Patent Application
20070144351
The present invention relates to a heat exchanging unit that efficiently recovers heat during ventilation.
There is a technology (e.g., refer to Patent Document 1) that aims to prevent contamination of a heat exchange element of a total heat exchanging unit (due to, for example, dust, bacteria, viruses or the like suspended in the outdoor air) by disposing an air filter, whereon a photocatalyst is supported, on the supply airflow upstream side of the heat exchange element.
Patent Document 1
Japanese Published Unexamined Patent Application No. H 10-311581
It is an object of the present invention to provide a heat exchanging unit that can prevent, more effectively than the conventional case, the contamination of a heat exchange element due to, for example, dust, bacteria, viruses or the like suspended in the outdoor air.
A heat exchanging unit according to a first aspect of the present invention comprises an indoor air exhaust passageway, an outdoor air supply passageway, a heat exchange element and a first air cleaning member. Furthermore, the “heat exchanging unit” herein includes both a total heat exchanging unit and a sensible heat exchanging unit. The indoor air exhaust passageway exhausts indoor air to an outdoor space as exhaust air. The outdoor air supply passageway supplies outdoor air to an indoor space as supply air. The heat exchange element exchanges at least the sensible heat of the sensible heat and the latent heat between the exhaust air and the supply air. Furthermore, the heat exchange element may be a fixed type or a rotational type. In addition, “sensible heat” herein specifically means temperature. In addition, “latent heat” herein specifically means humidity. In addition, the heat exchange element communicates with the indoor air exhaust passageway and the outdoor air supply passageway. The first air cleaning member is provided on the supply airflow upstream side of the heat exchange element. In addition, the first air cleaning member supports apatite that has a photocatalytic function. Furthermore, the “air cleaning member” herein is, for example, an air filter, an electric precipitator or the like. In addition, the “apatite that has a photocatalytic function” herein is an apatite wherein, for example, some of the calcium atoms of calcium hydroxyapatite are substituted by titanium atoms by a technique such as ion exchange or the like. In addition, the apatite that has a photocatalytic function may be supported on an air cleaning member by mixing it into, for example, a resin, or may be supported on the air cleaning member by coating it thereon. In addition, the apatite that has a photocatalytic function may be activated by a light source, such as an ultraviolet light lamp or an LED, by outdoor or indoor light, or by a plasma discharger and the like.
Herein, the first air cleaning member is provided on the supply airflow upstream side of the heat exchange element. In addition, the first air cleaning member supports the apatite that has a photocatalytic function. The apatite that has a photocatalytic function exhibits a decomposition capacity that is greater than titanium dioxide with respect to, for example, bacteria, viruses and the like. Consequently, if the photocatalytic function of the apatite that has a photocatalytic function can be activated, then this heat exchanging unit can prevent, more effectively than a conventional heat exchanging unit, the contamination of the heat exchange element due to, for example, dust, bacteria, viruses or the like suspended in the outdoor air.
A heat exchanging unit according to a second aspect of the present invention is a heat exchanging unit according to a first aspect of the present invention, further comprising a second air cleaning member. The second air cleaning member is provided on the exhaust airflow upstream side of the heat exchange element. In addition, the second air cleaning member supports the apatite that has a photocatalytic function.
If the heat exchange element is a rotational type or a moisture permeable fixed type (i.e., a total heat exchanging type), then some of the exhaust air or the return air will mix with the supply air, and the bacteria, viruses and the like present in the exhaust air or the return air will unfortunately return back with the supply air.
However, the second air cleaning member herein is provided on the exhaust airflow upstream side of the heat exchange element. In addition, the second air cleaning member supports the apatite that has a photocatalytic function. Consequently, with this heat exchanging unit, if the photocatalytic function of the apatite that has a photocatalytic function can be activated, then the bacteria, viruses and the like present in the exhaust air or the return air will be decomposed, destroyed or deactivated by the time they arrive at the heat exchange element. Accordingly, this heat exchanging unit can prevent the return of bacteria, viruses, and the like present in the exhaust air or the return air back with the supply air, regardless of whether the heat exchange element is a rotational type or a moisture permeable fixed type. In addition, the heat exchanging unit can also effectively prevent the contamination of the heat exchange element due to, for example, dust, bacteria or viruses suspended in the indoor air.
A heat exchanging unit according to a third aspect of the present invention is a heat exchanging unit according to a first aspect or a second aspect of the present invention, further comprising a photocatalytic function activating part. The photocatalytic function activating part activates the photocatalytic function of the apatite. Furthermore, the “photocatalytic function activating part” herein is, for example, an ultraviolet light lamp, an LED, a plasma discharger (such as a glow discharger, a barrier discharger, or a streamer discharger) or the like.
Here, the photocatalytic function activating part activates the photocatalytic function of the apatite. Consequently, the heat exchanging unit can also be disposed in outdoor and indoor where light does not reach.
A heat exchanging unit according to a fourth aspect of the present invention is a heat exchanging unit according to a third aspect of the present invention, wherein the photocatalytic function activating part irradiates the apatite that has a photocatalytic function with light in a predetermined wavelength range. Furthermore, the “photocatalytic function activating part” herein is, for example, an ultraviolet light lamp, a purple LED or the like.
Here, the photocatalytic function activating part irradiates the apatite that has a photocatalytic function with light in a predetermined wavelength range. Consequently, it is possible to use, for example, an ultraviolet light lamp or an LED in order to activate the photocatalytic function of the apatite that has a photocatalytic function. Accordingly, the manufacturing cost of the heat exchanging unit can be held down.
A heat exchanging unit according to a fifth aspect of the present invention is a heat exchanging unit according to a third aspect of the present invention, wherein the photocatalytic function activating part is provided on the airflow upstream side of the air cleaning member. In addition, the photocatalytic function activating part supplies activators to the apatite that has a photocatalytic function. Furthermore, the “photocatalytic function activating part” herein is, for example, a glow discharger, a barrier discharger, a streamer discharger or the like. The “activators” herein are, for example, high speed electrons, ions, ozone, radicals such as hydroxy radicals, other excited molecules (such as excited oxygen molecules, excited nitrogen molecules, and excited water molecules) and the like.
Here, the photocatalytic function activating part is provided on the airflow upstream side of the air cleaning member. Furthermore, the photocatalytic function activating part supplies activators to the apatite that has a photocatalytic function. Consequently, with this heat exchanging unit, the high energy radicals can activate the photocatalytic function of the apatite that has a photocatalytic function. Accordingly, it is possible to accelerate the photocatalytic reaction speed of the apatite that has a photocatalytic function. As a result, the heat exchanging unit can prevent, more effectively than a conventional heat exchanging unit, the contamination of the heat exchange element due to, for example, dust, bacteria, viruses or the like suspended in the outdoor air. In addition, it is known that ozone is extremely effective against a bactericide and the like. Consequently, the heat exchanging unit can prevent, more effectively than a conventional heat exchanging unit, the contamination of the heat exchange element due to, for example, dust, bacteria, viruses or the like suspended in the outdoor air.
A heat exchanging unit according to a sixth aspect of the present invention is a heat exchanging unit according to a fifth aspect of the present invention, further comprising an air distribution part and an operation switching unit. Furthermore, the “air distribution part” herein is, for example, a fan. The air distribution part distributes the air. The operation switching unit switches the operation state of the air distribution part. Furthermore, the “operation switching unit” herein is, for example, a control device that switches the rotational speed of the impeller of a fan.
Here, the operation switching unit switches the operation state of the air distribution part. Consequently, a high concentration of activators is supplied to the air cleaning member if the photocatalytic function activating part is used in a state wherein, for example, during normal operation, dust, bacteria, viruses and the like are captured in advance by the air cleaning member without making use of the photocatalytic function activating part, operation is then switched to a cleaning operation mode after a fixed time, and the air volume of the fan is maximally suppressed. Accordingly, with this heat exchanging unit, the air cleaning member can be cleaned selectively and effectively.
If the photocatalytic function of the apatite that has a photocatalytic function can be activated, then the heat exchanging unit of the first aspect of the invention can prevent, more effectively than a conventional heat exchanging unit, the contamination of the heat exchange element due to, for example, dust, bacteria, viruses or the like suspended in the outdoor air.
With the heat exchanging unit of the second aspect of the invention, if the photocatalytic function of the apatite that has a photocatalytic function can be activated, then the bacteria, viruses and the like present in the exhaust air or the return air will be decomposed, destroyed or deactivated by the time they arrive at the heat exchange element. Accordingly, this heat exchanging unit can prevent the return of bacteria, viruses, and the like present in the exhaust air or the return air back with the supply air, regardless of whether the heat exchange element is a rotational type or a moisture permeable fixed type. In addition, the heat exchanging unit can also effectively prevent the contamination of the heat exchange element due to, for example, dust, bacteria, viruses or the like suspended in the indoor air.
The heat exchanging unit of the third aspect of the invention can also be disposed in outdoor and indoor where light does not reach.
The manufacturing cost of the heat exchanging unit according to the fourth aspect of the invention can be held down.
The heat exchanging unit according to the fifth aspect of the invention can prevent, more effectively than a conventional heat exchanging unit, the contamination of the heat exchange element due to, for example, dust, bacteria, viruses or the like suspended in the outdoor air. In addition, it is known that ozone is extremely effective against a bactericide and the like. Consequently, the heat exchanging unit can prevent, more effectively than a conventional heat exchanging unit, the contamination of the heat exchange element due to, for example, dust, bacteria, viruses or the like suspended in the outdoor air.
With the heat exchanging unit according to the sixth aspect of the invention, the air cleaning member can be cleaned selectively and effectively.
(Constitution of the Total Heat Exchanging Unit)
As shown in
(Constituent Elements of the Total Heat Exchanging Unit)
(1) Casing
As shown in
A. Heat Exchange Element Chamber
The heat exchange element chamber 21 is a rectangular parallelepipedic space, as shown in
Furthermore, housing the heat exchange element 12 in the heat exchange element chamber 21 creates four substantially triangular prism shaped spaces 17, 18, 19, 20 therein. Hereinbelow, the spaces indicated by reference symbols 17, 18, 19, and 20 in
B. Exhaust Air Fan Housing Chamber
The exhaust air fan housing chamber 22 houses the exhaust air fan 10, as shown in
C. Exhaust Air Fan Motor Housing Chamber
The exhaust air fan motor housing chamber 41 houses an exhaust air fan motor 10M, as shown in
D. Supply Air Fan Housing Chamber
The supply air fan housing chamber 24 houses the supply air fan 11, as shown in
E. Supply Air Fan Motor Housing Chamber
The supply air fan motor housing chamber 43 houses a supply air fan motor 11M, as shown in
F. Outdoor Side Suction Chamber
The outdoor side suction chamber 26 comprises a supply air outdoor side suction port 5 on its side wall, as shown in
G. Indoor Side Suction Chamber
The indoor side suction chamber 27 comprises an exhaust air indoor side suction port 4 on its side wall, as shown in
H. Supply Air Communicating Chamber
The supply air communicating chamber 45 is partitioned by the partition plate 16F, and is positioned below the exhaust air fan motor housing chamber 41. In addition, the supply air communicating chamber 45 communicates with the third space 19, as shown in
I. Exhaust Air Communicating Chamber
The exhaust air communicating chamber 46 is partitioned by the partition plate 16G, and is positioned below the supply air fan motor housing chamber 43. In addition, the exhaust air communicating chamber 46 communicates with the fourth space 20, as shown in
J. Bypass Chamber
The bypass chamber 31 is positioned on the side opposite an extraction direction k of the heat exchange element chamber 21. Furthermore, the bypass chamber 31 communicates with the first space 17 via an opening 32. In addition, the bypass chamber 31 communicates with the indoor side suction chamber 27 via an opening 33. As a result, the exhaust air fan housing chamber 22 and the indoor side suction chamber 27 communicate via the exhaust air fan motor housing chamber 41, the first space 17, and the bypass chamber 31.
(2) Heat Exchange Element
The heat exchange element 12 is formed substantially as a rectangular parallelepiped, as shown in
Furthermore, a handle 12a for removing the heat exchange element 12 is provided to an end surface of the heat exchange element 12, which can be inserted or removed in the longitudinal direction along its long side via an insertion/removal opening 13, which is open to a maintenance surface M of the casing 1, by removing a cover 14 as shown in
(3) Air Filter
As shown in
(4) Ultraviolet Light Lamps
The ultraviolet light lamps 15 are provided to the third space 19 and the fourth space 20, respectively, and the supply of ultraviolet light thereby activates the photocatalytic function of the titanium apatite supported on the air filters 12b.
(5) Fan
The exhaust air fan 10 and the supply air fan 11 are sirocco fans (rotors), as shown in
(6) Damper
The damper 34 is disposed inside the indoor side suction chamber 27. The damper 34 is pivoted by, for example, an electric motor (not shown) that opens either the opening 30 or the opening 33 and blocks the other.
(7) Electrical Equipment Box
The electrical equipment box EB is disposed in a portion M1, which opposes the exhaust air fan 10, of the maintenance surface M. The electrical equipment box EB houses electrical equipment, such as a control circuit board (not shown). Furthermore, the control circuit board is connected to and in communication with a wired remote control (not shown), and controls the operation of the fans 10, 11 and the damper 34 based on signals sent from the wired remote control.
(Performance of Titanium Apatite on Bacteria and Viruses)
Table 1 shows the percentage of viruses, bacteria, and toxins inactivated by titanium apatite.
Furthermore, these inactivity percentages were measured at Japan Food Research Laboratories by the methods described below.
1. Inactivity Percentage of Influenza Virus
(1) Test Overview
An influenza virus suspension was dropped onto titanium apatite-coated filters (approximately 30×30 mm) and preserved at room temperature under dark (shielded from light) and light (black light irradiation with a distance of approximately 20 cm between the filter and the black light) conditions; after 24 hours, the virus infectivity titer was measured.
(2) Calculation of Inactivity Percentage
Inactivity percentage=100×(1−10B/10A)
(3) Test Method
A. Test Virus: Influenza Virus Type A (H1N1)
B. Cells: MDCK (NBL-2) Cells, ATCC CCL-34 (Dainippon Pharmaceutical Co., Ltd.)
C. Culture Medium
The following tissue culture was used:
D. Preparation of Virus Suspension
a) Cell Culture
A monolayer culture of MDCK cells was incubated in a tissue culture flask using a cell growth medium.
b) Seeding of Virus
After monolayer incubation, the cell growth medium was eliminated from the flask, and the culture was seeded with the test virus. Next, the cell maintenance medium was added and then incubated for 2 to 5 days at 37° C. in a CO2 incubator (CO2 concentration of 5%).
c) Preparation of Virus Suspension
After incubation, an inverted phase contrast microscope was used to observe the cytomorphology, and a morphological change (cytopathic effect) was confirmed in over 80% of the cells. Next, the culture solution was centrifugally isolated (3,000 rpm for 10 min), and the obtained supernatant liquid was used as the virus suspension.
E. Preparation of Sample
After the filter (approximately 30×30 mm) was sterilized with moist heat (121° C. for 15 min), it was air dried for one hour, placed in a plastic Petri dish, irradiated with black light (black light blue, two FL20S BL-B 20W bulbs in parallel) for over 12 hours, and then used as a sample.
F. Test Operation
0.2 mL of the virus suspension was dropped onto the sample. The samples were maintained at room temperature under light shielded and black light irradiation (distance of approximately 20 cm between the filter and the black light) conditions. In addition, polyethylene film was used as the control sample, and tested in the same manner.
G. Washing Out the Virus
After the above conditions were preserved for 24 hours, 2 mL of the cell maintenance medium was used to wash out the virus suspension in the test specimen.
H. Measurement of Virus Infectivity Titer
The cell growth medium was used to incubate a monolayer culture of MDCK cells in a tissue culture microplate (96 wells), after which the cell growth medium was eliminated and the cell maintenance medium was added 0.1 mL at a time. Next, a washout liquid and 0.1 mL of a diluted solution thereof were used to seed 4 wells each, which were then incubated for 4 to 7 days at 37° C. in a CO2 incubator (5% CO2 concentration). After incubation, an inverted phase contrast microscope was used to observe the presence of cytomorphological change (cytopathic effect), and the 50% tissue culture infectious dose (TCID50) was computed using the Reed-Muench method and then used the result to calculate the virus infectivity titer per milliliter of the washout liquid.
2. Inactivity percentages of Escherichia coli (0157), Staphylococcus aureus, and Cladosporium
(1) Test Overview
The antimicrobial activity of filters were tested, referencing the test method of the Society of Industrial-Technology for Antimicrobial Articles, i.e., Assay Antimicrobial Activity III for Antimicrobial Processed Products (2001 Edition) Light Irradiation Film Contact Method (hereinafter, referred to as the “Light Irradiation Film Contact Method—SIAA 2001 Edition”).
Furthermore, testing was performed as follows.
Bacterial suspensions of Escherichia coli, staphylococcus aureus, and Cladosporium were dropped onto samples, which were then sealed by covering them with a low density polyethylene film. These samples were preserved at room temperature (20°-25° C.) under dark (shielded from light) and light (black light irradiation with a distance of approximately 20 cm between the filters and the black light) conditions; after 24 hours, the viable cell count was measured.
(2) Test Method
A. Test Strain
Microbes:
Fungi:
B. Test Culture
C. Preparation of Bacterial Suspensions
Microbes
Test strains were incubated beforehand in the NA medium at 35° C. for 16 to 24 hours, the NA medium was reseeded with that culture, and the bacteria bodies, which were incubated at 35° C. for 16 to 20 hours, were evenly dispersed in the 1/500 NB medium, and then prepared so that the bacteria count per milliliter was 2.5×105 to 1.0×106.
Fungi
After incubation in a PDA medium for 7 to 10 days at 25° C., the spores (conidias) were suspended in a 0.005% dioctyl sodium sulfosuccinate solution, filtered with gauze, and then prepared so that the spore count per milliliter was 2.5×105 to 1.0×106.
D. Preparation of Samples
After each filter (approximately 50×50 mm) was sterilized with moist heat (121° C. for 15 min), it was air dried for one hour, placed in a plastic Petri dish, irradiated for over 12 hours with black light (black light blue, two FL20S BL-B 20W bulbs in parallel), and then used as a sample.
E. Test Operation
0.4 mL of each bacterial suspension was dropped onto a sample, which was then sealed by covering it with low density polyethylene film (40×40 mm). The samples were preserved at room temperature (20°-25° C.) under light shielded and black light irradiation (with a distance of approximately 20 cm between the filter and the black light) conditions. In addition, the polyethylene film was used as the control sample and tested in the same manner.
F. Measurement of Viable Cell Count
After the above conditions were preserved for 24 hours, the surviving bacteria were washed out from each sample with the SCDLP medium and the viable cell count of the washout liquid was measured by the poured plate culture method, wherein the SA medium was used for the microbes (incubated for 2 days at 35° C.) and the PDA medium was used for the fungi (incubated for 7 days at 25° C.); thereafter, the viable cell count per sample was calculated. In addition, immediately after seeding, this measurement was performed on the control sample.
3. Inactivity Percentage of the Enterotoxin
(1) Test Overview
The samples were seeded with staphylococcal enterotoxin A (hereinafter, abbreviated as “SET-A”) and then preserved at room temperature (20°-25° C.) under dark (shielded from light) and light (irradiated with ultraviolet light with a luminous flux of approximately 1 mW/cm2) conditions; 24 hours later, the concentration of the SET-A was measured and the decomposition percentage was calculated.
(2) Test Method
A. Preparation of Standard Stock Solution
A 5 μg/mL standard stock solution was prepared by dissolving a SET-A reference sample (Toxin Technology Inc.) in a 1% sodium chloride solution containing 0.5% bovine serum albumin.
B. Standard Solution Used for the Calibration Curve
Standard solutions of 0.2, 0.5, and 1 ng/mL were prepared by diluting the standard stock solution with the buffer solution included with the VIDAS staphylococcus enterotoxin (SET) test kit (bioMerieux, Inc.).
C. Preparation of Samples
The filter was cut into 50×50 mm pieces, irradiated for 24 hours with a black light from a distance of approximately 1 cm, and then used as the samples.
D. Test Operation
Each sample was placed in a plastic Petri dish and seeded with 0.4 mL of SET-A standard stock solution. The samples were preserved at room temperature (20°-25° C.) under light shielded and light irradiation (black light, two FL20S BL-B 20W bulbs in parallel), with an ultraviolet light luminous flux of approximately 1 mW/cm2 conditions.
After the above conditions were preserved for 24 hours, the SET-A was washed out from each sample with 10 mL of a buffer solution, which was included in the VIDAS staphylococcus enterotoxin (SET) test kit (bioMerieux, Inc.).
Furthermore, a plastic Petri dish, wherein a sample was not placed, was seeded with 0.4 mL of SET-A standard stock solution, and then 10 mL of buffer solution, which was included in the VIDAS staphylococcus enterotoxin (SET) test kit (bioMerieux, Inc.), was immediately added, and the result was used as the control.
E. Generation of the Calibration Curve
The concentration and the fluorescent light intensity of the calibration curve standard solution were measured by the ELISA method using a VIDAS staphylococcus enterotoxin (SET) test kit (bioMerieux, Inc.), and the calibration curve was generated based on those measurements.
F. Measurement of SET-A Concentration and Calculation of Decomposition Percentage
The fluorescent light intensity of the sample solution was measured by the ELISA method using a VIDAS staphylococcus enterotoxin (SET) test kit (bioMerieux, Inc.), the SET-A concentration was derived from the calibration curve generated in Step E, and the decomposition percentage was calculated by the following expression:
Decomposition percentage (%)=(Control measured value−Sample solution measured value)/Control measured value×100
(Supply Air and Exhaust Air Flows)
The total heat exchanging unit 100 is provided with three operation modes, i.e., a total heat exchange ventilation mode, a normal ventilation mode, and the air filter cleaning mode. The following describes the details of each of these operation modes.
(1) Total Heat Exchange Ventilation Mode
With the total heat exchanging unit 100, if total heat exchange ventilation is performed using the heat exchange element 12, then the damper 34 opens the opening 30. Furthermore, as discussed above, the opening 33 is blocked at this time. Furthermore, if the fans 10, 11 are operated in this state, the indoor air is suctioned via a duct from the indoor side suction port 4 into the indoor side suction chamber 27, passes through the exhaust air passageway 8, which extends from the opening 30 to the exhaust air communicating chamber 46, the fourth space 20, the air filters 12b, the heat exchange element 12, the first space 17, the opening 23, the exhaust air fan motor housing chamber 41, and the exhaust air fan housing chamber 22, and is then blown out from the outdoor side blow out port 7 and exhausted to the outdoor space via a duct; simultaneously, the outdoor air is suctioned via a duct from the outdoor side suction port 5 into the outdoor side suction chamber 26, passes through the supply air passageway 9, which extends from the supply air communicating chamber 45 to the third space 19, the air filters 12b, the heat exchange element 12, the second space 18, the opening 25, the supply air fan motor housing chamber 43, the opening 44, and the supply air fan housing chamber 24, and is then blown out from the indoor side blow out port 6 and supplied via a duct to the indoor space.
(2) Normal Ventilation Mode
Normal ventilation, which does not perform heat exchange, is performed during intermediate seasons, such as spring and fall, when cooling and heating are not needed.
When normal ventilation is performed with the total heat exchanging unit 100, the damper 34 opens the opening 33. Furthermore, as discussed above, the opening 30 is blocked at this time. Furthermore, if the fans 10, 11 are operated in this state, the indoor air is suctioned via a duct from the indoor side suction port 4 into the indoor side suction chamber 27, passes through a bypass ventilation passageway, which extends from the opening 33 to the bypass chamber 31, the opening 32, the first space 17, the opening 23, exhaust air fan motor housing chamber 41, and the exhaust air fan housing chamber 22, and is then blown out from the outdoor side blow out port 7 and exhausted via a duct to the outdoor space; simultaneously, the outdoor air is suctioned via a duct from the outdoor side suction port 5 into the outdoor side suction chamber 26, passes through the supply air passageway 9, which extends from the supply air communicating chamber 45 to the third space 19, the air filters 12b, the heat exchange element 12, the second space 18, the opening 25, the supply air fan motor housing chamber 43, the opening 44, and the supply air fan housing chamber 24, and is then blown out from the indoor side blow out port 6 and supplied via a duct to the indoor space (the flow of the supply air is the same as for the case of total heat exchange ventilation).
(Features of the Total Heat Exchanging Unit)
(1)
With the total heat exchanging unit 100 according to the present embodiment, the heat exchange element 12 is a total heat exchanging type that comprises the moisture permeable spacer paper 122 and the partitioning paper 121. Furthermore, an air filter 12b is provided to the heat exchange element 12 not only on the supply airflow upstream side, but also on the exhaust airflow upstream side. In addition, both air filters 12b support titanium apatite. Furthermore, the catalytic function of the titanium apatite is activated by ultraviolet light lamps 15, which are provided nearby. Titanium apatite exhibits decomposition capacity with respect to, for example, bacteria, viruses and the like that is stronger than titanium dioxide of the anatase form. Consequently, the total heat exchanging unit 100 can prevent, more effectively than a conventional heat exchanging unit, contamination of the heat exchange element 12 due to, for example, dust, bacteria, viruses or the like suspended in the outdoor air.
(2)
According to the present embodiment, the ultraviolet light lamps 15 are provided to the total heat exchanging unit 100 in the vicinity of the air filters 12b. Consequently, the total heat exchanging unit 100 can also be disposed in outdoor and indoor where light does not reach.
(3)
With the total heat exchanging unit 100 according to the present embodiment, the catalytic function of the titanium apatite is activated by the ultraviolet light lamps 15. Accordingly, it is possible to hold down the manufacturing cost of the total heat exchanging unit 100.
(A)
With the total heat exchanging unit 100 according to the previous embodiment, the heat exchange element 12 is a total heat exchanging type that comprises the moisture permeable spacer paper 122 and partitioning paper 121, but the heat exchange element 12 may also be a sensible heat exchange type (a so-called heat pipe type heat exchange element) that comprises a moisture impermeable spacer plate and partition plate. Furthermore, with the sensible heat exchange type heat exchange element, only sensible heat is exchanged between the supply air and the exhaust air. In this case, a constitution may be adopted wherein an air filter 12b is provided only on the supply airflow upstream side. This is because, with the sensible heat exchange type heat exchange element, the supply air and the exhaust air do not mix, and therefore there is no risk that the dust, bacteria, viruses or the like contained in the exhaust air will mix into the supply air.
(B)
With the total heat exchanging unit 100 according to the previous embodiment, the heat exchange element is a fixed type, but may be a rotational type heat exchange element 220, as shown in
The heat exchanging unit 200 principally comprises a casing 201, the heat exchange elements 220, air filters 220b, an ultraviolet light lamp (not shown), and fans 210, 211, as shown in
When the fans 210, 211 of the heat exchanging unit 200 operate, the indoor air is sucked into an indoor side suction port 254 via a duct, passes through an exhaust air passageway that extends from the air filters 220b to the heat exchange element 220 and the exhaust air fan 210, is then blown out from an outdoor side blow out port 257 and exhausted to the outdoor space via a duct; simultaneously, outdoor air is sucked into an outdoor side suction port 255 via a duct, passes through a supply air passageway that extends from the air filters 220b to the heat exchange element 220 and the supply air fan 211, and is then blown out from an indoor side blow out port 256 and supplied to the indoor space via a duct.
(C)
The total heat exchanging unit 100 according to the previous embodiment employs the ultraviolet light lamps 15 in order to activate the catalytic function of the titanium apatite, but an LED may be used instead. Doing so can contribute to energy conservation and a reduction in the global environmental load (because mercury is not used in the LED), and can also hold down manufacturing costs.
(D)
The total heat exchanging unit 100 according to the previous embodiment uses the ultraviolet light lamps 15 in order to activate the catalytic function of the titanium apatite; however, if the total heat exchanging unit 100 is installed in outdoor or indoor where light reaches, then at least one of the casing 1 and the cover body 3 may be made transparent, and the titanium apatite may be activated by at least one of outdoor light and indoor light.
The total heat exchanging unit 100 according to the previous embodiment uses the ultraviolet light lamps 15 in order to activate the catalytic function of the titanium apatite, but a streamer discharger, a glow discharger, a barrier discharger, or the like may be used instead. By disposing such a discharger in the total heat exchanging unit 100, it is possible to supply, for example, ozone and high energy radicals that have a bactericidal effect on the titanium apatite. Accordingly, the total heat exchanging unit 100 increases the bactericidal effect and can also accelerate the photocatalytic reaction speed of the titanium apatite. As a result, the heat exchanging unit 100 can prevent, more effectively than a conventional heat exchanging unit, the contamination of the heat exchange element 12 due to, for example, dust, bacteria, or viruses that are suspended in the outdoor air.
Furthermore, if the total heat exchanging unit 100 is provided with a plasma discharger, then an air filter cleaning mode may be made available in addition to the total heat exchange ventilation mode and the normal ventilation mode. In the air filter cleaning mode, the rotational speed of the fans 10, 11 is controlled so that it transitions to a state wherein the amount of ventilation is suppressed as much as possible. Furthermore, the plasma discharger may be constituted so that it is energized only in this mode, or so that it is continuously energized. In so doing, a high concentration of radicals is supplied to the air filters 12b. Accordingly, with the total heat exchanging unit 100, it is possible to selectively and efficiently purify the air filters 12b.
(F)
With the total heat exchanging unit 100 according to the previous embodiment, titanium apatite is supported in a form wherein it is embedded in the enveloping layer of the polypropylene fibers, but it may be coated thereon.
(G)
With the total heat exchanging unit 100 according to the previous embodiment, polypropylene fibers are used as the support body of the titanium apatite, but the support body of the titanium apatite is not limited thereto. For example, it is possible to use various kinds of plastic fibers and natural fibers.
(H)
With the total heat exchanging unit 100 according to the previous embodiment, titanium apatite is supported in a form wherein it is embedded in the enveloping layer of the polypropylene fibers, but it may be coated on one or both sides of each air filter 12b.
A heat exchanging unit according to the present invention can prevent, more effectively than a conventional heat exchanging unit, the contamination of a heat exchange element due to, for example, dust, bacteria, viruses or the like suspended in the outdoor air, and can also be adapted to applications such as an air conditioner or an air cleaner.
| Number | Date | Country | Kind |
|---|---|---|---|
| 2004-120843 | Apr 2004 | JP | national |
| Filing Document | Filing Date | Country | Kind | 371c Date |
|---|---|---|---|---|
| PCT/JP05/05727 | 3/28/2005 | WO | 10/3/2006 |
