JPH01291027A - Water-washing type air-cleaning and sterilizing device - Google Patents
Water-washing type air-cleaning and sterilizing deviceInfo
- Publication number
- JPH01291027A JPH01291027A JP63120350A JP12035088A JPH01291027A JP H01291027 A JPH01291027 A JP H01291027A JP 63120350 A JP63120350 A JP 63120350A JP 12035088 A JP12035088 A JP 12035088A JP H01291027 A JPH01291027 A JP H01291027A
- Authority
- JP
- Japan
- Prior art keywords
- water
- air
- ozone
- washing tower
- receiving tank
- 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.)
- Pending
Links
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A50/00—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE in human health protection, e.g. against extreme weather
- Y02A50/20—Air quality improvement or preservation, e.g. vehicle emission control or emission reduction by using catalytic converters
Landscapes
- Central Air Conditioning (AREA)
- Separation Of Particles Using Liquids (AREA)
Abstract
(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.
Description
【発明の詳細な説明】 〔産業上の利用分野〕 本発明はバイオクリーンルームを対象に、塵埃。[Detailed description of the invention] [Industrial application field] The present invention is aimed at bio-clean rooms to reduce dust.
菌を介む室内空気を水洗塔との間で循環送風することに
より除塵、除菌して室内空気を清浄化するようにした水
洗浄式空気清浄、除菌装置に関する。The present invention relates to a water washing type air purifying and sterilizing device that cleans indoor air by removing dust and bacteria by circulating indoor air containing bacteria between a washing tower and a water washing tower.
食品製造、医薬品製造、医療分野で使用されるバイオク
リーンルームは、室内環境の無菌化、バイオハザード等
の必要性から除塵の他に、浮遊微生物等に対する除曹機
能が要求され、かかる空気の清浄5除田装置として、水
洗塔を採用してその洗浄捕集作用により処理空気中の浮
遊塵埃、R等を除塵、除菌するとともに、さらに捕集し
た閑をオゾンで滅菌するようにした水洗浄式空気清浄。Bio-clean rooms used in food manufacturing, pharmaceutical manufacturing, and medical fields are required to not only remove dust but also remove carbon dioxide from airborne microorganisms due to the need to sterilize the indoor environment and prevent biohazards. A water-washing type that uses a water-washing tower as a paddy removal device to remove and sterilize floating dust, R, etc. from the treated air through its washing and collection action, and further sterilizes the collected waste with ozone. Air purification.
除菌装置が特開昭62−69033等で既に提案されて
いる。A sterilization device has already been proposed in Japanese Patent Application Laid-Open No. 62-69033.
次に第2図により頭記した水洗浄式空気清浄。Next is the water cleaning type air purifier as shown in Figure 2.
除r11装置の従来システムを説明する0図において、
lはバイオクリーンルーム、2はブロア、3は水洗塔で
あり、バイオクリーンルーム1の空気取出口11と給気
口12との間には前記ブロア2.水洗塔3を経由する空
′Xv&環送風路4が形成されている。In Figure 0 explaining the conventional system of the removal r11 device,
1 is a bio-clean room, 2 is a blower, and 3 is a water washing tower. An air 'Xv&circular air passage 4 passing through the water washing tower 3 is formed.
一方、水洗塔3はその底部に受水[31を、また塔内通
風路の上部にはに除滴用のエリミネータ32゜および散
水ノズル33を備え、ポンプ34を介して受水槽31の
貯留水を散水ノズル33へ供給して塔内通ffi路へシ
ャワー撒布するように構成されている。On the other hand, the water washing tower 3 is equipped with a water receiving tank 31 at its bottom, and an eliminator 32 for removing drips and a water spray nozzle 33 at the upper part of the ventilation passage in the tower. It is configured to supply water to the water spray nozzle 33 and spray it onto the in-column ffi passage.
さらに受水槽31には人中に浸漬して外部のオゾナイザ
5に接続したオゾン散気管51がi!lll!備されて
いる。な1B35は水抜用のFレンコックである。Furthermore, an ozone diffuser pipe 51 immersed in the water tank 31 and connected to an external ozonizer 5 is connected to the i! llll! Equipped with 1B35 is an F-lencock for draining water.
かかる構成でバイオクリーンルーム1の空気を除塵、除
田処理するには、まず水洗塔3において受水槽31の貯
留水中にオゾナイザ5で生成したオゾンをオゾン散気管
51より散気させてオゾンを水中に溶解、@収させつつ
、受水槽31の水を散水ノズル33より塔内通風路中に
撒布し、この状態でブロア2の運転によりバイオクリー
ンルーム1から吸引した塵埃、菌を含む処1空気を水洗
塔3の側面に開口するダクトを通じて塔内へ押し込み送
風する。In order to remove dust and dirt from the air in the bio-clean room 1 with this configuration, first, the ozone generated by the ozonizer 5 is diffused into the water stored in the water receiving tank 31 in the water washing tower 3 through the ozone diffuser pipe 51 to diffuse ozone into the water. While dissolving and collecting water, the water in the water tank 31 is sprayed into the ventilation passage in the tower from the water spray nozzle 33, and in this state, the blower 2 is operated to wash the air containing dust and bacteria sucked from the bio-clean room 1 with water. Air is forced into the tower through a duct that opens on the side of the tower 3.
これにより処理空気流Aが水洗塔3の塔内通風路を上昇
通風する過程で向流式に水ノズル33より噴出する水シ
ヤワーBの撒布を受け、処理空気中に浮遊している塵埃
、および塵埃に付着している菌等が水シヤワーによる洗
浄集塵作用で水滴に取り込まれて分離捕集され、処理空
気流Aの除塵。As a result, the treated air flow A is sprayed by the water shower B ejected from the water nozzle 33 in a countercurrent manner in the process of ascending through the ventilation passage in the washing tower 3, and the dust floating in the treated air is removed. Bacteria adhering to the dust are taken into water droplets and separated and collected by the cleaning and dust collection action of the water shower, and the treated air stream A is cleaned of dust.
Il#菌が行われる。また水洗塔3で清浄化された空気
はエリミネータ32で水滴を除滴した上で、バイオクリ
ーンルーム1の給気口12を通じて室内に還流、放出さ
れる。一方、塵埃、菌を捕集したシャワー水は塔内を自
重により沈降して受水槽31へ回収された後に、再びポ
ンプ34を経て散水ノズル33に供給されるように反復
使用される。しかも受水槽31の水中にはオゾナイザ5
からオゾン散気管51を通じて供給されたオゾンCが溶
解、吸収されており、・水シヤワーで捕集された菌はオ
ゾン吸収水と接触反応して速やかに滅菌処理される。Il# bacteria are performed. Further, the air purified in the water washing tower 3 has water droplets removed by an eliminator 32, and then is returned and discharged into the room through the air supply port 12 of the bioclean room 1. On the other hand, the shower water that has collected dust and bacteria settles in the tower due to its own weight and is collected in the water receiving tank 31, after which it is repeatedly used so as to be supplied to the water nozzle 33 via the pump 34 again. Moreover, there is an ozonizer 5 in the water in the water tank 31.
Ozone C supplied through the ozone diffuser pipe 51 is dissolved and absorbed, and the bacteria collected by the water shower are rapidly sterilized by contact reaction with the ozone-absorbed water.
ところで上記した従来装置のままでは年間を通じて稼働
する場合に、除重効果の面で次記のような問題点がある
。By the way, if the above-mentioned conventional device is operated throughout the year, the following problems arise in terms of the weight removal effect.
すなわち、水洗塔3の受水槽31に貯留されている水温
は周囲温度の影響を大きく受け、冬期は低温であるが夏
期には高温になる等、その水温が年間を通じて大きく変
動する。That is, the temperature of the water stored in the water receiving tank 31 of the water washing tower 3 is greatly affected by the ambient temperature, and varies greatly throughout the year, such as being low in winter and high in summer.
一方、水中にオゾンを散気して溶解吸収させる場合に、
その供給オゾン量と水中の溶存オゾン量との割合を表す
分配係数と水温との関係は第3図の特性図のごとくであ
り、分配係数は水温が低い程高くなる傾向を示す、つま
り水中に同じオゾン量を供給した場合でも、水温が高い
とオゾン吸収率が低く、逆に水温が低いとオゾン吸収率
が高する。また水中に溶解したオゾンは水温が高いほど
その自己分解速度が早まり、短時間でオゾンが酸素に変
わることも知られている。On the other hand, when ozone is diffused into water and dissolved and absorbed,
The relationship between the distribution coefficient, which represents the ratio between the amount of supplied ozone and the amount of dissolved ozone in water, and water temperature is as shown in the characteristic diagram in Figure 3.The distribution coefficient tends to increase as the water temperature decreases. Even when the same amount of ozone is supplied, the higher the water temperature, the lower the ozone absorption rate, and conversely, the lower the water temperature, the higher the ozone absorption rate. It is also known that the higher the water temperature, the faster the rate of self-decomposition of ozone dissolved in water, converting ozone into oxygen in a short time.
したがって第2図の従来装置では、受水槽31ヘオゾナ
イザ5より同じ量のオゾンを供給するものとして、周囲
温度によって受水槽内の貯留水に対するオゾンの分配係
数9分解速度、つまり貯留水のオゾン濃度が変動する。Therefore, in the conventional device shown in FIG. 2, assuming that the same amount of ozone is supplied from the water receiving tank 31 and the ozonizer 5, the ozone partition coefficient 9 decomposition rate with respect to the water stored in the water receiving tank, that is, the ozone concentration of the stored water, changes depending on the ambient temperature. fluctuate.
しかも水シヤワーで空気中より捕集した菌を受水槽31
の水中で滅菌させる能力はオゾン水のオゾン濃度に依存
することから、特に夏期のように水温が上昇した状態で
はオゾンの自己分解速度が早まることと併せてオゾン水
による滅菌能力が低下し、この結果として受水槽内で菌
が増殖するようになる。また生存菌を多く含む水が散水
ノズル33を通じて循環空気流中に撒布されると、水シ
ヤワーで洗浄捕集し切れずに閾が再飛散して空気流と一
緒にバイオクリーンルーム1の室内へ侵入する割合が多
くなり、結果的に水洗浄式空気清浄、除wigの除菌率
が低下する。Moreover, the water tank 31 collects bacteria collected from the air using a water shower.
The ability to sterilize in water depends on the ozone concentration of ozonated water, so when the water temperature rises, especially in the summer, the self-decomposition rate of ozone accelerates, and the sterilizing ability of ozonated water decreases. As a result, bacteria begin to proliferate within the water tank. Furthermore, when water containing many viable bacteria is sprayed into the circulating air stream through the water spray nozzle 33, the water shower cannot wash and collect it, and the threshold is re-splattered and enters the bio-clean room 1 along with the air stream. As a result, the sterilization rate of water-based air purifiers and wig removers decreases.
本発明は上記の点にかんがみ成されたものであり、年間
を通じて水洗浄式空気清浄、 Wkw装置を稼働する場
合でも、周囲温度の影響を受けることなく常に安定して
高い除菌効率が維持できるようし、しかもバイオクリー
ンルームの室内空気を水洗塔との間で循環送風する際に
室内へ還流する空気の温度をバイオクリーンルーム側で
要求される空気温に合わせて適温にm節できるようにし
た水洗浄式空気清浄、除菌装置を提供することを目的と
する。The present invention has been developed in consideration of the above points, and even when operating a water cleaning type air purifier or WkW device throughout the year, it is possible to always maintain stable and high sterilization efficiency without being affected by the ambient temperature. Moreover, when the indoor air in the bio-clean room is circulated between the water washing tower and the water washing tower, the temperature of the air that is returned to the room can be adjusted to an appropriate temperature according to the air temperature required by the bio-clean room. The purpose is to provide cleaning air purification and sterilization equipment.
上記課題を解決するために、本発明の装置においては、
水洗塔の受水槽の貯留水を常時低温に維持する冷却手段
と、水洗塔の下流側でバイオクリーンルームとの間の循
環通風路に介装した空気温!Il!lff用の空気加熱
手段とを備えて構成するものとする。In order to solve the above problems, in the device of the present invention,
Cooling means that keeps the water stored in the water receiving tank of the washing tower at a constant low temperature and the air temperature installed in the circulation ventilation path between the downstream side of the washing tower and the bio-clean room! Il! It shall be constructed by including an air heating means for lff.
上記構成で、冷却手段として水洗塔の受水槽にチリング
ユニットを接続し、また空気加熱手段として水洗塔の出
口側の循環通風ダクト内には空気温!1m用ヒータが配
備されおり、ここでチリングユニットは受水槽の貯留水
温度を年間を通じて9〜11 ”C程度に維持するよう
運転制御する。また空気温11u用ヒータも同様にバイ
オクリーンルーム側で要求される温度基準に水洗塔から
バイオクリーンルームに還流する空気の温度を適温に維
持するように通電制御される。With the above configuration, a chilling unit is connected to the water receiving tank of the washing tower as a cooling means, and the air temperature inside the circulation ventilation duct on the outlet side of the washing tower is used as an air heating means. A 1m heater is installed, and the chilling unit controls operation to maintain the temperature of the stored water in the water tank at around 9 to 11"C throughout the year. A 11u air temperature heater is also required by the bioclean room. Electricity is controlled to maintain the temperature of the air flowing back from the water washing tower to the bio-clean room at an appropriate temperature based on the temperature standard.
これにより周囲温の変動に影響を受けることなく、受水
槽内の貯留水温度を常に低温に保持して貯留水中へのオ
ゾン吸収効率、つまり除薗率が年間を通じて高安定に維
持されるようになるとともに、併せて水シヤワーの撒布
を受けて温度が低下した循環空気を所定温度まで戻した
上でバイオクリーンルームに還流させることができる〔
実施例〕
第1図は本発明の実施例のシステム図を示すものであり
、第2図に対応する同一部分には同じ符号が付しである
。まず図示実施例では、水洗塔3に並置して独立したオ
ゾン溶解槽6が設置してあり、該オゾン溶解槽6と水洗
塔3の受水p131との間がポンプ61を含むWIN送
水路62を介して連通接続されており、かつオゾン溶解
槽6の底部にはオゾナイザ5に接続したオゾン散気管5
1が配備しである。なお63はオゾン溶解槽6の頂部に
接続した徘オゾン処理器である。ここでオゾン溶解槽6
と水洗塔3の受水槽31との間で水を循環送水させつつ
、オゾン溶解槽6の水中へオゾナイザ5で生成したオゾ
ンをオゾン散気管51を通じて散気することにより水中
にオゾンが溶解吸収され、かつオゾン吸収水が水洗塔3
の受水槽31との間で循環送水される過程で処理空気流
中より分離捕集した薗を滅田する。This ensures that the temperature of the water stored in the water tank is always maintained at a low temperature without being affected by fluctuations in ambient temperature, and that the ozone absorption efficiency, or removal rate, of ozone into the water is maintained at a high level throughout the year. At the same time, the circulating air whose temperature has decreased due to water showering can be returned to a predetermined temperature and then returned to the bioclean room.
Embodiment] FIG. 1 shows a system diagram of an embodiment of the present invention, and the same parts corresponding to FIG. 2 are given the same reference numerals. First, in the illustrated embodiment, an independent ozone dissolution tank 6 is installed in parallel with the water washing tower 3, and a WIN water supply channel 62 including a pump 61 is connected between the ozone dissolution tank 6 and the water receiving p131 of the water washing tower 3. and an ozone diffuser pipe 5 connected to the ozonizer 5 at the bottom of the ozone dissolving tank 6.
1 is deployed. Note that 63 is a wandering ozone treatment device connected to the top of the ozone dissolution tank 6. Here, ozone dissolution tank 6
The ozone generated by the ozonizer 5 is diffused into the water of the ozone dissolving tank 6 through the ozone diffuser pipe 51 while circulating water between the water receiving tank 31 of the washing tower 3 and the ozone is dissolved and absorbed in the water. , and the ozone-absorbed water is in the washing tower 3.
During the process of circulating water between the water receiving tank 31 and the water receiving tank 31, the soybeans separated and collected from the treated air stream are destroyed.
かかる構成で、本発明により水洗塔3の受水槽3!に対
し、貯留水の冷却手段として符号7で示すチリングユニ
ットが送水ポンプ71を含む8M送水配管72を介して
配管接続されている。さらに水洗塔3の下流側でバイオ
クリーンルーム1との間の空気循環通風ダクト内には符
号8で示す空気温調節用の加熱し−タが介装配備されて
いる。With such a configuration, the water receiving tank 3 of the water washing tower 3 according to the present invention! On the other hand, a chilling unit designated by reference numeral 7 is connected as a cooling means for the stored water via an 8M water pipe 72 including a water pump 71. Furthermore, in the air circulation ventilation duct between the washing tower 3 and the bioclean room 1 on the downstream side, a heating heater 8 for controlling the air temperature is interposed.
ここでチリングユニット7は、第3図の特性図で表した
オゾンの水に対する分配係数をll5t草に保持するた
めに、受水槽31の貯留水の水温を9〜11℃を維持す
るように運転制御され、またヒータ8は水洗塔3を経て
バイオクリーンルーL1に還流する空気の室内への吹出
温度設定値を例えば12±3℃として、該空気温度が1
0″C以下でメン、11℃以上でオフとなるように通’
t@mされる。Here, the chilling unit 7 is operated to maintain the temperature of the water stored in the water receiving tank 31 at 9 to 11 degrees Celsius in order to maintain the distribution coefficient of ozone to water as shown in the characteristic diagram of FIG. The heater 8 is controlled so that the air temperature is set to 12±3°C, for example, and the air temperature set at 12±3°C is set for the air flowing back into the bioclean room L1 through the water washing tower 3.
It is set so that it turns on when it is below 0"C and turns off when it is above 11℃.
t@m is done.
なお、図示実施例では水洗塔3にオゾン溶解槽を付設し
てここにオゾンを散気し、ここで生成したオゾン水を水
洗塔3の受水槽31へ送水するようにした例を示したが
、第2図のように水洗塔3の受水槽31の水中に直接オ
ゾンを散気するようにした装置に対しても同様に実施で
きるのは勿論のこと、チリングユニットを第1図におけ
るオゾン溶解槽6に接続して実施することも可能である
。In the illustrated embodiment, an ozone dissolving tank is attached to the water washing tower 3, ozone is diffused there, and the ozonated water generated here is sent to the water receiving tank 31 of the washing tower 3. , it goes without saying that the chilling unit can be similarly applied to a device that diffuses ozone directly into the water in the water receiving tank 31 of the water washing tower 3 as shown in FIG. It is also possible to carry out the process by connecting to the tank 6.
本発明の水洗浄式空気清浄、除菌装置は、以上説明した
ように構成されているので、次記の効果を奏する。The water cleaning type air purifying and sterilizing device of the present invention is configured as described above, and therefore has the following effects.
すなわち、水洗塔の受水槽の貯留水を常時低温に維持す
る冷却手段と、水洗塔の下流側でバイオクリーンルーム
との間の循環通風路に介装した空気温調節用の空気加熱
手段とを備えたことにより、1′!l囲温序のト響を受
けることなく、年間を通じて受水槽の貯留水に対するオ
ゾン吸収率を高く維持して効果的な除菌処理を行うこと
ができるとともに、併せて水洗塔を経てバイオクリーン
ルームにXi流する空気温を室内側で要求される適温に
温度調節できるなど、バイオクリーンルームを対象とし
た室内空気の清浄、無菌化に優れた効果を発揮する水洗
浄式空気清浄、除vIi装置が得られる。In other words, it is equipped with a cooling means that constantly maintains the water stored in the water receiving tank of the washing tower at a low temperature, and an air heating means for controlling the air temperature, which is installed in the circulation ventilation path between the washing tower and the bio-clean room on the downstream side. As a result, 1′! l It is possible to maintain a high ozone absorption rate in the water stored in the water tank throughout the year without being affected by the effects of circadian temperature, and to perform effective sterilization treatment. The water cleaning air purifier and vIi device is highly effective in purifying and sterilizing indoor air for bio-clean rooms, such as by being able to adjust the temperature of the air flowing through the Xi to the appropriate temperature required indoors. It will be done.
第1図、第2図はそれぞれ本発明実施例、および従来の
水洗浄式寮気清浄、除l1vl置のシステム図、第31
!Iはオゾンの水温と分配係数との関係を表した特性図
である。各図において、
l:バイオクリーンルーム、2ニブロア、3:水洗塔、
31:受水槽、33:散水ノズル、42室内空気の循環
送風路、5:オゾナイザ、51ニオシン散気管、7:チ
リングユニット、8:空気温調節第2!!lFigures 1 and 2 are system diagrams of an embodiment of the present invention and a conventional water-washing dormitory air purifier/exhaust system, respectively.
! I is a characteristic diagram showing the relationship between ozone water temperature and distribution coefficient. In each figure, l: bio clean room, 2 niblore, 3: water washing tower,
31: Water tank, 33: Water nozzle, 42 Indoor air circulation channel, 5: Ozonizer, 51 Niosin diffuser pipe, 7: Chilling unit, 8: Air temperature control 2nd! ! l
Claims (1)
水洗浄して除塵、除菌する水洗浄式空気清浄、除菌装置
であり、塔内の上部に散水ノズル、底部に受水槽を有す
る水洗塔と、前記受水槽の貯留水へ外部からオゾンを散
気して溶解吸収させるオゾン供給手段とを備え、前記受
水槽の貯留水にオゾンを溶解吸収させ、かつこのオゾン
水を散水ノズルを通じて塔内通風路に撒布させた状態で
、バイオクリーンルームと水洗塔との間で室内空気を循
環送風して空気の除塵、除菌を行うようにした水洗浄式
空気清浄、除菌装置において、水洗塔の受水槽の貯留水
を常時低温に維持する冷却手段と、水洗塔の下流側でバ
イオクリーンルームとの間の循環通風路に介装した空気
温調節用の空気加熱手段とを備えたことを特徴とする水
洗浄式空気清浄、除菌装置。1) A water washing type air purifier and sterilization device that cleans indoor air with water to remove dust and bacteria, targeting bio-clean rooms, etc. A water washing tower has a water nozzle at the top of the tower and a water receiving tank at the bottom. and ozone supply means for dissolving and absorbing ozone from the outside into the water stored in the water receiving tank, and dissolving and absorbing ozone in the water stored in the water receiving tank, and supplying this ozonated water into the tower through a watering nozzle. In a water washing type air purifying and sterilizing device that circulates and blows indoor air between the bio-clean room and the washing tower while spraying it in the ventilation duct to remove dust and sterilize the air. It is characterized by being equipped with a cooling means for constantly maintaining the water stored in the water receiving tank at a low temperature, and an air heating means for controlling the air temperature, which is installed in the circulation ventilation path between the water washing tower and the bioclean room on the downstream side. A water-cleaning air purifying and sterilizing device.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP63120350A JPH01291027A (en) | 1988-05-17 | 1988-05-17 | Water-washing type air-cleaning and sterilizing device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP63120350A JPH01291027A (en) | 1988-05-17 | 1988-05-17 | Water-washing type air-cleaning and sterilizing device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH01291027A true JPH01291027A (en) | 1989-11-22 |
Family
ID=14784054
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP63120350A Pending JPH01291027A (en) | 1988-05-17 | 1988-05-17 | Water-washing type air-cleaning and sterilizing device |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH01291027A (en) |
Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH0438174U (en) * | 1990-07-27 | 1992-03-31 |
-
1988
- 1988-05-17 JP JP63120350A patent/JPH01291027A/en active Pending
Patent Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH0438174U (en) * | 1990-07-27 | 1992-03-31 |
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