Background
U.S. Pat. No. 4,216,741 to Owen R. Moss, discloses an exposure chamber in which a succession of trays serve as distributing means to achieve uniform concentration throughout the chamber of a gas which includes an additive, e.g. aerosol. While intended primarily for the exposure of experimental animals to a controlled atmosphere, it may be used substantially unchanged for other purposes, e.g. the exposure or treatment of plants or the treatment of materials, for example the smoking of meat or fish.
The chamber is characterized by an opening at one end, e.g. the top, and an outlet at the other end, e.g. the bottom. In this configuration the gaseous composition is introduced at the top and deflected towards the side walls of the chamber, trays are arranged horizontally within the chamber, spaced from the side walls and spaced from each other along the mid-plane of the chamber. The gaseous composition flows downwardly through both sets of passages. The trays serve to create a turbulence or circulating movement within the chamber which results in thorough mixing.
Summary of the Invention
We have now found that the chamber described above can be modified so that different compositions are present in different zones, but in which the composition is uniform within a given zone. We accomplish this by the provision of additional inlets, intermediate to the inlet and outlet of the chamber as described above. An intermediate section of the chamber (which is not used for exposure) serves as a mixing zone. For example, an aerosol of given concentration can be introduced at the top of the chamber. Substantially pure air or gas is introduced through the intermediate inlets. In the upper portion of the chamber, the aerosol has a substantially uniform concentration. In the lower portion, the concentration is lower, but also substantially uniform. For animal experiments the above arrangement is preferred. However, it will be understood that instead of introducing pure air at the auxiliary inlets an aerosol of higher concentration could be introduced so that the concentration in the lower portion of the chamber is greater than in the upper portion.
The number of plates or trays can be increased and the number of points of introduction of the auxiliary gas can also be increased so that several different concentrations may be present in a given chamber.
The system can be used for other purposes than as an exposure chamber. For example, in some chemical processes it may be desirable to produce a fluid flow the composition of which periodically changes along its path. The system as described could be used to introduce additional components at different points in the chamber.
As pointed out in the patent, the inlet can also, though less desirably, be at the bottom and the outlet at the top. Moreover, if the system is to be used for general gas or liquid mixing, the bulk flow can be horizontal and the "trays," now simply baffles, positioned vertically. The essential requirement is that they be substantially normal to the direction of bulk flow.
Detailed Description
The presently preferred embodiment of this invention is a modification of the animal exposure chamber shown and described in U.S. Pat. No. 4,216,741 referred to above. The disclosure of the patent, which is specifically incorporated herein by reference, illustrates the mechanical details of the chamber except where they are changed as shown in the drawings and described in the remainder of the specification of this case.
The chamber constituting the present invention, like that of the patent, includes a casing 2, having an air inlet 4 at its top and an air outlet 6, at or near the bottom. The upper wall 8 of casing 2 slopes downwardly and outwardly in all four directions from the inlet 4. Immediately beneath inlet 4 is a deflector 12 which directs air toward the sloping top wall 8.
Within the casing 2 are a series of animal cages 14, 16, 18 and 20, beneath which are catch pans 22, 24, 26 and 28. In the structure shown in the patent, the cages and their catch pans fill substantially the entire chamber. In the present case, however, there is an empty space in the portion where cages would have appeared between cage 14 and cage 16 and between cage 18 and cage 20. A "dummy catch pan" or baffle 30, 32, however, is provided above each of the cages 16 and 20. Catch pans 22 and 26 and baffles 30 and 32 are, like the catch pans of the reference patent, spaced from the walls of the chamber by distances which are small compared to the horizontal dimension of the pans, but great enough to supply sufficient air to pans downstream. Pans 24 and 28, however, are provided with baffle plates 34 and 36 to prevent flow of air between them and the sidewalls. Typical dimensions of the structure as defined thusfar, are disclosed in columns 4 and 5 of the referenced patent.
The novel feature of this invention is the introduction of secondary air. The means for doing this will now be described.
A secondary air distributor 38 is provided between catch pan 22 and baffle 30. Another secondary air distributor 40 is provided between catch pan 26 and baffle 32.
FIG. 3 is a perspective view of distributor 40. Distributor 38 is identical except it is reversed from left to right with respect to distributor 40. We have successfully used as a distributor a "sandwich" consisting of a porous sintered metal tube 42 between two inverted catch pans 44 and 46. The space between the edges nearest the center line of the chamber is closed, 48. The spaces between the other three edges are open and the downturned edges 50 serve to direct air downwardly along the sidewalls. We have found that this downward deflection of the air is important to prevent upward circulation which would dilute upstream air. Inlet tubes 52 and 54 are connected to porous tubes 42 and pass through the chamber walls.
The operation of the chamber is as follows: An aerosol of a given composition is introduced through inlet 4. It is deflected laterally by deflector 12 and downwardly and laterally by upper wall 8. Circulation above catch pans 22 and 26 produces a uniform composition in this volume. Part of the aerosol flows downwardly between pans 22 and 26 and the sidewalls 10, while another portion flows downwardly through the central portion of the chamber between the inner edges of pans 22 and 26. Secondary clean air is introduced through inlet tubes 52 and 54 to distributors 38 and 40, respectively. It is directed downwardly into the space between baffles 30 and 32 and the catch pans 22 and 26. A circulation takes place in this volume mixing the secondary air with the aerosol from above pans 22 and 26. The aerosol, now diluted by the secondary air, flows downwardly around baffles 30 and 32 into the space occupied by cages 16 and 20. Due to the presence of baffles 34 and 36 it can not escape around catch pans 24 and 28 and all flows downwardly between these catch pans and eventually out of the chamber through outlet 6.
Experimental Examples
In the experiments described below, a Battelle exposure chamber having the structure and dimensions described in the U.S. Patent referenced above was modified by removing the cages forming the middle layer and means were provided for introducing secondary air through sampling ports which were provided in doors 41, 43, 45 and the fourth door (not shown) of the above patent. This gave essentially the arrangement shown and described above in this specification. As will be noted, however, the specific means for introducing air was not always that shown and described above.
Example 1
In this series of experiments, the air introduction device was a downwardly directed Y-shaped pair of tubes provided just inside each of the four doors referred to above. An ammonium sulfate aerosol (0.4 .mu.m amad, GSD=1.7 to 2.0) was used. The aerosol was introduced into the chamber with a total air flow of 10 cfm=283 l/min. After a steady state concentration of 1 to 3 g/l was reached, one half of the total flow was introduced through the secondary inlets described above. Changes in concentration (in micro amperes) were measured with a sulfur analyzer (a linear relation exists between changes in micro amperes and concentration). In this experiment, a constant flow of 10 cfm was drawn off at outlet 6. A constant amount per minute of ammonium sulfate was introduced into the air sucked in at inlet 4. When the dilution air was "on," the same amount of ammonium sulfate was suspended in 5 cubic feet per minute of air introduced at inlet 4, and 5 cubic feet per minute of pure air was introduced in the empty portion of the chamber between pans 22 and 30 and between pans 26 and 32. The analysis was in each case at 2 cm above the middle of each of the cages 14, 16, 18 and 20 and centered on the length and width of the above cage. The results are shown on Table 1.
The following conclusions were drawn: When approximately one half of the total chamber flow is introduced as dilution air into the middle of the Battelle exposure chamber the following changes are observed:
1. The concentrations 2 cm above the middle of cage units 14 and 18 increase by 61 to 79 percent.
2. The concentration 2 cm above the middle of the cage units 16 and 20 decreases slightly (2 to 13 percent).
In order to determine the uniformity of the concentration in cage 20, a greater number of sampling probes was provided. As before, each was 2 cm above the middle of the cage. The position of the sampling probes and the analyses are shown in Table 2.
The following conclusions were drawn: With open tube dilution air lines, the concentration in cage 20 is reduced 8 to 15 percent. The concentrations 2 cm above the rear of the cage are 5 to 7 percent less than the concentrations above the middle.
Example 2
After a number of experiments using different dilution systems, that are shown and described above, that is to say, the porous sintered tube sandwiched between two catch pans, was found to give the best results. Using this improved system, a vapor of tetrachloroethylene was employed. It was introduced into the air by a hot wick vapor generator. A photoionization detector was used for measuring concentration. In this experiment, a total air-vapor flow of 283 l/m (10 cfm) was used with 141 l/m (5 cfm) introduced at inlet 4 and the balance of pure air is divided evenly between inlet tubes 52 and 54. A total of 36 sampling points was used. The distribution of the sampling points and the measured concentrations (in the recorder units) are shown on Table 3.
The following conclusions were drawn: A factor of two in concentration was maintained between the top level (cages 14 and 18) and the bottom level (cages 16 and 20). The uniformity at the top level was within 5 percent and the bottom level was within 10 percent. These tests were made to show viability of the approach and not to find the optimal configuration of the sintered tube-catch pan sandwich. The two-concentration-level system is inherently safe. Should the dilution air system fail, the missing air is automatically and passively made up at the top inlet of the chamber causing the concentration in the chamber to fall to the lower of the two values.
While the animal exposure chamber described in the detailed description above constitutes the best mode in which we have up to now contemplated applying the invention, there are various embodiments that can be used. Considering only the animal exposure chamber, it can be provided with a greater number of cages and more than one inlet level for secondary air, so that three or more concentrations may be provided in a single chamber. As stated in the referenced patent, the flow of air may, less desirably, be from the bottom to the top (with certain structural changes described in that patent). The chamber, virtually without change, can be used for purposes other than the exposure of experimental animals. For example, it may be used for the exposure or treatment of plants, the smoking or other curing of meat, fish, fruit, vegetables and so forth.
The invention may also be applied in more unrelated fields. It may be used to produce a stream of fluid, either gaseous or liquid, which varies in composition along its length, for example, in chemical processes. When used for fluid blending without exposure of animals, plants, or materials, the chamber may be in either of the orientations referred to above, or it may be positioned on its side, relative to the position shown in the drawings, so that the flow between inlet 4 and outlet 6 is horizontal or in any other desired direction.
We therefore, wish our invention to be limited solely by the scope of the following claims.