Air purifier

An air purifier intended for use, e.g., as a grease filter in air venting systems. The purifier comprises a plurality of modules operating according to centrifugal separation, each module comprising at least one vortex chamber. Gas flow entering the vortex chamber is set into helical motion therewithin, such that the gas flows through the vortex chamber in a single direction, substantially perpendicular to a direction in which the incoming gas flow is introduced into the module.

BACKGROUND OF THE INVENTION 
The present invention concerns an air purifier intended to be used, for 
instance, as a so-called grease filter in the air venting systems of 
institutional, bar, grill room and restaurant kitchens or equivalent 
spaces, said air purifier comprising a purifier part which has of two or 
more air purifying modules operating on the centrifugal separation 
principle, each of them having one or several vortex chambers, and air 
purifier frame structures, if any. 
An important field of use of air purifiers is the so-called grease filters. 
Through the grease filters, spoiled air is drawn in connection with food 
preparation. In professional kitchens, such as restaurant, grill room and 
institutional kitchens, the air that is spoiled in connection with the 
preparing of food causes a special problem. 
The grease filter separates grease and other impurities from the vapors and 
gases produced when food is being prepared and in this way prevents the 
entry of these inflammable and otherwise harmful substances in the 
ventilation system. The grease filter is most often placed in air venting 
means over the stove or equivalent. Several grease filters may be used 
side by side. 
The object of the grease filters is to prevent the duct systems and fans 
from becoming dirty and thus to reduce the need for cleaning the 
ventilation system and to improve fire safety and hygiene. The following 
requirements, among others, are imposed on a grease filter; naturally, 
good filtering capacity. The degree of self-cleaning of the filters based 
on running down of the accumulated grease should be as good as possible. 
The filter cleaning period should be long without increasing the 
resistivity of the filter or altering its cleaning efficiency. The filter 
should be easy to service and to inspect. The filter should present the 
highest possible fire safety and hygienic standard. 
The filter should also be durable and user-friendly. 
At a present, so-called impact filters are commonly used for grease filters 
which consist of mutually superimposed metal nets or of nets and a metal 
fiber mat. A drawback of these kinds of filters is that their separating 
capacity is usually too low. The filter needs frequent servicing because 
the grease adheres to the filter material instead of running down into the 
grease groove. Cleaning is difficult. These drawbacks also have the 
consequence that fire hazard increases, and the specific pressure loss 
increases significantly in comparison with a clean filter, whereby the 
quantity of vented air decreases and the quality of the indoor air 
deteriorates. The service life of such filters is relatively short. They 
are easily damaged at mounting, in use, or when they are being cleaned. 
For grease filters, so-called centrifugal filters are also used. 
Present-day centrifugal filters also have comparatively low separating 
capacity, owing to their construction. As examples of inappropriate 
shaping of the elements in grease filters, the U.S. Pat. Nos. 3,834,135; 
3,910,782; and 3,566,585 may be mentioned. Their construction is also 
unnecessarily complex and the filter is relatively expensive for this 
reason. The separating capacity of centrifugal filters as well as impact 
filters varies greatly in practice, depending on the amount of air flow. 
Attempts have been made to eliminate this drawback by means of adjustable 
filters. When several adjustable filters are used with different settings 
in one kitchen, there is a risk that they become mixed up e.g. after 
washing. 
GB-A-2,092,483 teaches a conventional air purifier with centrifugal 
separators, where the outlet pipes 22 (FIGS. 4, 6 and 7) are merely 
central tubes or conduits of a conventional cyclone separator. It is 
emphasized that the direction of flow of a gaseous fluid reverses by 
180.degree. in the conduits 22. This is best seen in FIGS. 4, 6 and 7, as 
denoted by the arrow Q3. Accordingly, this known air purifier suffers from 
a strong tendency to become clogged. Additionally, the air purifier 
according to GB-A-2,092,483 has a comparatively complicated structure, 
wherein a flow channel 12 extends over the entire length of the air 
purifier supplying air flow into each particular vortex chamber 4, 6, 8, 
10 (FIG. 1). The particulates separated from the air flow continue to flow 
toward the outlet 20. Furthermore, as explicitly illustrated in 
GB-A2,092,483, the start of the escape point, or the inner end of the 
central tube 22 of the cyclone separator, is centered therewithin. 
Certain advantages are however achieved with centrifugal filters. The 
service life of centrifugal filters is in general rather long. The filter 
efficiency also does not deteriorate as a consequence of repeated washing 
as is the case with fiber filters. The fire safety of centrifugal filters 
is also better than that of fiber filters. 
In the centrifugal filters known in the art, the air flow turns 180.degree. 
in the lower cyclone cone, after which the air flow exits from the cyclone 
through the central tube. For this reason the filtering capacity is rather 
low and does not increase significantly after the change of direction. It 
is true that the separating capacity can be somewhat improved with the aid 
of vortices. The centrifugal filter does not store grease in the filter 
because the separated grease runs off efficiently. However, other solid 
particles also usually accompany the grease, e.g. dirt, dust, etc., and in 
this case the respective impurity is no longer freely flowing and fails 
therefore to run off even a slippery surface. This is the reason why 
existing centrifugal filters may become clogged. 
Currently, such grease filters are also in use in which two consecutive 
filters are used. These so-called two-phase filters are good in principle, 
but if in both filters both phases are filtering out the same particle 
size, then the latter phase is unnecessary in practice because the 
filtering capacity only increases about 1% in comparison with the 
filtering capacity of the first filter. 
SUMMARY OF THE INVENTION 
The object of the invention is to produce an air purifier superior to the 
grease filters known in the art operating on the centrifugal principle. 
A more detailed object of the invention is to provide an air purifier which 
is an eminently useable so-called coarse filter, in which group the grease 
filters are classified. 
Another object of the invention is to provide an air purifier having 
sufficient separating capacity, whereby the soiling of ducts and blowers 
is prevented. 
Still another object of the invention is to provide an air purifier having 
a hollow construction, so that even great quantities of grease may be 
allowed to accumulate in it without any consequent derangement of 
function, and which is also easy to service, free of fire hazard, reliable 
in operation, safe in installation, and which substantially lengthens the 
service life of fine filters if in the design a fine filter is also 
employed in addition to the coarse filter. 
The aims of the invention are achieved with an air purifier which is mainly 
characterized in that the air flow entering through each inlet aperture of 
the air purifier modules is, with the aid of the differential pressure 
.DELTA..sub.p across the air purifier, set in the vortex chamber of each 
air purifying module into one or several helical motions proceeding, with 
reference to the cross-section of each vortex chamber, in substantially 
the same perpendicular direction. 
The chambers may be placed in parallel, and there may be a partition 
between the chambers. 
The chambers may be divided with a guide baffle into at least two partial 
chambers. 
The other characteristic features of the air purifier of the invention are 
presented below. 
With the air purifier of the invention, all those desirable properties are 
attained which are required from a good grease filter. The filtering 
capacity of the air purifier of the invention is good, the air purifier is 
easy to service, the air purifier causes no fire hazard, and the air 
purifier is highly reliable in operation.

DESCRIPTION OF THE PREFERRED EMBODIMENTS 
In the embodiment depicted in FIGS. 1-3, the air purifier of the invention 
in general has been indicated by reference numeral 10. In this embodiment 
the air purifier 10 comprises a purifier part 11, a top collar 12a and a 
lower collar 12b. Side collar 13 and 14 serve the sidemost chambers 16. 
The handle is indicated by reference numeral 15. 
As taught by the basic idea of the invention, the purifier part 11 has been 
composed of separate modules which in FIG. 4 are generally indicated by 
reference numeral 16. The modules are separated by a partition 17, to 
which the separate modules 16 are attached with a beak-like member 18c by 
any fixing method known in itself in the art. In this embodiment, grease 
separation from the incoming air flow, in FIG. 4 indicated by the arrow A, 
takes place in the modules 16 placed in parallel. As is seen in FIG. 4, 
the air flow A is caused to rotate in separate vortex chambers 16a, 16b 
without change of the direction of rotation. As a result a highly 
efficient separation effect is obtained with relatively low air flow 
velocities, the degree of separation of particles over 5 .mu.m being about 
95% and that of particles over 2.5 .mu.m still about 50%. 
In the embodiment of FIG. 4, the modules 16 have been divided with a guide 
baffle 18b into two vortex chambers 16a and 16b in which vortices are 
produced, indicated in FIG. 4 by arrows B' and B". As is observed in FIG. 
4, the air flows B', and B" in the vortex chambers 16a and 16b are helical 
rotary motions. As illustrated in FIG. 4, the air flows B', B" proceeding 
in the same direction have opposite directions of rotation inside the 
vortex chambers 16a, 16b. 
In FIG. 5 an advantageous embodiment of the modular design is presented. In 
this embodiment, the structure 18 of the module 16 includes beak-like 
parts 18a and 18c. The beak-like member 18a of the structure 18 of the 
module 16 defines, as seen in FIG. 4, a flow slit 19 of size less than 
about 10 mm, so that most efficient separation possible might be obtained. 
The size of the flow slit 19 is advantageously in the range of about 3-8 
mm. 
In the air purifier 10 of the invention, the helical motion B may be made 
such that air emerges from the air purifier 10 both from top and from 
below. Furthermore, the air purifier 10 of the invention is characterized 
in that the helical rotary motion B', B" continues a certain distance 
after leaving the air purifier 10. The escaping air flows B', B" may be 
disposed to take place from the top and from under the air purifier 10. 
In FIGS. 6 and 7, the incoming air flow A and the outgoing flows B.sub.1 
and B.sub.2 are illustrated. The helical flows within the purifier modules 
are indicated in FIGS. 6 and 7. 
The incoming air flow, which contains impurities such as grease, for 
example, is thrown at the walls of each vortex chamber, and the air free 
of impurities escapes along both lower and top flows B.sub.1 and B.sub.2 
respectively. If the incoming air flow A is below the center line of the 
air purifier 10, the air free of impurities escapes along the lower flow 
B.sub.1. 
Similarly, if the incoming air flow A is above the center line of the air 
purifier 10, the air escapes along the top flow B.sub.2. The direction of 
rotation of the vortex in the vortex chamber depends on the orientation ad 
location of the beak-like guide member 18a. In FIG. 7, the direction of 
rotation of the vortex is counter-clockwise in the chambers at the left 
side of the center line and, similarly, the direction of rotation of the 
vortex is clockwise in the chambers at the right side of the center line. 
It is to be particularly noted that the grease as a heavy component always 
runs downwards throughout the entire wall structure of a vortex chamber, 
while the lighter air purified of grease may flow out either from below or 
the top in the flows B.sub.1 and B.sub.2 respectively. In the air purifier 
according to the invention, it is very important that each vortex chamber 
comprises means 17, 18a for setting the incoming gas flow within the 
vortex chamber 16a into the helical motion, such that the gas flows 
through the vortex chamber 16a only in directions substantially 
perpendicular to the direction in which the incoming gas flow is 
introduced through the inlet aperture 19. Great quantities of grease may 
therefore be allowed to accumulate in the air purifier according to the 
invention without any damage to its operation. 
Thus, this air purifier is quite easy to service, reliable in operation, 
safe to install and free of any fire hazards. Its service life is also 
greatly extended as compared to the service lives of the cyclone 
separators previously used. Highly efficient separation may be obtained 
with relatively low air flow velocities. The degree of separation of 
particles over 5 microns is about 95%, while the degree of separation of 
particles over 2.5 microns is still about 50% 
The escape points in the structure of the air purifier according to the 
present invention are away from the separation portion whereas in 
GB-A-2,092,483 the start of the escape point or the inner end of the 
central tube 22 of the cyclone separator is centered therewithin. 
In FIGS. 8 and 9, the air inflow has been indicated with symbol A, and 
similarly the air outflow has been denoted with symbols B.sub.1 and 
B.sub.2. The helical flows are indicated in FIGS. 4, 8 and 9. The 
operation of the illustrated apparatus in FIGS. 8 and 9 is similar to the 
alternative embodiment in FIGS. 6 and 7 as follows. The incoming air which 
contains impurities, such as, for example, grease, is thrown at the walls 
of each vortex chamber, and the air free of impurities escapes both from 
below and above in flows B.sub.1 and B.sub.2 respectively. If the incoming 
air flow A is below the center line of the structure 10 of the invention, 
the air free of impurities escapes from below in flow B.sub.1. Similarly, 
if the incoming air flow A is above the center line of the structure 10, 
the flow escapes from above in flow B.sub.2. The direction of rotation of 
the vortex in the vortex chambers 16a, 16b depends on the orientation and 
location of the beak-like member 18a. 
In FIG. 8 (as in FIG. 7), the direction of rotation of the vortex is 
counter-clockwise in the chambers at the left side of the center line and, 
similarly, the direction of rotation of the vortex is clockwise in the 
chambers at the right side of the center line. It is to be particularly 
noted that the grease as a heavy component always runs downwardly 
throughout the entire wall structure of a chamber, while the lighter air 
purified of grease may flow out either from below or above in the flows 
B.sub.1 and B.sub.2 respectively. The force driving the air flow A into 
the purifier 10 of the invention depends on the p used. The differential 
pressure .DELTA.p must generally be between about 25 and 150 pascal. It is 
particularly noted that it is disadvantageous to use too great a .DELTA.p 
which would result in deterioration of the purification effect. Likewise, 
it is disadvantageous to use too small a .DELTA.p, which would result in 
decrease of the separation efficiency. 
The vertical outflow is denoted in FIG. 10 by B'. The embodiment 
illustrated in FIGS. 10 and 11 essentially corresponds to the embodiment 
illustrated in FIGS. 4 and 5, but with omission of guide baffle 18b. 
Therefore, only a single helical flow B' generated in each respective 
module 16. Accordingly, similar components have been denoted by the same 
reference numerals. The rotational direction in a single duct or chamber 
16a or 16b is always the same, even though there are opposite overall 
translational flows from one another, as best seen in FIGS. 6 and 9. 
The air purifier of the present invention may be utilized in conjunction 
with an air exhausting device described in U.S. patent application Ser. 
No. 010,277 filed Dec. 5, 1986 which is incorporated by reference herein. 
In other words, the air purifier of the present invention may be 
positioned in the device of U.S. Ser. No. 010,277 so that appropriate air 
flow is "captured" and directed toward the air purifier with appropriate 
.DELTA.p. .DELTA.p can be regulated with a blower forming part of the 
device disclosed in U.S. Ser. No. 010,277, or with a regulating organ in 
an air conditioning canal system that is known per se. 
FIG. 12 is a perspective view of the air purifier of the present invention, 
illustrating the separation principles that are accomplished herewith. 
More specifically, the air purifier of the present invention may be 
obliquely positioned as illustrated in FIG. 12, e.g. in the device of U.S. 
Ser. No. 010,277, and accomplish the separation of particles from gas 
(air) flow as illustrated herein. Such separation is especially effective 
as noted above, and as illustrated in the graph of FIG. 13. 
The rotation of flows B', B" are in the opposite directions from one 
another, as illustrated in FIG. 4. However, these rotational flows B', B" 
may be in the same direction, if baffle 18b is moved to the opposite 
partition wall 17. In other words the rotational directions of flows B' 
and B" are determined by baffle 18b. 
The separated grease particles are thrown against the inner walls of the 
separate or air purifier and run down in a liquid flow into a collecting 
vessel 100 as illustrated in FIG. 14. This vessel is periodically emptied. 
Such a collecting vessel is also exemplified by grease channel 14 in U.S. 
Ser. No. 010,277. 
Italian Pat. No. 471,267 discloses a separator based upon impact. According 
to FIGS. 1, 2, and 4 of this reference, gas flows through an aperture 2 
into the separator and collides with the plates 7 within the separator 
itself. The plates 7 are shaped to have curved edges 9. The shape of these 
edges 9 naturally produces a turning movement, however, the thus-produced 
turning movement is stable, i.e. does not move downwardly or upwardly, but 
continues flow in the incoming direction. In other words, the resulting 
flow thereof is not perpendicular to the incoming direction through inlet 
2, but is rather substantially parallel to this incoming direction of 
flow. Only a continuous, successive turning in different directions occurs 
in the incoming flow of this reference. 
The resulting flow then exits through an aperture 3 from the separator in 
the Italian Pat. No. 471,267. According to the structure and procedure 
taught in this reference, the flow direction of gas from the inlet 
aperture 2 to the outlet aperture 3, remains unchanged, as best seen by 
the arrows in FIGS. 1 and 2 of this reference. 
More specifically, it is immediately clear from FIG. 1 of this reference 
that the incoming flow 2 and exhaust flow 3 are in the same plane and 
parallel to each other, unlike the structure of the present invention 
where the incoming gas flow A is in a different plane from the plane of 
the exhaust gas flows B.sub.1 and B.sub.2. In other words the flows A and 
B.sub.1, B.sub.2 are not parallel and are in different planes such that 
the flows and consequently the flow planes are perpendicular to one 
another. 
Referring to FIG. 4 of this reference, it is immediately seen that the 
incoming flow 2 turns in the purifier part 6 through 90.degree., then 
through 90.degree., and further through 90.degree., etc. in a succession 
of different directions. However both the incoming flow 2 and the exhaust 
flow 3 are always in the same plane, with the exhaust flow 3 always being 
parallel to the incoming flow 2. Accordingly, there is actual no rotary 
flow created in the purifier section 6 which at all resembles rotary flows 
B.sub.1, B.sub.2, much less any such flow which is perpendicular to the 
direction of the incoming flow. 
While flow is naturally changed slightly sidewardly at the edges 9 of the 
plates 7 (FIG. 4 of this reference) when the gas flow passes between the 
various plates 7 as illustrated, the flow still remains in the same plane 
as the incoming direction of flow. 
It is emphasized that the purifier or separator of the present invention is 
based upon centrifugal separation principles whereas the separator taught 
in Italian Pat. No. 471,267 is based upon impact principles, i.e. is a 
so-called plate impact separator. 
In the foregoing, a few advantageous embodiments of the invention have been 
presented and it is clear to a person skilled in the art that numerous 
modifications thereof are feasible within the scope of the inventive idea 
stated above.