mixing different fluids, one of them being in a liquid phase
• CPC Class Codes: Y10S 261/48 Sonic vibrators
• CPC Class Codes: Y10S 261/65 Vaporizers

Abstract

A nebulizer for use in connection with a lung ventilating system characterized in providing a dual stage atomization of medicament carrying liquid. A first stage develops an aerosol exhibiting an initial, relatively larger average liquid particle size which is introduced to a chamber at a given stagnation pressure. From that chamber, a second atomization is carried out by passing the gas entrained liquid particles through a knife edge orifice to produce a rapid expansion free-jet flow and consequent particle breakdown to achieve a desired particle size distribution.

Claims

1. Nebulizer apparatus, connectable with a source of gas and with a liquid source comprising:

a first atomizer stage chamber for simultaneously communicating with a source of pressurized gas and with said source of liquid for forming by the Bernoulli effect a first particulate dispersion of said liquid entrained with said gas, the liquid particles of said first particulate dispersion exhibiting an average diameter, D₁, and a surface tension, S, and said gas exhibiting a density ρ

g;

a containment chamber embodying a second atomizer stage communicating through an input aperture narrower than the chamber with said first atomizer stage and having an input zone for receiving said first particulate dispersion at a stagnation pressure, P_o, and including a knife-edge exit orifice having diameter, d_o, to effect the expulsion through said exit orifice of said first particulate dispersion to impart supersonic velocities to said gas under flow conditions according to the expression;

space="preserve" listing-type="equation">o.sub.g u.sub.r.sup.2 ≧

W.sub.e S/D.sub.I, where

u_r is the relative velocity between a given said liquid particle and the velocity of said gas, and W_e is Weber number of value effective to effect a breakdown of said liquid particles to form a second gas entrained particulate dispersion of said liquid having an average particle diameter, D_S, less than said diameter, D_I ; and

a flexible tube communicating at one end with a source of gas under relatively low positive pressure, at the other end with a mouthpiece, and between the ends with said exit orifice whereby the second gas entrained particulate dispersion and low positive pressure gas are delivered to the mouthpiece.

2. The apparatus of claim 1 in which said Weber number, W_e, has a value with respect to a critical value thereof, W_e.sbsb.c, selected to effect said particle breakdown by a stripping mechanism, in accordance with the expression:

space="preserve" listing-type="equation">W.sub.e /W.sub.e.sbsb.c ≧

1.

3. The apparatus of claim 1 in which:

said liquid particles of said first dispersion exhibit a characteristic particle oscillation period, τ

; and

said second atomizer stage is configured for developing a barrel shock region adjacent said exit orifice having an extent sufficient to effect a supersonic velocity gas breakdown influence over said particles for an action time interval, t_a, equal to or greater than said oscillation period, τ

.

4. The apparatus of claim 1 in which the value of said exit orifice diameter, d_o, is selected to derive a liquid particle conversion efficiency, ε

, of at least about fifty percent.

5. The apparatus of claim 4 in which said stagnation pressure, P_o, is about 50 p.s.i.g.

6. The apparatus of claim 1 including means for effecting the passage of said pressurized gas into said first chamber to establish a flow therethrough in a predetermined direction;

means defining a nozzle having an outlet communicating in liquid flow relationship with said liquid source and oriented within said first chamber to deliver said liquid within said pressurized gas flow to effect the said formation and entrainment of droplet particles exhibiting said average particle diameter, D_I .

7. The apparatus of claim 6 wherein said first chamber outlet means comprises a conical duct converging to an orifice, said orifice being positioned for effecting the passage of said first particulate dispersion into said second atomizer stage means input zone.

8. The apparatus of claim 1 wherein said containment chamber is configured to define said input zone, said exit orifice being situated remotely from said input aperture.

9. The apparatus of claim 1 in which said first chamber and said containment chamber are formed in mutual adjacency within a sanitary housing.

10. The apparatus of claim 9 in which said means defining said nozzle is threadably connected with said housing so as to permit the adjustable positioning thereof with respect to said outlet means.