[0001] The present invention relates to an electrostatic air filtration module and a two-stage
electrostatic filter, in particular for air recirculating apparatus comprising said
module.
[0002] It is known that in electrostatic air filters the air passes through an ionization
zone or section comprising a high-potential electrode, where the suspended solid particles
are ionized, and said ionized particles pass along paths which are bounded by walls
having a sign opposite to that of the particles, which are thus attracted towards
the said walls and stably deposited thereon.
[0003] The said electrostatic filters may be essentially of two types: so-called single-stage
filters, in which the ionization section and the collection section are combined in
a single section, and two-stage filters, in which the two sections are separate and
arranged in succession.
US2005/0051028 and
W02009/059451 disclose electrostatic filters of the conventional type in which the anode components
are all electrically connected to each other and to the positive pole. This means
that any damage to an anode plate results in blockage of the entire filter.
[0004] US 4,119,416 also discloses and defines special dimensional ratios for the various parts and in
particular the ratio between the distance of the polarization wire and ground and
the relative distance between the anode and cathode surfaces.
[0005] In connection with two-stage filters
EP 0,636,418, in the name of the same present Applicants, also discloses a two-stage electrostatic
filter for air recirculating apparatus comprising at least one ionization stage formed
by facing parallel walls which have, arranged inside, a high-potential electrode able
to generate an induction field which charges with a positive potential the walls of
ionization cells and at least one precipitation stage formed by parallel walls, having
a negative potential compared to the ionization potential, wherein said ionization
and precipitation cells consist of at least one cathode element in the form of an
"overturned U", the opposite ends of which are mechanically and electrically connected
to a transverse support profile and which is provided internally with at least one
partition extending parallel to the outer arms of the "U" along the length of the
profile, but with a height less than that of said arms and able to cooperate with
a U-shaped anode element arranged opposite it and mechanically fixed by means of insulating
support members, further cathode elements being envisaged for modular expansion of
the filter in the direction of the its width.
[0006] Although performing its function, this known filter has, however, limitations consisting
in the limited possibility of increasing its performance by means of an increase in
the filtration efficiency (= capacity of the filter to retain the particles) and the
regularity of performance over time, without correspondingly increasing the energy
consumption. The technical problem which is posed, therefore, is to provide a two-stage
filter which can be formed from a minimum number of parts which can be easily produced
and assembled together in a geometric configuration which can be realized and/or modified
very easily depending on the specific requirements of the individual applications
and which has a greater efficiency, but low energy consumption.
[0007] In connection with said problem the filter must also be simple to build and assemble,
at little cost, and be able to be applied easily to purification apparatus and also
be able to reduce the faults arising from handling of the ionization electrode, but
at the same be suitable for achieving and obtaining high efficiency characteristics
which are as constant as possible over time and with a small amount of maintenance.
Said technical problems are solved according to the present invention by a module
for forming a two-stage electrostatic filter comprising a cathode stage for collecting
the particles and a polarization stage, said cathode stage comprising a pair of flat
side elements of suitable length in the vertical direction and at least three further,
flat, central elements of smaller length compared to the length of the side elements;
the cathode side elements and central elements being parallel to each other and connected
in pairs in the transverse direction by pairs of intermediate bridges; and said anode
stage comprises at least four flat segments of suitable height in the vertical direction,
arranged alternating with the anode elements in the transverse direction; said anode
segments being connected together in pairs in the transverse direction by pairs of
intermediate bridges; insulating elements for supporting the components of the cathode
stage and anode stage; a high-potential electrode extending in the longitudinal direction
and arranged between the two cathode side elements.
[0008] Further details may be obtained from the following description with reference to
the accompanying drawings in which:
- Figure 1
- shows a schematic cross-sectional view of the basic elements forming a filter module
according to the present invention;
- Figure 2
- shows an exploded view of the module of Fig. 1;
- Figure 3
- shows an exploded schematic view of a preferred embodiment of the particle collection
stage according to the present invention;
- Figure 4
- shows an exploded schematic view of a preferred embodiment of the two stages, i.e.
polarization stage and particle deposition stage;
- Figure 5
- shows a perspective of the filter according to Fig. 4 in the assembled condition;
- Figure 6
- shows a partial cross-section along the plane indicated by VI-VI in Fig. 5 and
- Figure 7
- shows a comparative graph of the efficiency results which can be obtained with a filter
according to the prior art and a filter according to the present invention under different
geometric operating conditions.
[0009] Assuming solely for the sake of convenience of the description and without any limiting
meaning a set of three reference axes in a longitudinal direction X-X, transverse
direction Y-Y and vertical direction Z-Z and referring, for the sake of brevity, to
the higher potential elements as "anodes" and the lower potential elements as "cathodes",
Figs. 1 and 2 show the structure of a base module for forming a two-stage filter according
to the present invention.
[0010] In greater detail the said base module comprises:
- a cathode stage 100 formed by:
- a pair of flat side elements 110 of suitable length C1 in the vertical direction and
at least three further, flat, central elements 120 having a smaller length C2 than
the length C1 of the side elements 110;
said side elements 110 and central elements 120 being parallel to each other and connected
in pairs in the transverse direction Y-Y by end bridges 131 and by pairs of intermediate
bridges 132; said intermediate pairs defining a space 132a in the longitudinal direction
X-X suitable for the insertion of support elements 300, as will become clearer below.
It is envisaged moreover that said end bridges 131 are coplanar and, preferably, all
connected together in the transverse direction Y-Y by a cross-piece 140 which is for
example L-shaped as shown in Fig. 3 and which is in turn connected to the lower potential;
- an anode stage 200 formed by:
- at least four flat segments 210 of suitable height in the vertical direction Z-Z and
arranged alternating with the anode elements 120 in the transverse direction Y-Y;
the anode segments 210 being in turn connected together in pairs in the transverse
direction Y-Y by pairs of intermediate bridges 232 suitable for defining a space 232a
in the longitudinal direction such as to allow the insertion of said support means
300;
- a high-potential electrode 400 extending in the longitudinal direction X-X, arranged
inside the base module and suitable for producing the positive charge of the anode
elements 220;
- support elements 300 substantially formed by a coil of insulating material, suitable
for containing and supporting the various flat anode elements 110, 120 and cathode
elements 210: the coil has projections 301 oppositely arranged in the vertical direction
Z-Z for stable insertion with an interference fit inside the said seats 132a,232a
defined by the cathode intermediate transverse bridges 132 and the anode transverse
bridges 232.
[0011] Once the cathode stage 100 and the anode stage 200 have been joined together by means
of the insulating supports 300, the base module is formed and geometrically stable
for use.
[0012] According to a preferred embodiment of the base module for a modular electrostatic
filter it is also envisaged that: if R indicates the radius of a virtual cylinder
C, having a longitudinal axis coinciding with the polarization electrode 400, the
following is obtained:
- the cathode side elements 110 are tangential to the side surface of the cylinder C;
- the free end of the cathode segments 120 is tangential to the side surface of the
cylinder C.
[0013] It is envisaged, moreover, that, once the radius R has been defined as described
above, the relative distances between the various elements of the module are as follows:
D1 = the distance in the vertical direction Z-Z between the end of the cathode segments
210 and the electrode 400; said distance D1 being between 0.33R and 0.57R, preferably
between 0.41R and 0.49R;
D2 = the distance in the vertical direction Z-Z between the bottom end of the central
cathode element 120 and bottom end of the anode elements 210; said distance D2 being
between 0.40R and 0.60R, preferably between 0.49R and 0.54R;
D3 = the distance in the transverse direction Y-Y between the vertical anode elements
210 and the cathode segments 120; the distance D3 being between 0.41R and 0.57R, preferably
between 0.48R and 0.56R.
[0014] As shown in Figs. 3 to 6 with the base module for electrostatic filter according
to the invention, it is possible to provide a two-stage modular filter comprising:
- an ionization stage 2000 formed by a frame 2010 of insulating material having, arranged
inside, the electrode 400 formed by a continuous wire extending in the longitudinal
direction X-X so as to be arranged with parallel sections which have a constant interaxial
distance equal to 2R in the transverse direction Y-Y;
- a stage 1000 for collecting the ionized particles, formed by a plurality of base modules
extending as required in the longitudinal direction X-X and arranged alongside each
other in the transverse direction Y-Y.
[0015] Preferably the base modules are connected together by a pair of L-shaped cross-pieces
140 for connection to the lower potential and inserted inside insulating end-pieces
1010 suitable for connection to and engagement with the frame 2010 of the polarization
stage 1000.
[0016] Said end-pieces have special guide seats 1010a suitable for insertion, in the longitudinal
direction X-X, of the ends of the anode segments 110 and cathode segments 210 in order
to obtain the correct interaxial distance in the transverse direction.
[0017] According to a preferred embodiment, said cathode elements 210 and anode elements
110 are assembled together individually in order to form modules which are electrically
insulated so that any malfunctioning or short-circuiting of one of the modules does
not alter the electric field of the entire filter, adversely affecting the overall
operating performance thereof.
[0018] It has been established during tests that, with the filtration module and modular
filter according to the present invention, it is possible to obtain a high degree
of efficiency and reliability with lower energy consumption and high degree of reliability
and ease of maintenance for normal cleaning operations.
[0019] As shown, in fact, in Fig. 7 it is possible to establish that the efficiency (continuous
line A) which can be obtained with a filter provided according to the teachings of
the present invention which has:
useful deposition area = 5.40 m
2;
R = 12 mm; D1 = 5.5 mm; D2 = 6.5 mm ; D3 = 2.5 mm
and with the characteristics shown in the table below
Novel filter type with proportions as per patent (version 1) |
Pressure Drop Pa |
2 |
Temp |
35 |
Relative Humidity (ur) % |
16.4 |
Diethyl sebacate exil (dehs) |
0.5 |
Recorded throughput m3/h |
1050 |
Nominal throughput m3/h |
1200 |
Power supply |
7330 |
Current |
0.22 mA |
is far superior to that of a filter provided according to the teachings of
EP 0,636,418 (broken line B) and with the characteristics as shown in the table below
Existing (old) filter type |
Pressure Drop Pa |
8 |
Temp |
35 |
Relative Humidity (ur) % |
16.4 |
Diethyl sebacate exil (dehs) |
0.5 |
Recorded throughput m3/h |
1050 |
Nominal throughput m3/h |
1200 |
Power supply |
7330 |
Current |
0.35 mA |
[0020] From the same Fig. 7 it is also possible to establish (dot-dash line C) that a filter
designed with the structure according to the present invention and with
same deposition area = 5.40 m2;
but with dimensional ratios
R = 12 mm; D1 = 7.5 mm; D2 = 4.5 mm ; D3 = 2.5 mm different from those envisaged by
the present invention and with the characteristics as shown in the table below
Novel filter type with different proportions (version 2) |
Pressure Drop Pa |
2 |
Temp |
35 |
Relative Humidity (ur) % |
16.4 |
Diethyl sebacate exil (dehs) |
0.5 |
Recorded throughput m3/h |
1050 |
Nominal throughput m3/h |
1200 |
Power supply |
7330 |
Current |
0.30 mA |
produces a limited increase in efficiency and a simultaneous increase in current consumption,
thus demonstrating that the efficiency has been surprisingly increased without having
to resort to a banal increase in the deposition areas.
[0021] As shown in Fig. 5 it is also envisaged that the end side cathode elements in the
transverse direction Y-Y are formed by means of elements 1110 folded in the manner
of a Z in order to provide support surfaces for the cross-pieces 140 for electrical
connection to the lower potential and to the frame 2010 of the polarization stage.
[0022] It is envisaged moreover that said cathode and anode elements are preferably made
by folding sheet metal parts so as to limit the need for special mechanical machining
equipment and therefore resulting in lower production costs.
[0023] Although described in connection with certain constructional forms and certain preferred
examples of embodiment of the invention, it is understood that the scope of protection
of the present patent is defined solely by the following claims.
1. Module for forming a two-stage electrostatic filter comprising a cathode stage (100)
for collecting the particles and a polarization stage (200), in which said cathode
stage (100) comprises:
- a pair of flat side elements (110) of suitable length (C1) in the vertical direction
and at least three further, flat, central elements (120) of smaller length (C2) compared
to the length of the side elements (110);
characterized in that
- said cathode side elements (110) and central elements (120) of the cathode stage
(100) are parallel to each other and connected in pairs in the transverse direction
(Y-Y) by pairs of intermediate mechanical bridges (132);
and said anode stage (200) comprises:
- at least four flat segments (210) of suitable height in the vertical direction (Z-Z),
arranged alternating with the anode elements (120) in the transverse direction (Y-Y);
- the anode segments (210) being connected together in pairs in the transverse direction
(Y-Y) by pairs of intermediate mechanical bridges (232);
- insulating elements (300) for supporting the components (110,210) of the cathode
stage (100) and anode stage (200);
- a high-potential electrode (400) extending in the longitudinal direction (X-X) and
arranged between the two cathode side elements (110);
in that
- said intermediate pairs of mechanical bridges (132,232) define a space (132a,232a)
in the longitudinal direction (X-X) suitable for the insertion of support elements
(300);
in that
- said cathode elements and anode elements are formed by means of folding; and
in that
- said cathode side elements (110) and central elements (120) are connected together
by mechanical end bridges (131).
2. Module according to Claim 1, characterized in that said end bridges (131) are coplanar and all connected together in the transverse
direction (Y-Y) by a cross-piece (140) connected to the lower potential.
3. Module according to Claim 1, characterized in that the cathode side elements (110) are tangential to the side surface of a virtual cylinder
(C) of radius R which has a longitudinal axis coinciding with the polarization electrode
(400).
4. Module according to Claim 3, characterized in that the free end of the central cathode segment (120) is tangential to the side surface
of the said cylinder (C).
5. Module according to Claim 3, characterized in that the distance D1 in the vertical direction (Z-Z) between the end of the anode segments
(210) and the electrode (400) is between 0.33R and 0.57R.
6. Module according to Claim 5, characterized in that said distance D1 is preferably between 0.41R and 0.49R.
7. Module according to Claim 3, characterized in that the distance D2 in the vertical direction (Z-Z) between the bottom end of the central
cathode element (120) and the bottom end of the cathode elements (210) is between
0.40R and 0.60R.
8. Module according to Claim 7, characterized in that said distance D2 is preferably between 0.49R and 0.54R.
9. Module according to Claim 3, characterized in that the distance D3 in the transverse direction (Y-Y) between the vertical anode elements
(110) and the cathode segments (120) is between 0.41R and 0.57R.
10. Module according to Claim 9, characterized in that said distance D3 is preferably between 0.48R and 0.56R.
11. Module according to Claim 1, characterized in that said support elements (300) are formed by a coil of insulating material which has
projections (301) oppositely arranged in the vertical direction (Z-Z) for insertion
with an interference fit inside the said seats (132a,232a) defined by the pairs of
cathode transverse bridges (132) and anode transverse bridges (232).
12. Two-stage, modular, electrostatic filter comprising an ionization stage (2000) and
a stage (1000) for collecting the ionized particles, characterized in that it comprises at least one electrostatic filtration module according to Claim 1.
13. Filter according to Claim 12, characterized in that the ionization stage (2000) is formed by a frame (2010) which is made of insulating
material and inside which the polarization electrode (400) is arranged and the stage
(1000) for collecting the ionized particles is formed by a plurality of modules extending
as required in the longitudinal direction (X-X) and arranged alongside each other
in the transverse direction (Y-Y).
14. Filter according to Claim 12, characterized in that said polarization electrode is formed by a continuous wire (400) extending in the
longitudinal direction (X-X) so as to be arranged with parallel sections having a
constant interaxial distance equal to 2R in the transverse direction (Y-Y).
15. Filter according to Claim 12, characterized in that the cathode elements (110,120) of the base modules are rigidly connected together
by a pair of cross-pieces (140) for connection to the lower potential.
16. Filter according to Claim 12, characterized in that it has insulating end-pieces (1010) suitable for connection and relative engagement
between the frame (2010) of the ionization stage (2000) and the collection stage (1000).
17. Filter according to Claim 16, characterized in that said end-pieces (1010) have guide seats (1010a) suitable for insertion of the ends
of the anode segments (110) and cathode segments (210).
18. Filter according to Claim 12, characterized in that said cathode elements (210) and anode elements (110) are assembled together individually
forming electrically insulated modules.
19. Filter according to Claim 12, characterized in that the cathode end side elements in the transverse direction (Y-Y) are formed by means
of elements (1110) folded in the form of a "Z" and arranged opposite each other.