The present invention refers to an apparatus for the oxidation of particles suspended in the air, comprising a plura lity of ducts open at both ends, within which is disposed a resistiwe wire.

Brazilian patent application PI 8302255 of the same inventor discloses an air sterilization system using a high temperature gradient ducts, inside which resistive nickel- -chromium wires are axially introduced, the ducts being prefera bly cylindrical.

Experiments have demonstrated that such a system is viable only if some parameters are observed which are not considered in said application. The present, invention aims to provide an improvement of said system, in order to permit a rapid oxidation of particles suspended in the air, under application of a relatively low total power and with high efficiency.

This aim is achieved by the invention due to the fact that said ducts 5 have a maximum volume of 10 m ³ and amaximum cross section area of 1 cm , the length and cross section being dimensioned in such a way that the minimum permanence time of the air mass within the ducts 5 is 0,01 second and the minimum power density within the ducts is 50 KW/ m ³ . Experiments have shown that by maintaining the above parameters it is possible to achieve a sterilization with high efficiency and low costs in closed ambience.

The present invention provides a new way of aσheiving the oxidation of particles suspended in the air in ambienee,

should they be alive forms or inaminated, reducing also the relative humidity in a surprisingly efficient manner. The high oxidation rate, which is achieved inside the ducts, promotes the elimination of microorganisms from the air by means of the oxidation of the proteins as well as eliminates odors and oxidates some molecular forms of gases such as CO (toxicant) transforming it C0 ₂ (inert to humam organism) . It refers to an improvement of extreme importance on the asepsis methods, polu- tion control, conservation of works of art, conservation of agricultural products and the like.

According to a preferred embodiment, the present invention is basically composed by three systems: the first one is a refractory material block provided with more than a hundred cappilaries whereby a high power density is generated; the second one is a control system and the third is a propulsive system.

Those systems are interconnected in such a way that the set works as an only system.

A preferred embodiment consists- in executing the ducts as cylindrical perforations in a refractory block disposed in¬ side a box, which is provided below the block, with a fan for controlling the air flow, the fan being actuated by means of an electronic circuit, which, by its turn, is connected to a temperature sensor disposed within the block. This embodiment will be described afterwards in more detail.

An embodiment example utilizes a refractory material block of 7 cm thickness in which 120 trespassing cylindrical ducts withabout2,0 to 2,5 mm diameter are provided, whereby a NiCr filament with a resistivity of 24 i /m is axially passed through the ducts, dissipating a total power of 500 W. The power dissipated in each duct is 3,5 W for a total lenght to the NiCr filament of 10m.

The refractory material block has, preferably, the following weight composition: 45% Si0 ₂ , 42% Al ₂ 0 ₃ , 4% ZrO-, 1% Ti0 ₂ , 6% CaO and 2% MgO. This refractory material has a thermal conductivity coefficient K = 0,300 cal/h°C m/m ² at a temperatu re of 600°C.

Effecting the calculation for this embodiment example, it is found: a) The power density within each duct (up) :

_.

- 3 -

up = duct power/duct volume, where duct power = 3,5W duct"volume = ^* U D ² x.L = π χ(2x10 ^""3 ) ~ χ 7 x 10~

4 4 = 2,2x10 ^"7 m ³ up = 15,90 x 10 W/m ³ , what represents an extra narily high, value. b) Energy density transformed within each duct (u uEtd = up x t, where t is the average permanen time of the air mass within the duct. For t=0 uEtd = 1 ,59 x 10 ⁶ J/m ³ Considering the importance of the radiation in th infrared band in the oxidation process of particle: c) Energy density in the infrared band (uEir) : uEir = 1,59 x 10 ⁴ J/m ³ , assuming that 1% of uEtd is in the infrared ba d) Energy of each photon generated with the wave lenght

Js

m/°

T

T = 500°C = 773°K then Emax = 6,'63 x 10~ ⁴ X 3 x 10 ⁸

T ,898 x 10 ^~3 /773 e) Number of photons peorT cubic meter (N \ _' max) :

N = 3,00 x 10 photons/m ³ , which is a ra high number. Associating those results to the scientific knowle one verifies that the air mass carrying suspended particles those particles oxidated in an undoubtful way when submitted conditions of thermal power and infrared power together with Nickel of the filament which acts as a catalyst.

♦ The control of the air flow through the ducts, has objective of making the permanence time of the air mass as w as the temperature within the ducts not affected by the envi ent conditions. This is done by means of a signal generate

a Constantan Iron sensor, i.e., a thermocouple (other kinds of thermal sensors can be used) which generates a control signal bymeans of an electronic circuit whose outlet controls the air flow of a fan. The apparatus will be described, based on an embodi¬ ment example represented on the drawings. The figures show schematically: figure 1 a side sectioned view of the apparatus; figure 2 the basic electric circuit of the apparatus of figure 1 ; igure 3 a graphic of an experiment σarried by the Brazilian Ministry of Health.

The apparatus represented in figure 1 is disposed within a metal box 7 provided with superior 1 and inferior 12 protecting network screen. The refractory block 4, within which are executed the small volume ducts 5, is fixed to the box 7 by fixing pieces 8. The piece 6 serves for the fixation of the electric wire, which is passed through the ducts 5 in a tensive way in the art of a "needle-work", ^" the wire not being " -represented in figure 1 in order to simplify it. ^*

The electronic control circuit 10 is connected to a thermal sensor 9 which is allocated within the block 4, although it is also possible to dispose the sensor on the out¬ let of the ducts. The control system of the fan motor 11 can = be executed as a continuous control, but in this example it is executed as an ON-OFF type with hysterisis, as represented in figure 2.

A perforated inox steel 3, provided with perforations with a diameter ofabout2mm, is fixed within the box 7 above the block 4, in order to actuate as heat exchanger, cooling the air that leaves the box, a thermostate or thermal circuit breaker 2 being disposed above the perforated plate 3 to turn off the apparatus if the temperature of the air leaving the box..7 exceeds a predetermined limit. A fuse 13 guarantees the apparatus against possible overload.

On the scheme represented on figure 2 there are provided a Slow-Blow type fuse 14 of 5 amperes, an ON-OFF type switch 15, a thermostate 16 with disarm at 70°C, a Ni-Cr

filament 17 of 24,2Jf2/m x 500 for the 110V version, a thermal sensor 9 of the thermocouple type, as well as the fan's motor 11 and the electronic control circuit 10.

The electronic control circuit 10 operates in such a - way, that when it receives a signal from the thermal sensor 9 indicating that the temperature on the block 4 reached a pre¬ determined maximum value, it activates the fan's motor 11, in¬ creasing the pressure P1 below the block and, thus, increasing the air flow speed through the ducts, the pressure P2 above the block being smaller than P1. The raise of air flow causes the temperature, to fall until it reaches a predetermined minimum value, when, then, the electronic control circuit 10 desactiva- tes the fan. With this system it is possible to maintain the temperature and the permanence time of the air within the ducts within predetermined values.

A model based on the above described example supplied a mean flow of 35 m ³ /h of sterilized air for a room temperature αf 30 C and relative humidity of 85%. ^'

The temperature variation/ in its maximum and minimum spots through l_!he ducts, was of 95 C in the inferior portio.n,

450°C at 6 cm above the inferior portion and 300 C on the outlet of the ducts at 7 cm.

The model proved to be efficient in the reduction of biological activity in the air in a room of 250 cubic meters volume. Thus, it was verified that the present invention does not heat significantly the room, being destinated only to the air treatment, reducing the relative humidity and the biological activity.

For instance, it may be mentioned that the average thermal irradiation of a grown-up person is ahoutl OOWatts. There_ fore the 500W model of the present invention is thermically equivalent to 5 people within a room of about100 square meters and 2,5 meter high. This demonstrates that its ^' load on the cooling systems is insignificant, thus being of great utility in rooms where there is no air renovation.

Since it does not produce a significant heating of the room, due to its low power per air volume unit relation, the present invention independs on the climatization form and can be used indiscriminately.

In an experiment carried in Bremen University (German Federal Republic) with an apparatus of the present type inside a garbage room of 21,2 m ³ (3,67 m x 2,88 m x 2,00 m) , the follow ing results were found: parameters of experiment:

- operation time of the apparatus : 64 h

- number of apparatus : 2 results table: germs content before after reduction total germs content 4 10 28% yeast + mould 5 1 80% enterobacteriacese 4 - 1 00 % bac. cereus 5 3 80%

- encubating time : 7 days Conclusions : each apparatus could reduce, e.g., the yeast + mould incidence in 80% for a room of 10 m ³ . In the gross, it seems that the apparatus used in the experiment permit an advantageous germ elimination effect.

Yet, another experience carried in the Brazilian Ministry of Health - Oswaldo Cruz Foundation ^' - National Institute for Quality Control in Health resulted in a particle reduction as represented on figure 3. The parameters of the experiment were as follow:

- specification of se : flow = 9 m ³ /h - volume of the test room : 25,80 m ³

- number of sterilizers : 3

- experimental method : growing of colonies of micro¬ organisms (fungi and bacteria) in Petri dishes, in blood agar and Sabourand's agar media exposed to the environment for 15 minutes.

The process is repeated with different set operating periods ( 0 min, 45 min, 75 min, 135 min and 195 min)

Conclusions and remarks were stated as follow:

The exponential pattern e^ = e ⁹³ ' ¹⁰⁶ . x~ ¹¹ ' ⁸³ is appropriate for representing the decrease of viable particles with set operating time.

Both factors, set operation time and also the day the experiments were carried out are significant. We should interpret the difference observed as a consequence rather of the

(successive) day than of the fact that the experimenter remained in the room or circulated entering and leaving it.

Considering that the experiments were carried on on succeeding days , a large decrease evident in the number of viable particles obtained in experiment II, and such difference is statistically significant.

As can be seen from the graph, the number of particles remains, much stabler, though decreasing with time, on the second day, so that there is a stabilization of the general level of particles in the environment. The difference between the experiments (days) proves highly sifnificant in the beginning (0 ¹ ) and at 135 ' . In the latter case it is likely that a variation has occurred in the voltage, causing the number of particles to increase, contrary to expectation. The significance of the interaction is reflected by the fact that the variations observed between set operation times depended on the day (1st or 2nd) the experiment was performed.

Accordingly, we may conclude that the general level of particles in the environment tends to vary in function of the initial concentration of particles. On the second day, the concentration is much smaller (a highly significant difference within t ₁ = 0 ' and the number of particles decreases with operation time, but not so sharply. As a result of the general analysis applied, we conclude that the set is efficient in reducing the number of viable particles in the environment.

So the object in a second stage of the analysis, would then be to find out whether the reduction of the number of particles attains that minimum level of concentration which characterizes a sterile environment.

According to N.A.S.A. specifications, a sterile environment must contain no more than 0.0035 viable particles per liter. Since the flow in the set is 9 cubic meters per hour and the volume of the room 25.80 cubic meters, we conclude that sterilization of the room would occur after approximately 2 hours 52 minutes or 172 minutes of set operation.

The present experiment used three (3) sets operating

simultaneously, so room sterilization time would be reduced to 172 minutes divided by three, or 57 minutes, i.e. about one hour.

Considering the volume above the area where the Petri dishes were exposed to be approximately one cubic meter, we conclude" that an index of 3.5 viable particles per cubic meter would represent a correct index of sterility to the environment.

In experiment I, the values were significant at the 5% level with 75' and 135", and almost significant (but that is no longer: s:ignificant) at 195'; accordingly, one concludes that on.that first: day, when the room had an initial natural concentration of particles in the environment, after 3 hours of operation was the set able to reduce the environmental air to a level considered sterile. In experiment II, i.e. on the second day, the differences were not significant, with much lower concentration, and in this case the atmosphere may be considered sterile.