Patent Application
20100251679
The present invention relates to filter units and filter unit panels, for example, used in air inlets of clean rooms, air conditioning equipment, gas turbines, and steam turbines.
An air filter is provided in each inlet of, for example, clean rooms, air conditioning equipment, gas turbines, and steam turbines. An air filter suitable for these purposes is a filter unit panel in which a plurality of filter units, each having a filter medium and a frame for supporting it, are joined together with their outer peripheral surfaces being in contact with each other. JP 2005-177641 A discloses an example of such a filter unit.
The filter unit disclosed in JP 2005-177641 A includes a filter medium and a frame (supporting frame), and the frame is formed by injection molding of a resin. During the injection molding, the filter medium can be fixed to the frame simultaneously with the formation of the frame. JP 2005-177641 A describes, in paragraph 0026, that the frame may contain an additive such as a pigment, an antibacterial agent, or a carbon fiber.
When the frame is formed by injection molding of a resin, the frame is deformed due to the shrinkage of the resin, and the filter medium is deformed accordingly. When the filter medium is deformed significantly, adjacent ridges of the pleats of the filter medium are brought close excessively to each other, which increases the pressure loss of the filter medium. A smaller ratio of the distance between the ridges to the height of the pleats is more suitable for a larger filtration area. A deeply-folded filter medium for reducing this ratio, however, is susceptible to a significant increase in pressure loss due to the deformation of the frame.
Accordingly, it is an object of the present invention to provide a filter unit in which an increase in pressure loss is suppressed despite the use of an injection-molded resin as a frame, and a filter unit panel using the filter unit.
The present invention provides a filter unit including: a pleated filter medium; and a frame for supporting the filter medium. The frame has inner and outer peripheries, each of which is rectangular in shape when viewed along an air flow path through the filter medium. In this filter unit, the filter medium is fixed to the frame with a peripheral portion of the filter medium being embedded in an inner peripheral surface of the frame. The pleated filter medium has a value D/P of 0.25 or less. This value D/P is obtained by dividing a distance D between adjacent ridges of the pleats of the filter medium by a height P of the pleats, and the distance D has a minimum value d of at least 1 mm. The frame is a resin member containing 5 to 30% by weight of glass fiber. The frame has a length La longer than a length Lm. The length La is a length of the frame measured in a direction in which the ridges of the filter medium are arranged, and the length Lm is a maximum length of the frame measured in a direction in which the ridges of the filter medium extend.
In another aspect, the present invention provides a method of manufacturing a filter unit including a pleated filter medium and a frame for supporting the filter medium. The frame has inner and outer peripheries, each of which is rectangular in shape when viewed along an air flow path through the filter medium. This method includes the step of setting the pleated filter medium in an injection molding machine so that the filter medium has a value D/P of 0.25 or less and a peripheral portion of the filter medium is exposed to a resin injection space in the injection molding machine. The value D/P is obtained by dividing a distance D between adjacent ridges of the pleats of the filter medium by a height P of the ridges. The method also includes the step of forming the frame that is a resin member made of a resin containing 5 to 30% by weight of glass fiber by injecting the resin into the resin injection space and thereby embedding the peripheral portion of the filter medium in the frame to fix the filter medium to the frame. The frame has a length La longer than a length Lm. The length La is a length of the frame measured in a direction in which the ridges of the filter medium are arranged, and the length Lm is a maximum length of the frame measured in a direction in which the ridges of the filter medium extend.
The present invention further provides a filter unit panel including a plurality of the filter units of the present invention, integrated into a single unit with the outer peripheral surfaces of the frames thereof being in contact with each other.
According to the present invention, since the resin containing 5 to 30% by weight of glass fiber is injection-molded to form the frame, the frame resists deformation. Further, in the present invention, since the frame is formed so that the length La of the frame becomes longer than the length Lm thereof, the deformation of the filter medium, which may cause an increase in the pressure loss, is reduced, as described later in Examples. Accordingly, even in a filter medium having such sharp-ridged pleats that the value D/P obtained by dividing the distance D between adjacent ridges by the height P of the pleats is 0.25 or less, the increase in the pressure loss can be suppressed. According to the present invention, it is possible to suppress the increase in the pressure loss of the filter unit, while taking advantage of the simplification of the manufacturing processes of the filter unit by injection molding.
Hereinafter, an embodiment of the present invention will be described as an example with reference to the accompanying drawings.
As shown in
The frame 2 is a resin member that has been injection-molded so that the peripheral portion of the filter medium 1 is fixed to the frame 2. The injection molding allows the formation of the frame 2 and the fixing of the filter medium 1 to the frame 2 to be performed simultaneously, and thereby simplifies the manufacturing processes. The peripheral portion of the filter medium 1 is embedded inside (in the inner peripheral surface of) the injection-molded frame 2, and the resin has penetrated into the peripheral portion of the filter medium 1.
The frame 2 is a resin member containing 5 to 30% by weight of glass fiber. The glass fiber prevents the shrinkage of the injection-molded resin. When the content of glass fiber in the resin member exceeds 30% by weight, the resulting molded article becomes brittle and the components of the molding machine are worn severely. On the other hand, when the content of the glass fiber in the resin member is less than 5% by weight, the shrinkage of the resin cannot be prevented sufficiently. The content of the glass fiber in the resin member preferably is 10 to 30% by weight. Carbon fiber also is known as a fibrous additive. Glass fiber is, however, much more preferable than carbon fiber from the viewpoint of suppression of coloring and cost effectiveness (i.e., prevention of deformation of the frame).
A plurality of the filter units 10 may be used as a single panel. A filter unit panel 20 shown in
As shown in
A smaller value DIP is better to reduce the pressure loss while securing a sufficient filtration area for the filter medium 1. The value D/P preferably is 0.25 or less, and particularly preferably 0.15 or less. On the other hand, an excessively small value DIP may increase the pressure loss of the filter medium 1. An excessively small value D/P also may deteriorate the durability of a mold used for injection molding. Therefore, the value DIP preferably is at least 0.05. It should be noted that the value D/P is calculated using, as the distance D, the average value of the distances between all pairs of adjacent ridges 11 and the average value of the distances of all pairs of adjacent ridges 12.
As shown in
In order to prevent the pressure loss from increasing, the minimum distance d (i.e., the minimum value of the distance D) in the filter medium 1 is at least 1 mm. The distance d preferably is at least 2 mm, and particularly preferably at least 3 mm.
In order to obtain a value of the distance d in the above range, it is preferable that the shape of the frame 2 is maintained as designed in the extension direction W of the ridges 11. The preferable dimensions of the frame 2 are described again with reference to
Preferably, the height (depth) Lh of the panel is less than 50 mm from the viewpoint of space saving.
Preferably, the pressure loss and the particle collection efficiency of the filter unit panel are 250 Pa or less and 95% or more, and particularly preferably 150 Pa or less and 99% or more, respectively, when expressed as values measured by a method to be described later. In this regard, however, the values indicating the characteristics of the filter unit panel of the present invention are not limited to the above-mentioned ones because the required pressure loss and particle collection efficiency vary depending on the intended use.
The type of the filter medium 1 is not particularly limited. A laminated body of a porous polytetrafluoroethylene (PTFE) membrane and an air-permeable fibrous layer is preferred. Although an electret filter medium has a low pressure loss, it does not exhibit such a high collection efficiency as a HEPA-grade filter medium, and its collection efficiency decreases when it is washed. When a glass fiber layer is used as a filter medium, the pressure loss increases. When the height P of the pleats is increased to compensate for the increase in the pressure loss, the frame has a greater height and thereby has a larger size, which increases the weight of the air filter accordingly.
The air-permeable fibrous layer may be, for example, felt, nonwoven fabric, woven fabric, and meshes (network sheet). Examples of the material of this layer include polyolefins (such as polyethylene (PE) and polypropylene), polyamides (including aromatic polyamide), and polyesters (such as polyethylene terephthalate (PET)). Preferably, the air-permeable fibrous layer is a nonwoven fabric formed of a fiber having a core-sheath structure in which the core component is made of a higher melting point material than the material of the sheath component.
Examples of the resin constituting the frame 2 and the outer frame 3 include polyolefin resins, polyamide resins (including aromatic polyamide resin), polyurethane resins, polyester resins, polystyrene resins (such as ABS resin), and polycarbonate resins. Two or more of these resins may be used in combination, or different types of resins may be used for the frame and the outer frame.
The shrinkage factor of the glass fiber-containing resin constituting the frame 2 preferably is 10/1000 or lower, and particularly preferably 5/1000 or lower. In the present description, the shrinkage factor of the resin means a molding shrinkage factor (SMn) measured in the direction perpendicular to the flow direction according to JIS K7152-4.
Hereinafter, the present invention is described further in detail with reference to Examples. First, a method of measuring the collection efficiency is described.
[Collection Efficiency]
The rate of air flow through each sample filter unit panel was adjusted to 0.5 m/sec, and polydisperse dioctyl phthalate (DOP) particles were allowed to flow from the upstream side of the sample at a concentration of 107 particles per liter. The concentration of the DOP particles on the upstream side of the sample and the concentration of the particles that have passed through the sample to the downstream side thereof were measured with a particle counter. Thus, the collection efficiency of each sample was obtained according to the following equation. The DOP particles with diameters of 0.3 to 0.4 μm were used.
Collection efficiency (%)=[1−(Concentration on downstream side/Concentration on upstream side)]×100
[Pressure Loss]
A pressure loss was measured with a pressure gauge (manometer) when the rate of air flow through each sample filter unit panel was adjusted to 0.5 m/sec.
A porous PTFE membrane was placed between two sheets of nonwoven fabric so as to be overlapped. Then, the resulting sheet was passed through a pair of rolls heated at 180° C. and thereby thermal lamination was carried out. Thus, a filter medium with a thickness of 0.32 mm, a pressure loss of 170 Pa, and a collection efficiency of 99.99% was obtained. A PET/PE core-sheath type nonwoven fabric with a weight per unit area of 30g/m2 (“Eleves T03030WDO” manufactured by UNITIKA, LTD.) was used.
The porous PTFE membrane was prepared in the following manner. 100 parts by weight of PTFE fine powder (F-104, manufactured by Daikin Industries, Ltd.) and 20 parts by weight of a liquid lubricant (dodecane) were mixed uniformly, and the resulting mixture was preformed. Next, the preformed body was formed into a rod by paste extrusion, followed by rolling the rod thus formed with a pair of metal rolls. Thus, a continuous sheet having a thickness of 200 μm was obtained. This continuous sheet was stretched by a factor of 10 in the longitudinal direction thereof at a stretching temperature of 200° C. Then, the resulting sheet further was stretched by a factor of 20 in the width direction thereof at a stretching temperature of 80° C. by a tenter method. Thus, an unsintered porous PTFE membrane was obtained. This unsintered porous PTFE membrane was sintered in a hot air furnace at 400° C., and thereby a long strip of porous PTFE membrane (with a thickness of 10 μm) was obtained.
The filter medium obtained in the manner described above was pleated so that 93 pleats having a height (P) of 22 mm were formed therein. The pleated filter medium was set in a mold of an injection molding machine, and a polycarbonate resin containing 30% by weight of glass fiber was injection-molded into a frame with a thickness (wd1, wd2, wd3, and wd4) of 3 mm. Thus, a filter unit having outer dimensions of 195 mm (Lm)×295 mm (La) with a height of 27 mm (Lh) was obtained. The thickness of the frame of the filter unit is thus uniform around the entire periphery of the filter medium (i.e., wd1=wd2=wd3=wd4). As the polycarbonate resin containing 30% by weight of glass fiber, “IUPILON” manufactured by Mitsubishi Engineering-Plastics Corporation was used. The shrinkage factor of the polycarbonate resin was 3.5/1000.
Next, six filter units were placed with the outer peripheral surfaces of the frames being in contact with each other and integrated into a single unit by heat welding. Thus, a filter unit panel was obtained. Further, four polycarbonate resin bars, which have been produced previously by extrusion molding, were disposed on the outer peripheral surface of the filter unit panel, and the filter unit panel and the bars were heat-welded. Thus, a filter unit panel with an outer frame (i.e., an air filter) having outer dimensions of 610 mm×610 mm with a height of 27 mm was obtained. For the above-mentioned heat weldings, protrusions formed on the upper and lower faces of the frames and the outer frame were used as welding ribs.
An air filter was obtained in the same manner as in Example 1, except that the content of glass fiber in the polycarbonate resin used for injection molding was changed to 10% by weight. The shrinkage factor of the polycarbonate resin containing 10% by weight of glass fiber was 5/1000.
An air filter was obtained in the same manner as in Example 1, except that the polycarbonate resin containing no glass fiber was subjected to injection molding.
A commercially available air filter including a glass fiber layer as a filter medium was prepared.
An air filter was obtained in the same manner as in Example 1, except that filter units each having outer dimensions of 295 mm (Lm)×195 mm (La) with a height of 27 mm (Lh) were formed.
Table 1 below shows the characteristics (pressure losses and particle collection efficiencies) of the air filters obtained in Examples and Comparative Examples. Table 1 also shows the outer dimensions and weights of the air filters, the values D/P, the values d, and the actually measured values of ratios (Lm−Le)/Lm of the filter media, and the values La/Lm obtained from the lengths of the frames of the filter units used for forming the air filters. It should be noted that the values D/P, the values d, and the ratios {(Lm−Le)/Lm}×100 (shrinkage factors of the frames) were obtained by calculating the average values of those of the six filter units. In Examples and Comparative Examples, the length La, the length Lm, and the thicknesses wd1, wd2, wd3 and wd4 of the frame of each filter unit were almost unchanged after the heat welding for forming the air filter.
In the air filter of Comparative Example 1, the filter medium was deformed partially near the frame due to the shrinkage of the resin. Thereby, in the deformed region, adjacent ridges were brought very close to each other with a smaller distance therebetween. Presumably, such a deformation of the filter medium increased the pressure loss.
Also in the air filter of Comparative Example 3, the filter medium was deformed partially near the frame, and thereby, the distance between adjacent ridges became smaller in the deformed region. In the filter unit of Comparative Example 3, the length of the frame in the direction in which the ridges of the filter medium extend was longer than the length of the frame in the direction in which the ridges of the filter medium are arranged. Presumably, this is the reason why the filter medium was deformed and thereby the pressure loss was increased, even though the shrinkage factor of the frame was as small as the frames of Examples.
A comparison between Example 1 and Example 2 shows that the difference in the content of glass fiber between 10% and 30% has little influence on the effect of suppressing the increase in the pressure loss. In view of this, the content of glass fiber may be, for example, 10 to 20%.
The filter unit panel composed of the filter units of the present invention is suitable for air filters used in inlets of, for example, clean rooms, air conditioning equipments, gas turbines, and steam turbines.
| Number | Date | Country | Kind |
|---|---|---|---|
| 2007-298672 | Nov 2007 | JP | national |
| Filing Document | Filing Date | Country | Kind | 371c Date |
|---|---|---|---|---|
| PCT/JP2008/070615 | 11/12/2008 | WO | 00 | 5/12/2010 |
