JPS6335918B2 - - Google Patents
Info
- Publication number
- JPS6335918B2 JPS6335918B2 JP55164299A JP16429980A JPS6335918B2 JP S6335918 B2 JPS6335918 B2 JP S6335918B2 JP 55164299 A JP55164299 A JP 55164299A JP 16429980 A JP16429980 A JP 16429980A JP S6335918 B2 JPS6335918 B2 JP S6335918B2
- Authority
- JP
- Japan
- Prior art keywords
- deodorizing
- total heat
- duct
- zone
- exhaust
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired
Links
- 230000001954 sterilising effect Effects 0.000 claims description 24
- 239000000463 material Substances 0.000 claims description 21
- 230000001877 deodorizing effect Effects 0.000 claims description 14
- 230000008929 regeneration Effects 0.000 claims description 11
- 238000011069 regeneration method Methods 0.000 claims description 11
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 10
- 239000011358 absorbing material Substances 0.000 claims description 10
- 238000004659 sterilization and disinfection Methods 0.000 claims description 10
- 239000010425 asbestos Substances 0.000 claims description 4
- 239000004744 fabric Substances 0.000 claims description 4
- 229910052895 riebeckite Inorganic materials 0.000 claims description 4
- 229920000049 Carbon (fiber) Polymers 0.000 claims description 3
- 239000000123 paper Substances 0.000 claims description 3
- 238000010926 purge Methods 0.000 claims description 3
- 239000010419 fine particle Substances 0.000 claims description 2
- 239000003230 hygroscopic agent Substances 0.000 claims 1
- 239000004745 nonwoven fabric Substances 0.000 claims 1
- 239000007789 gas Substances 0.000 description 23
- MWUXSHHQAYIFBG-UHFFFAOYSA-N nitrogen oxide Inorganic materials O=[N] MWUXSHHQAYIFBG-UHFFFAOYSA-N 0.000 description 6
- 238000010521 absorption reaction Methods 0.000 description 4
- 241000894006 Bacteria Species 0.000 description 3
- 238000003795 desorption Methods 0.000 description 3
- 239000003960 organic solvent Substances 0.000 description 3
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 description 2
- 239000002250 absorbent Substances 0.000 description 2
- 230000002745 absorbent Effects 0.000 description 2
- 239000011162 core material Substances 0.000 description 2
- KWGKDLIKAYFUFQ-UHFFFAOYSA-M lithium chloride Chemical compound [Li+].[Cl-] KWGKDLIKAYFUFQ-UHFFFAOYSA-M 0.000 description 2
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical class C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 2
- 229920006395 saturated elastomer Polymers 0.000 description 2
- 229920003002 synthetic resin Polymers 0.000 description 2
- 239000000057 synthetic resin Substances 0.000 description 2
- UXVMQQNJUSDDNG-UHFFFAOYSA-L Calcium chloride Chemical compound [Cl-].[Cl-].[Ca+2] UXVMQQNJUSDDNG-UHFFFAOYSA-L 0.000 description 1
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 1
- 238000004887 air purification Methods 0.000 description 1
- 239000007864 aqueous solution Substances 0.000 description 1
- 239000011230 binding agent Substances 0.000 description 1
- 229910001628 calcium chloride Inorganic materials 0.000 description 1
- 239000001110 calcium chloride Substances 0.000 description 1
- 229910002091 carbon monoxide Inorganic materials 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000003365 glass fiber Substances 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 238000002791 soaking Methods 0.000 description 1
- XTQHKBHJIVJGKJ-UHFFFAOYSA-N sulfur monoxide Chemical class S=O XTQHKBHJIVJGKJ-UHFFFAOYSA-N 0.000 description 1
- 229910052815 sulfur oxide Inorganic materials 0.000 description 1
Classifications
-
- G—PHYSICS
- G11—INFORMATION STORAGE
- G11B—INFORMATION STORAGE BASED ON RELATIVE MOVEMENT BETWEEN RECORD CARRIER AND TRANSDUCER
- G11B13/00—Recording simultaneously or selectively by methods covered by different main groups among G11B3/00, G11B5/00, G11B7/00 and G11B9/00; Record carriers therefor not otherwise provided for; Reproducing therefrom not otherwise provided for
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24F—AIR-CONDITIONING; AIR-HUMIDIFICATION; VENTILATION; USE OF AIR CURRENTS FOR SCREENING
- F24F3/00—Air-conditioning systems in which conditioned primary air is supplied from one or more central stations to distributing units in the rooms or spaces where it may receive secondary treatment; Apparatus specially designed for such systems
- F24F3/12—Air-conditioning systems in which conditioned primary air is supplied from one or more central stations to distributing units in the rooms or spaces where it may receive secondary treatment; Apparatus specially designed for such systems characterised by the treatment of the air otherwise than by heating and cooling
- F24F3/14—Air-conditioning systems in which conditioned primary air is supplied from one or more central stations to distributing units in the rooms or spaces where it may receive secondary treatment; Apparatus specially designed for such systems characterised by the treatment of the air otherwise than by heating and cooling by humidification; by dehumidification
- F24F3/1411—Air-conditioning systems in which conditioned primary air is supplied from one or more central stations to distributing units in the rooms or spaces where it may receive secondary treatment; Apparatus specially designed for such systems characterised by the treatment of the air otherwise than by heating and cooling by humidification; by dehumidification by absorbing or adsorbing water, e.g. using an hygroscopic desiccant
- F24F3/1423—Air-conditioning systems in which conditioned primary air is supplied from one or more central stations to distributing units in the rooms or spaces where it may receive secondary treatment; Apparatus specially designed for such systems characterised by the treatment of the air otherwise than by heating and cooling by humidification; by dehumidification by absorbing or adsorbing water, e.g. using an hygroscopic desiccant with a moving bed of solid desiccants, e.g. a rotary wheel supporting solid desiccants
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24F—AIR-CONDITIONING; AIR-HUMIDIFICATION; VENTILATION; USE OF AIR CURRENTS FOR SCREENING
- F24F2203/00—Devices or apparatus used for air treatment
- F24F2203/10—Rotary wheel
- F24F2203/1032—Desiccant wheel
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24F—AIR-CONDITIONING; AIR-HUMIDIFICATION; VENTILATION; USE OF AIR CURRENTS FOR SCREENING
- F24F2203/00—Devices or apparatus used for air treatment
- F24F2203/10—Rotary wheel
- F24F2203/104—Heat exchanger wheel
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24F—AIR-CONDITIONING; AIR-HUMIDIFICATION; VENTILATION; USE OF AIR CURRENTS FOR SCREENING
- F24F2203/00—Devices or apparatus used for air treatment
- F24F2203/10—Rotary wheel
- F24F2203/1068—Rotary wheel comprising one rotor
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24F—AIR-CONDITIONING; AIR-HUMIDIFICATION; VENTILATION; USE OF AIR CURRENTS FOR SCREENING
- F24F2203/00—Devices or apparatus used for air treatment
- F24F2203/10—Rotary wheel
- F24F2203/1076—Rotary wheel comprising three rotors
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24F—AIR-CONDITIONING; AIR-HUMIDIFICATION; VENTILATION; USE OF AIR CURRENTS FOR SCREENING
- F24F2203/00—Devices or apparatus used for air treatment
- F24F2203/10—Rotary wheel
- F24F2203/1084—Rotary wheel comprising two flow rotor segments
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24F—AIR-CONDITIONING; AIR-HUMIDIFICATION; VENTILATION; USE OF AIR CURRENTS FOR SCREENING
- F24F2203/00—Devices or apparatus used for air treatment
- F24F2203/10—Rotary wheel
- F24F2203/1096—Rotary wheel comprising sealing means
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Combustion & Propulsion (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Central Air Conditioning (AREA)
- Packaging Of Annular Or Rod-Shaped Articles, Wearing Apparel, Cassettes, Or The Like (AREA)
Description
【発明の詳細な説明】
平面状シート素材１と波形シート素材２との少
なくとも一方を活性カーボン繊維混入紙の如きガ
ス吸収性材料で構成し、第１図に示す如く該平面
状シート素材１と波形シート素材２とを交互に接
着積層して芯材３に巻き重ね、両端面に小透孔４
が透通した円筒状に形成してなる脱臭殺菌全熱交
換用ローター５は既に提案されている。DETAILED DESCRIPTION OF THE INVENTION At least one of the planar sheet material 1 and the corrugated sheet material 2 is made of a gas-absorbing material such as activated carbon fiber-containing paper, and as shown in FIG. The corrugated sheet materials 2 are alternately bonded and laminated and rolled around the core material 3, and small through holes 4 are formed on both end surfaces.
A rotor 5 for deodorizing and sterilizing total heat exchange, which is formed into a cylindrical shape through which the rotor 5 is transparent, has already been proposed.
この脱臭殺菌全熱交換用ローター５は第１図お
よび第２図に示す如くケーシング１８のパージス
ポーク６によつて入気ゾーン７と排気ゾーン８と
再生殺菌ゾーン９とに分離し、入気ゾーン７には
外気用ダクト１０と給気用ダクト１１とを取付
け、排気ゾーン８には還気用ダクト１２と排気用
ダクト１３とを取付け、再生殺菌ゾーン９には熱
風送入用ダクト１４と排気用ダクト１５とを取付
け、ローター５を低速で回転させ、入気ゾーン７
にたとえば低温の外気OAを通し、排気ゾーン８
にたとえば高温の還気RAを通すことにより、還
気RAに含まれる全熱を回収して入気SAに取入
れ再使用するとともに、入気ゾーン７においてロ
ーター５のガス吸収性材料により外気OA中の活
性ガス即ち有機溶剤蒸気、オゾン、窒素酸化物の
如き有害ガスを吸着除去してきれいな給気SAを
室内に供給し、間歇的に熱風送入用ダクト１４よ
り再生殺菌ゾーン９に熱風を送入し、ローター５
のガス吸収性材料に吸着した有害ガスを脱着しロ
ーター５を再生するものであるが、ローター５の
ガス吸収性材料は排気ゾーン８においても還気
RAに含まれる活性ガスを吸着除去し比較的清浄
となつた空気が排気EAとして外気中に排出され
る。 As shown in FIGS. 1 and 2, this deodorizing and sterilizing total heat exchange rotor 5 is separated into an inlet zone 7, an exhaust zone 8, and a regeneration sterilization zone 9 by a purge spoke 6 of a casing 18. An outside air duct 10 and a supply air duct 11 are attached to the exhaust zone 7, a return air duct 12 and an exhaust duct 13 are attached to the exhaust zone 8, and a hot air supply duct 14 and an exhaust air duct are attached to the regeneration sterilization zone 9. duct 15 and rotate the rotor 5 at low speed to open the intake zone 7.
For example, pass low-temperature outside air OA to exhaust zone 8.
For example, by passing high-temperature return air RA through, the total heat contained in the return air RA is recovered and taken into the inlet air SA for reuse. Active gases such as organic solvent vapor, ozone, and harmful gases such as nitrogen oxides are adsorbed and removed to supply clean air SA into the room, and hot air is intermittently sent to the regeneration sterilization zone 9 from the hot air delivery duct 14. Insert, rotor 5
The rotor 5 is regenerated by desorbing harmful gases adsorbed to the gas absorbing material of the rotor 5, but the gas absorbing material of the rotor 5 also absorbs return air in the exhaust zone
The active gases contained in the RA are adsorbed and removed, and the relatively clean air is discharged into the outside air as exhaust EA.
本発明はこの空気清浄化の観点で見たとき無駄
に排出される清浄な排気EAを給気の一部として
再利用しようとするもで、以下実施例を図面につ
いて詳細に説明する。 The present invention attempts to reuse clean exhaust gas EA, which is wastefully discharged from the viewpoint of air purification, as part of the air supply, and embodiments will be described in detail below with reference to the drawings.
実施例 １
第１図に示す如く紙、布、アスベスト紙、合成
紙、合成樹脂シートの如き材料よりなる平面状シ
ート素材１と活性カーボン微粒子を付着した紙、
布、アスベスト紙、合成紙、合成樹脂シートの如
き材料よりなる波形シート素材２とを交互に接着
積層して芯材３に巻き重ね、両端面に小透孔４が
透通した円筒状に形成して脱臭殺菌全熱交換用ロ
ーター５を得、第１図、第３図に示す如くケーシ
ング１８に入れて原動機（図示せず）により第１
図矢印の如く駆動回転し得るように保持し、ケー
シング１８のパージスポーク６により入気ゾーン
７、排気ゾーン８、再生殺菌ゾーン９に分離し、
入気ゾーン７には外気用ダクト１０と給気用ダク
ト１１とを連設し、排気ゾーン８には還気用ダク
ト１２と排気用ダクト１３とを連設し、再生殺菌
ゾーン９には第２図に示す如く熱風送入用ダクト
１４と排気用ダクト１５とを連設し、第３図に示
す如く外気用ダクト１０と排気用ダクト１３とは
バイパス１７により連結し、バイパス１７にはダ
ンパー１６を設け更に排気用ダクト１３にはダン
パー１９を設けてなる脱臭殺菌全熱交換器であ
り、ダンパー１６，１９の開閉度を調節すること
により排気EAを外気OA側に送り込む量を加減
するようにしたものである。尚再生殺菌ゾーン９
は中心角18゜〜36゜程度とする。Example 1 As shown in FIG. 1, a planar sheet material 1 made of a material such as paper, cloth, asbestos paper, synthetic paper, or synthetic resin sheet, and paper to which activated carbon fine particles are attached,
Corrugated sheet materials 2 made of materials such as cloth, asbestos paper, synthetic paper, and synthetic resin sheets are alternately bonded and laminated and wound around a core material 3 to form a cylindrical shape with small through holes 4 on both ends. The rotor 5 for deodorizing and sterilizing total heat exchange is obtained, and as shown in FIGS.
It is held so that it can be driven and rotated as shown by the arrow in the figure, and is separated into an intake zone 7, an exhaust zone 8, and a regeneration sterilization zone 9 by the purge spoke 6 of the casing 18.
The intake zone 7 is provided with an outside air duct 10 and a supply air duct 11, the exhaust zone 8 is provided with a return air duct 12 and an exhaust duct 13, and the regeneration sterilization zone 9 is provided with an external air duct 10 and a supply air duct 11. As shown in FIG. 2, a hot air supply duct 14 and an exhaust duct 15 are connected, and as shown in FIG. It is a deodorizing and sterilizing total heat exchanger which is provided with a damper 19 in the exhaust duct 13, and by adjusting the degree of opening and closing of the dampers 16 and 19, the amount of exhaust gas EA sent to the outside air OA side can be adjusted. This is what I did. Furthermore, regeneration sterilization zone 9
The center angle should be approximately 18° to 36°.
使用に当つては脱臭殺菌全熱交換用ローター５
を５〜10r.p.m程度の低速で回転し、外気用ダク
ト１０に外気OAを、還気用ダクト１２に室内空
気RAを夫々送風機（図示せず）によつて図示矢
印の如くローター５の小透孔４に通し、外気OA
と室内空気RAとの間で熱交換を行ない、外気
OAは入気ゾーン７においてローター５のガス吸
収性材料２によりその含有する湿気および有害ガ
スたとえば有機溶剤蒸気、窒素酸化物、オゾン、
硫黄酸化物、一酸化炭素等を吸着除去され清浄な
入気SAとして室内に送り、室内空気RAは排気
ゾーン８においてローター５のガス吸収性材料２
によりその含有する湿気および有害ガスを吸着除
去され清浄な排気EAとして排出されるが、ここ
でダンパー１６およびダンパー１９を適宜開閉し
て清浄な排気EAの一部を入気OAに混合し給気
SAとして再使用するものである。ガス吸収性材
料２が有害ガスで飽和し、ガス吸収能力が低下し
たときは一時外気OAの送入および還気RAの排
出を中止し、熱風送入用ダクト１４より100゜〜
150℃の脱着用空気を15乃至120分程度通し吸着し
たガスおよび湿気を脱着除去するとともに吸着し
た細菌を殺菌する。 When using, deodorize and sterilize total heat exchange rotor 5.
The rotor 5 is rotated at a low speed of about 5 to 10 rpm, and a blower (not shown) is used to supply outside air OA to the outside air duct 10 and indoor air RA to the return air duct 12, as shown by the arrows in the figure. Pass through hole 4 to let outside air OA
Heat exchange is performed between the indoor air RA and the outdoor air RA.
OA is carried out in the inlet zone 7 by the gas-absorbing material 2 of the rotor 5, which absorbs moisture and harmful gases such as organic solvent vapors, nitrogen oxides, ozone, etc.
Sulfur oxides, carbon monoxide, etc. are adsorbed and removed and sent into the room as clean inlet air SA, and the indoor air RA is passed through the gas absorbing material 2 of the rotor 5 in the exhaust zone 8.
The moisture and harmful gases contained therein are adsorbed and removed and the exhaust air is discharged as clean exhaust EA. At this point, the damper 16 and the damper 19 are opened and closed as appropriate to mix a part of the clean exhaust EA with the intake air OA.
It will be reused as SA. When the gas absorbing material 2 becomes saturated with harmful gases and its gas absorption capacity decreases, the supply of outside air OA and the discharge of return air RA are temporarily stopped, and the hot air supply duct 14 is heated to 100°
Desorption air at 150°C is passed through for about 15 to 120 minutes to desorb and remove the adsorbed gas and moisture and sterilize the adsorbed bacteria.
実施例 ２
径が３〜10ミクロン、長さが１〜20mm程度の活
性カーボン繊維を30〜80％、パルプ、合成パルプ
およびまたはガラス繊維を60〜10％、バインダー
を５〜10％の割合で抄紙した活性カーボン繊維混
入紙よりなる平面状シート素材１と塩化リチウ
ム、塩化カルシウムの如き吸湿剤を水溶液の形で
浸漬し乾燥して含浸した紙、布、アスベスト紙、
合成紙の如き通気性材料よりなる波形シート素材
２とを用いて実施例１と同様に脱臭殺菌全熱交換
用ローター５を形成し、以後実施例１の第２図、
第３図と同様に構成してなる脱臭殺菌全熱交換器
である。Example 2 30 to 80% activated carbon fibers with a diameter of 3 to 10 microns and a length of 1 to 20 mm, 60 to 10% of pulp, synthetic pulp and/or glass fiber, and 5 to 10% of a binder. A planar sheet material 1 made of paper mixed with activated carbon fibers, and paper, cloth, asbestos paper, which is impregnated by soaking a moisture absorbent such as lithium chloride or calcium chloride in an aqueous solution and drying it.
A rotor 5 for deodorizing and sterilizing total heat exchange was formed in the same manner as in Example 1 using a corrugated sheet material 2 made of an air-permeable material such as synthetic paper.
This is a deodorizing and sterilizing total heat exchanger constructed in the same manner as shown in FIG.
使用法は実施例１で述べたところと同一であ
り、ガス吸収性材料２が有害ガスで飽和しガス吸
収能力が低下したときは熱風送入用ダクト１４に
80゜〜120℃に加熱した脱着用空気を短時間送入し
てローターに吸着されたガスおよび湿気を脱着除
去する。 The method of use is the same as that described in Example 1, and when the gas absorbent material 2 is saturated with harmful gas and its gas absorption capacity is reduced, the hot air supply duct 14 is
Desorption air heated to 80° to 120°C is introduced for a short period of time to desorb and remove the gas and moisture adsorbed by the rotor.
実施例１および実施例２においてシート素材
１，２の厚みは0.1〜0.5mm、波形シート素材２の
波の波長は３〜５mm、波高は２〜４mm、脱臭殺菌
全熱交換用ローター５の幅は200〜500mm程度、同
ローターの直径は1000〜4000mm程度、活性カーボ
ン繊維混入紙の表面積はローター１m3当り1000〜
2500m2の範囲より選択する。 In Examples 1 and 2, the thickness of the sheet materials 1 and 2 is 0.1 to 0.5 mm, the wave wavelength of the corrugated sheet material 2 is 3 to 5 mm, the wave height is 2 to 4 mm, and the width of the rotor 5 for deodorizing and sterilizing total heat exchange. The diameter of the rotor is about 1000 to 4000 mm, and the surface area of the activated carbon fiber-containing paper is about 1000 to 1000 per m3 of rotor.
Choose from a range of 2500m2 .
この範囲のローター５を使用し有機溶剤蒸気
5ppmを含む外気OAを処理して24時間に１回
120Cの熱風を再生殺菌ゾーン９に30分間通すこ
とにより脱着再生は完全にでき、繰返して熱交換
を行ない得る。 Organic solvent vapor using rotor 5 in this range
Treat outside air OA containing 5ppm once every 24 hours
By passing hot air at 120C through the regeneration sterilization zone 9 for 30 minutes, desorption and regeneration can be completed and heat exchange can be performed repeatedly.
上記条件において外気OAおよび還気RAの送
入速度を１〜5m／secとした場合の全熱交換効率
η（％）を第４図に、有害ガスの吸収除去率（％）
を第５図に示す。 Figure 4 shows the total heat exchange efficiency η (%) when the feeding speed of outside air OA and return air RA is 1 to 5 m/sec under the above conditions, and the absorption and removal rate (%) of harmful gases.
is shown in Figure 5.
本発明は以上の如く顕熱および潜熱の交換を行
なうとともに空気中の種々の有害ガスおよび細菌
を吸着除去してきれいな空気を給気SAとして所
要箇所に送り、また還気RAを脱臭殺菌全熱交換
用ローター５に通し種々の有害ガスおよび細菌を
吸着除去してきれいになつた排気EAの一部をダ
ンパー１６，１９の調節によりバイパス１７を通
し給気SAの一部として再利用するので全熱交換
の効率を挙げ得る効果を有するものである。 As described above, the present invention exchanges sensible heat and latent heat, adsorbs and removes various harmful gases and bacteria in the air, sends clean air to the required locations as supply air SA, and deodorizes and sterilizes return air RA. A part of the clean exhaust EA that has been passed through the replacement rotor 5 to adsorb and remove various harmful gases and bacteria is reused as part of the supply air SA through the bypass 17 by adjusting the dampers 16 and 19, so that all heat is removed. This has the effect of increasing the efficiency of exchange.
図は本発明の実施例を示し、第１図は脱臭殺菌
全熱交換用ローター５をケーシング１８に納めた
状態を示す一部欠截斜視説明図、第２図は第１図
のＡ―Ａ線における軸３に平行な垂直面で切断し
た断面図でダクトを取付けた態様を示し、第３図
は第１図の軸３における垂直断面図でダクトを取
付けた態様を示す。第４図は本発明の全熱交換効
率を示すグラフ、第５図は有害ガスの吸収除去率
を示すグラフである。
尚図中２０はシールである。
The figures show an embodiment of the present invention, FIG. 1 is a partially cutaway perspective explanatory view showing a state in which a rotor 5 for deodorizing and sterilizing total heat exchange is housed in a casing 18, and FIG. 2 is an A-A in FIG. 1. A sectional view taken along a vertical plane parallel to the axis 3 of the line shows the duct installed, and FIG. 3 shows the duct installed in a vertical sectional view taken along the axis 3 of FIG. FIG. 4 is a graph showing the total heat exchange efficiency of the present invention, and FIG. 5 is a graph showing the absorption and removal rate of harmful gases. In addition, 20 in the figure is a seal.
Claims (1)
少なくとも一方をガス吸収性材料で構成し、該平
面状シート素材１と波形シート素材２とを交互に
接着積層して芯材３に巻き重ね、両端面に小透孔
４が透通した円筒状に形成してなる脱臭殺菌全熱
交換用ローター５を駆動回転可能に保持し、パー
ジスポーク６により入気ゾーン７と排気ゾーン８
および再生殺菌ゾーン９に分離し、入気ゾーン７
に外気用ダクト１０と給気用ダクト１１とを連設
し、排気ゾーン８に還気用ダクト１２と排気用ダ
クト１３とを連設し、再生殺菌ゾーン９に熱風送
入用ダクト１４と排気用ダクト１５とを連設して
間歇的に再生殺菌を行ない、外気用ダクト１０と
排気用ダクト１３とをダンパー１６を設けたバイ
パス１７により連結してなることを特徴とする脱
臭殺菌全熱交換器。 ２ 平面状シート素材１と波形シート素材２との
何れか一方をガス吸収性材料で構成し、他方を吸
湿性材料で構成した特許請求の範囲第１項記載の
脱臭殺菌全熱交換器。 ３ ガス吸収性材料が活性カーボン微粒子を付着
した紙である特許請求の範囲第１項または第２項
記載の脱臭殺菌全熱交換器。 ４ ガス吸収性材料が活性カーボン繊維混入紙で
ある特許請求の範囲第１項または第２項記載の脱
臭殺菌全熱交換器。 ５ 吸湿性材料が吸湿剤を含浸した紙、布、不織
布またはアスベスト紙である特許請求の範囲第２
項乃至第４項のいずれか１つに記載の脱臭殺菌全
熱交換器。[Scope of Claims] 1. At least one of the planar sheet material 1 and the corrugated sheet material 2 is made of a gas-absorbing material, and the planar sheet material 1 and the corrugated sheet material 2 are alternately adhesively laminated to form a core. A rotor 5 for deodorizing and sterilizing total heat exchange, which is formed into a cylindrical shape with small through holes 4 through both ends, is held rotatably by the purge spokes 6. zone 8
and regeneration sterilization zone 9, and air intake zone 7.
An outside air duct 10 and a supply air duct 11 are installed in series, a return air duct 12 and an exhaust duct 13 are installed in the exhaust zone 8, and a hot air supply duct 14 and an exhaust air duct are installed in the regeneration sterilization zone 9. The deodorizing and sterilizing total heat exchange system is characterized in that the outside air duct 10 and the exhaust duct 13 are connected by a bypass 17 provided with a damper 16, and the outside air duct 10 and the exhaust duct 13 are connected together to perform regeneration and sterilization intermittently. vessel. 2. The deodorizing and sterilizing total heat exchanger according to claim 1, wherein one of the planar sheet material 1 and the corrugated sheet material 2 is made of a gas-absorbing material, and the other is made of a hygroscopic material. 3. The deodorizing and sterilizing total heat exchanger according to claim 1 or 2, wherein the gas absorbing material is paper to which activated carbon fine particles are attached. 4. The deodorizing and sterilizing total heat exchanger according to claim 1 or 2, wherein the gas absorbing material is paper mixed with activated carbon fibers. 5. Claim 2, in which the hygroscopic material is paper, cloth, nonwoven fabric, or asbestos paper impregnated with a hygroscopic agent.
The deodorizing and sterilizing total heat exchanger according to any one of items 1 to 4.
Priority Applications (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP55164299A JPS5787591A (en) | 1980-11-19 | 1980-11-19 | Overall heat exchanger for deodorization and sterilization |
| KR1019810004203A KR830008296A (en) | 1980-11-17 | 1981-11-03 | Tape cassette |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP55164299A JPS5787591A (en) | 1980-11-19 | 1980-11-19 | Overall heat exchanger for deodorization and sterilization |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5787591A JPS5787591A (en) | 1982-06-01 |
| JPS6335918B2 true JPS6335918B2 (en) | 1988-07-18 |
Family
ID=15790472
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP55164299A Granted JPS5787591A (en) | 1980-11-17 | 1980-11-19 | Overall heat exchanger for deodorization and sterilization |
Country Status (2)
| Country | Link |
|---|---|
| JP (1) | JPS5787591A (en) |
| KR (1) | KR830008296A (en) |
Families Citing this family (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US7150314B2 (en) * | 2001-09-17 | 2006-12-19 | American Standard International Inc. | Dual exhaust energy recovery system |
| JP2010048461A (en) * | 2008-08-21 | 2010-03-04 | Seibu Giken Co Ltd | Total enthalpy heat exchanger |
| JP5680456B2 (en) * | 2011-03-22 | 2015-03-04 | 株式会社西部技研 | Dehumidifying air conditioner |
-
1980
- 1980-11-19 JP JP55164299A patent/JPS5787591A/en active Granted
-
1981
- 1981-11-03 KR KR1019810004203A patent/KR830008296A/en not_active Withdrawn
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5787591A (en) | 1982-06-01 |
| KR830008296A (en) | 1983-11-18 |
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