JPS6269032A - Dust and germ removing device for gas - Google Patents

Dust and germ removing device for gas

Info

Publication number
JPS6269032A
JPS6269032A JP60207583A JP20758385A JPS6269032A JP S6269032 A JPS6269032 A JP S6269032A JP 60207583 A JP60207583 A JP 60207583A JP 20758385 A JP20758385 A JP 20758385A JP S6269032 A JPS6269032 A JP S6269032A
Authority
JP
Japan
Prior art keywords
tower
water
spray
water droplets
dust
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.)
Granted
Application number
JP60207583A
Other languages
Japanese (ja)
Other versions
JPH0325701B2 (en
Inventor
Kiyokatsu Ueda
上田 清勝
Akira Ishikawa
彰 石川
Takeo Takahashi
高橋 武男
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Fuji Electric Co Ltd
Original Assignee
Fuji Electric Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Fuji Electric Co Ltd filed Critical Fuji Electric Co Ltd
Priority to JP60207583A priority Critical patent/JPS6269032A/en
Publication of JPS6269032A publication Critical patent/JPS6269032A/en
Publication of JPH0325701B2 publication Critical patent/JPH0325701B2/ja
Granted legal-status Critical Current

Links

Abstract

PURPOSE:To miniaturize the title device and increase dust removing efficiency as well as germs removing efficiency by a method wherein fine water drip particles are sprayed from lower stage spray nozzles and rough water drip particles are sprayed from upper side spray nozzles while air is sent upwardly into a tower to contact it with the water drip particles through convection. CONSTITUTION:Water spraying spray nozzles are arranged in a water washing tower 5 by dividing them into the spray nozzle groups 7a, 7b in upper and lower stages. The spray nozzle group 6b in the lower stage is provided with spray nozzles having small diameter to spray the shower of fine water drip particles of approx. 200mum while the spray nozzle group 7a in the upper stage is designed so as to generate the shower of rough water drip particles of approx. 500mum. The rough water drip particles shower of fine water drip particles is sprayed against the same air in the lower part of the tower. The contaminated air flow, containing dust and germs, is introduced into the water washing tower 5 from the lower part thereof through a fan 3 and a filter 4, then, ascends in the tower as shown by an arrow A and contacts with the showers of water drip particles by convection during ascending.

Description

【発明の詳細な説明】[Detailed description of the invention] 【発明の属する技術分野】[Technical field to which the invention pertains]

この発明は食品加工室1食品保管室、病院における手術
室、病室、その他の無菌作業所等を対象に室内空気の除
塵、除菌を行って清浄化するようにした気体の除塵・除
@装置に関する。
This invention is a gas dust removal/removal @ device that cleans indoor air by removing dust and sterilization for food processing rooms, food storage rooms, operating rooms in hospitals, hospital rooms, and other sterile workplaces. Regarding.

【従来技術とその問題点】[Prior art and its problems]

まず第2図により頭記した気体の除塵・除菌装置の従来
における一般的なシステムを説明する。 図において、1は空気清浄化の対象となる食品加工室等
の室であり、謹呈1の空気取出口と給気口との間に空気
循環送風路2を構成し、ここに送風機3.粗大な塵埃を
除去するプレフィルタ4.水洗塔5.および空!!!装
置6が順に介装設置され、これらで除塵・除菌装置のシ
ステムを構成している。ここで前記の水洗塔5は塔内に
微少水滴を噴霧するスプレーノズル7、送水ポンプ8.
水濾過器9等の間を結んで成る水噴霧系を装備した噴霧
式洗浄集塵器として構成されている。 かかる構成で送風機3により室1より引き出された塵埃
、菌を含む室内の汚染空気は、まずプレフィルタ4で粗
大な塵埃を取り除いた後に水洗塔5の塔内下部へ導入さ
れる。ここで汚染空気は塔内を矢印Aのように上昇する
過程でスプレーノズル7から噴霧して塔内空間に充満す
る微細な水滴粒子Bと接触し、空気中に含まれている微
粒子塵埃および塵埃に付着ている薗等は洗浄集塵作用に
より水滴へ移行して空気流から分離補集され、塔内を沈
降して底部に溜る。一方、除塵、除菌して清浄化された
空気流は塔上部から排出され、さらに空調装置6で温度
、湿度を調整した後に再び室1内に送気還流される。一
方、水洗塔5内の底部に溜った水は活性炭、イオン交換
樹脂等の吸着物質を内蔵した濾過器9で濾過した後に、
送水ポンプ8を経て再びスプレーノズル7から塔内に噴
霧されるようにW1環して反復使用される。なお10は
定期的に塔内の洗浄水を交換する際に洗浄廃水を系外に
排水するドレン弁である。 ところで上記した除塵・除菌装置における水洗塔5での
除塵、除菌効率を上げるには、塔内を下方から上方へ向
けて通流する空気流人とスプレーノズル7から塔内に分
散噴霧する水滴粒子Bとの接触割合および衝突の相対速
度を高めて塵埃、閑の補集率を高める必要がある。した
がってこのためにはスプレーノズル7の噴霧口を小さく
、かつ噴射速度を高めて微細な水滴粒子を数多く発生(
7、これにより同じ水量での水滴表面積を増大させて空
気流との接触割合の増加を図る方法が一般に採られてい
る。 一方、スプレーノズルから噴霧する水滴粒子径が微細に
なる程塔内を上昇する空気流の影響を受は易くなり、水
滴粒子は塵埃、菌を取り込んだまま塔内を上昇する空気
流に運ばれて水洗塔5から外方へ逸出する割合が多くな
り、このままでは除塵、除菌効率が低下する。したがっ
てこのような水滴粒子の塔外逸出を避けるためには塔内
を流れる空気流の風速を下げる必要があるが、このため
に同じ空気量を処理するのに水洗塔5が径大となり設備
が大形化する問題が派生する。
First, a conventional general system of the gaseous dust removal and sterilization device described above with reference to FIG. 2 will be explained. In the figure, reference numeral 1 denotes a room such as a food processing room where air purification is to be performed, and an air circulation passage 2 is constructed between the air intake port and the air supply port of the enclosure 1, and a blower 3. Pre-filter to remove coarse dust 4. Washing tower 5. and sky! ! ! Devices 6 are installed in order, and these devices constitute a system of dust removal and sterilization devices. Here, the water washing tower 5 includes a spray nozzle 7 that sprays minute water droplets into the tower, a water pump 8.
It is constructed as a spray type cleaning dust collector equipped with a water spray system that connects water filters 9 and the like. With this configuration, the indoor contaminated air containing dust and bacteria drawn out from the room 1 by the blower 3 is introduced into the lower part of the washing tower 5 after first removing coarse dust with the pre-filter 4. Here, while the contaminated air rises inside the tower as shown by arrow A, it comes into contact with fine water droplets B that are sprayed from the spray nozzle 7 and fills the space inside the tower, and the particulate dust and dirt contained in the air are removed. The water particles adhering to the tower are converted into water droplets by the washing and dust collection action, separated and collected from the air stream, and settle in the tower and accumulate at the bottom. On the other hand, the air stream that has been purified by dust removal and sterilization is discharged from the upper part of the tower, and after the temperature and humidity are adjusted by the air conditioner 6, it is sent back into the room 1 again. On the other hand, the water accumulated at the bottom of the water washing tower 5 is filtered through a filter 9 containing adsorbent substances such as activated carbon and ion exchange resin.
W1 is used repeatedly so that it is sprayed into the tower from the spray nozzle 7 via the water pump 8. Note that 10 is a drain valve that drains washing waste water out of the system when washing water in the tower is periodically replaced. By the way, in order to increase the dust removal and sterilization efficiency in the water washing tower 5 in the above-mentioned dust removal and sterilization equipment, the air streamer flowing from the bottom to the top of the tower and the spray nozzle 7 disperse the spray into the tower. It is necessary to increase the rate of contact with the water droplet particles B and the relative speed of collision to increase the collection rate of dust and dirt. Therefore, in order to achieve this, the spray nozzle 7 should be made smaller and the spray speed should be increased to generate many fine water droplets (
7. Thereby, a method is generally adopted in which the surface area of water droplets is increased with the same amount of water, thereby increasing the contact ratio with the air flow. On the other hand, the finer the diameter of the water droplets sprayed from the spray nozzle, the more they are affected by the airflow rising inside the tower, and the water droplets are carried by the airflow rising inside the tower while taking in dust and bacteria. The proportion of the particles escaping outward from the water washing tower 5 increases, and if this continues, the efficiency of dust removal and sterilization will decrease. Therefore, in order to avoid such water droplets escaping outside the tower, it is necessary to reduce the speed of the air flowing inside the tower, but for this reason, the diameter of the water washing tower 5 has to be increased to process the same amount of air. A problem arises in which the size of the vehicle becomes larger.

【発明の目的] この発明は上記の点にかんがみなされたものであり、前記した従来装置の欠点を除去して小型な構成でかつ除塵、除菌効率の高い除享・除菌装置、特にその水噴霧式水洗塔を提供することを目的とする。 【発明の要点】[Purpose of the invention] The present invention has been made in view of the above points, and provides a cleaning and sterilization device that eliminates the drawbacks of the conventional devices described above and has a compact configuration and has high dust removal and sterilization efficiency, especially its water spray type water washing tower. The purpose is to provide [Key points of the invention]

上記目的を達成するために、この発明は水洗塔内に上下
複数段に分けて水滴粒子を塔内に噴霧するスプレーノズ
ルを配備し、かつ下段側のスプレーノズルからは微細水
滴粒子を、上段側のスプレーノズルからは粗大水滴粒子
を噴霧し、塔内に導入した気体流を下方から上方へ上昇
送風して前記水滴粒子と対流接触させるように構成し、
水洗塔内の下部領域では微細な水滴粒子と塔内に導入さ
れた汚染気体流との接触を充分に行わせて水滴粒子によ
る汚染気体流中の塵埃粒子、菌の補集効率を高め、かつ
塔内の上部領域では下方から」−昇i1流する気体流と
一諸に浮上してくる微細水滴粒子を粗大な水滴粒子によ
り捕捉して下方へ重力沈降させ、これにより高い除塵、
除菌効率が得られるようにしたものである。
In order to achieve the above object, the present invention provides a water washing tower with spray nozzles that spray water droplets into the tower in multiple stages, upper and lower, and the spray nozzles on the lower stage spray fine water droplets onto the upper stage. The spray nozzle sprays coarse water droplets, and the gas flow introduced into the tower is blown upward from below to bring it into convection contact with the water droplets,
In the lower region of the water washing tower, sufficient contact is made between fine water droplets and the contaminated gas flow introduced into the tower, thereby increasing the efficiency of collecting dust particles and bacteria in the contaminated gas flow by the water droplets. In the upper region of the tower, the fine water droplets that rise together with the rising gas stream are captured by coarse water droplets and allowed to settle downward by gravity, resulting in high dust removal,
It is designed to provide sterilization efficiency.

【発明の実施例】[Embodiments of the invention]

第1図はこの発明の実施例を示すものであり、第2図に
対応する同一部材には同じ符号が付しである。すなわち
この発明により、水洗塔5の内部に配備した水噴霧用の
スプレーノズルが上下複数段のスプレーノズル群7aと
7bとに分けて配備されており、ここで下段側のスプレ
ーノズル群7bは噴霧口を小径にして200μ麟前後の
微細水滴粒子シャワーを噴霧するようなノズルであるの
に対し、上段側のスプレーノズル群7aは500μ国前
後の粗大水滴粒子シャワーを発生するように設定された
ノズルとして成る。なお11は各段のスプレーノズル群
への分岐配管に介挿された流量制御弁、12は塔内へ洗
浄水を補給する上水道の配管、13は同配管に介挿した
水位調節弁、14は水洗塔5内の上部に装備した水滴除
去用のエリミネータ、15は水洗塔5の後段に接続され
た水滴除去用の除滴サイクロン、16はドレン排水管路
に介挿した濾過器である。 次に上記構成の動作に付いて説明する。運転時には送水
ポンプ8で圧送された水が流量制御弁11を通じて上下
各段のスプレーノズル群7a、 7bへ供給され、塔内
の下部領域には微細水滴粒子のシャワーP、bが、−ヒ
部領域には粗大水滴粒子のシャワーBaが分散噴霧され
る。一方、図示されてない室から抽気された塵埃、Wi
を含む汚染空気流は送風機3、プレフィルタ4を通じて
水洗塔5の塔内へ下方から導入され矢印Aのように塔内
を上昇して流れ、この上昇過程で前記した水滴シャワー
と対流接触する。この場合にまず空気流はスプレーノズ
ル群7bより噴霧して塔内の下部領域に充満している微
細な水滴粒子と効率よく接触し、空気流に含まれている
塵埃、閑等が水滴粒子に移行して補集される。同時にこ
の領域のF方には上段側のスプレーノズル7aから粗大
な水滴粒子のシャワーが噴霧されており、空気流ととも
に塔内を上昇浮上してくる塵埃、菌を採り込んだ微細水
滴粒子は粗大な水滴粒子に捕捉され、空気流人に逆らっ
て下方へ重力沈降して塔内底部に溜るようになる。この
ように塔内への洗浄水の噴霧を」二下2段に分けて上方
では粗大水滴粒子、下方では微細水滴粒子のシャワーを
汚染空気流に向けて噴霧することにより、塵埃、薗の補
集効率を高めつつ同時に微細水滴粒子が空気流に乗って
水洗塔から外方へ逸出するのを効果的に防止できるよう
になる。さらに加えて水洗塔5内の上部にエリミネータ
14を、また水洗塔5の後段に除滴サイクロン15を設
置することにより、粗大水滴粒子シャワーBaの間隙を
縫って空気流と一緒に下流側へ流出しようとする微細水
滴粒子も空気流から分離補集することができ、これによ
りより一肩の除塵、除菌効率の向上を図ることが可能と
なる。 次に上記した除塵、除重性能の評価を確認するために本
発明者が行った実験結果を示す。 実験条件:第1図の構成で上段スプレーノズル(1本)
の水滴粒径を500μ億、下段スプレーノズル(4本)
の水滴粒径を200μ請、噴霧水量を400A/h、処
理空気量を68n?/h、空気流速度を0.27m/s
として各種粒径の塵埃を含む空気を水洗塔で除塵処理を
行い、除塵後の空気に付いてこれに含まれている塵埃の
粒径分布を測定し、各粒径ごとにその除塵効率を求めた
。 実験結果:前記実験条件で除塵を行った結果によれば、
粒径側の除塵効率は粒径2.0μm以上では100%、
1.0μm以上では99.8%、0.5μm以上では9
8.7%、0.2μm以上では94,2%の良好な集塵
効率が得られた。
FIG. 1 shows an embodiment of the invention, and the same members corresponding to FIG. 2 are given the same reference numerals. That is, according to the present invention, the spray nozzles for water spraying provided inside the water washing tower 5 are divided into upper and lower spray nozzle groups 7a and 7b, where the lower spray nozzle group 7b is used for spraying water. The nozzle has a small diameter mouth and sprays a shower of fine water droplets of about 200 μm, whereas the upper spray nozzle group 7a is a nozzle set to generate a shower of coarse water droplets of about 500 μm. It consists of Note that 11 is a flow rate control valve inserted in a branch pipe to the spray nozzle group at each stage, 12 is a water supply pipe that supplies cleaning water into the tower, 13 is a water level control valve inserted in the same pipe, and 14 is a water level control valve inserted in the same pipe. An eliminator for removing water droplets is installed at the upper part of the water washing tower 5, 15 is a drip removal cyclone for removing water droplets connected to the rear stage of the water washing tower 5, and 16 is a filter inserted in the drain pipe. Next, the operation of the above configuration will be explained. During operation, water pumped by the water pump 8 is supplied to the upper and lower spray nozzle groups 7a and 7b through the flow rate control valve 11, and a shower of fine water droplets P and b is generated in the lower area of the tower. A shower of coarse water droplets Ba is dispersed and sprayed onto the area. On the other hand, dust extracted from a room not shown, Wi
The contaminated air flow containing the contaminated air is introduced from below into the water washing tower 5 through the blower 3 and the prefilter 4, and flows upward in the tower as shown by arrow A, and during this ascending process, it comes into convection contact with the water droplet shower described above. In this case, first, the air stream is sprayed from the spray nozzle group 7b and efficiently contacts the fine water droplets filling the lower area of the tower, and the dust, dirt, etc. contained in the air stream are converted into water droplets. Transferred and collected. At the same time, a shower of coarse water droplets is being sprayed from the spray nozzle 7a on the upper stage in the F direction of this area, and the fine water droplets that have taken in dust and bacteria that rise and float up in the tower with the airflow are coarse. It is captured by water droplets, sinks downward by gravity against the flow of air, and accumulates at the bottom of the tower. In this way, the spraying of cleaning water into the tower is divided into two lower stages, with a shower of coarse water droplets at the top and a shower of fine water droplets at the bottom, making it possible to replenish dust and dirt. While increasing the collection efficiency, it is also possible to effectively prevent fine water droplet particles from escaping outward from the water washing tower by riding on the air flow. Furthermore, by installing an eliminator 14 in the upper part of the water washing tower 5 and a drip removal cyclone 15 at the rear stage of the water washing tower 5, coarse water droplets flow through the gap in the shower Ba and flow to the downstream side together with the air flow. The fine water droplets that are intended to be removed can also be separated and collected from the air flow, thereby making it possible to further improve dust removal and sterilization efficiency. Next, the results of an experiment conducted by the present inventor in order to confirm the evaluation of the above-mentioned dust removal and weight removal performance will be shown. Experimental conditions: Upper spray nozzle (1 nozzle) with the configuration shown in Figure 1.
Water droplet size is 500μ billion, lower spray nozzles (4 pieces)
The water droplet size is 200μ, the amount of spray water is 400A/h, and the amount of air processed is 68n? /h, air flow velocity 0.27m/s
The air containing dust of various particle sizes is treated with a water washing tower to remove dust, and the particle size distribution of the dust contained in the air after dust removal is measured, and the dust removal efficiency is determined for each particle size. Ta. Experimental results: According to the results of dust removal under the above experimental conditions,
The dust removal efficiency on the particle size side is 100% when the particle size is 2.0 μm or more.
99.8% for 1.0 μm or more, 9 for 0.5 μm or more
A good dust collection efficiency of 8.7% and 94.2% was obtained at 0.2 μm or more.

【発明の効果】【Effect of the invention】

以上述べたようにこの発明によれば、水洗塔内に上下複
数段に分けて水滴粒子を塔内に噴霧するスプレーノズル
を配備し、かつ下段側のスプレーノズルからは微細水滴
粒子を1上段側のスプレーノズルからは粗大水滴粒子を
噴霧し、塔内に導入した気体流を下方から上方へ上昇送
風して前記水滴粒子と対流接触させるように構成したこ
とにより、コンパクトな構成で汚染気体中に含まれてい
る微少な塵埃、菌を効果的に分離補集して除塵。 除閉効率の高い除塵・除菌装置を得ることができた。
As described above, according to the present invention, the water washing tower is divided into upper and lower stages with spray nozzles that spray water droplets into the tower, and the spray nozzles on the lower stage spray fine water droplets onto the upper stage. Coarse water droplets are sprayed from the spray nozzle of the tower, and the gas flow introduced into the tower is blown upward from the bottom to bring it into convective contact with the water droplets. Effectively separates and collects minute amounts of dust and bacteria. We were able to obtain a dust removal and sterilization device with high removal and closure efficiency.

【図面の簡単な説明】[Brief explanation of drawings]

第1図はこの発明の実施例の構成配置図、第2図は従来
における一般的な除塵・除菌装置のシステム図である0
図において、 2:気体の循環送風路、3=送送風、5:水洗塔、7a
:粗大水滴粒子噴霧用のスプレーノズル、7b:i細水
滴粒子噴霧用のスプレーノズル、14:除滴用のエリミ
ネータ、15:除滴サイクロン、A:汚染空気流、Ba
、Bb:洗浄水の噴霧シャワー。 七゛3T人弁理1山口 y
Fig. 1 is a configuration diagram of an embodiment of the present invention, and Fig. 2 is a system diagram of a conventional general dust removal and sterilization device.
In the figure, 2: Gas circulation air passage, 3 = Air blower, 5: Water washing tower, 7a
: Spray nozzle for spraying coarse water droplets, 7b: i Spray nozzle for spraying fine water droplets, 14: Eliminator for drip removal, 15: Droplet removal cyclone, A: Contaminated air flow, Ba
, Bb: spray shower of cleaning water. 7゛3T patent attorney 1 Yamaguchi y

Claims (1)

【特許請求の範囲】 1)塵埃、菌を含む汚染気体を水洗塔内に導入し、該水
洗塔内で気体に水を噴霧することにより気体から塵埃、
菌を分離補集して汚染気体を清浄化する気体の除塵・除
菌装置において、前記水洗塔内に上下複数段に分けて水
滴粒子を塔内に噴霧するスプレーノズルを配備し、かつ
下段側のスプレーノズルからは微細水滴粒子を、上段側
のスプレーノズルからは粗大水滴粒子を噴霧し、塔内に
導入した気体流を下方から上方へ上昇送風して前記水滴
粒子と対流接触させるように構成したことを特徴とする
気体の除塵・除菌装置。 2)特許請求の範囲第1項記載の除塵・除菌装置におい
て、下段側スプレーノズルから噴霧する水滴粒子径がほ
ぼ200μm、上段側スプレーノズルから噴霧する水滴
粒子径がほぼ500μm程度に選定されていることを特
徴とする気体の除塵・除菌装置。 3)特許請求の範囲第1項記載の除塵・除菌装置におい
て、水洗塔の後段に気体流から水滴粒子を除去する除滴
サイクロンが接続されていることを特徴とする気体の除
塵・除菌装置。
[Claims] 1) Contaminated gas containing dust and bacteria is introduced into a water washing tower, and water is sprayed onto the gas in the washing tower to remove dust and bacteria from the gas.
In a gaseous dust removal and sterilization device that separates and collects bacteria to purify contaminated gas, the water washing tower is equipped with spray nozzles that spray water droplets into the tower in multiple upper and lower stages; The spray nozzles in the tower spray fine water droplets, and the upper spray nozzles spray coarse water droplets, and the gas flow introduced into the tower is blown upward from below to bring it into convection contact with the water droplets. A gaseous dust removal and sterilization device characterized by: 2) In the dust removal/sterilization device according to claim 1, the diameter of the water droplets sprayed from the lower spray nozzle is approximately 200 μm, and the diameter of the water droplets sprayed from the upper spray nozzle is approximately 500 μm. A gaseous dust removal and sterilization device characterized by: 3) The dust removal and sterilization device according to claim 1, characterized in that a drip removal cyclone for removing water droplets from the gas flow is connected to the rear stage of the water washing tower. Device.
JP60207583A 1985-09-19 1985-09-19 Dust and germ removing device for gas Granted JPS6269032A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP60207583A JPS6269032A (en) 1985-09-19 1985-09-19 Dust and germ removing device for gas

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP60207583A JPS6269032A (en) 1985-09-19 1985-09-19 Dust and germ removing device for gas

Publications (2)

Publication Number Publication Date
JPS6269032A true JPS6269032A (en) 1987-03-30
JPH0325701B2 JPH0325701B2 (en) 1991-04-08

Family

ID=16542159

Family Applications (1)

Application Number Title Priority Date Filing Date
JP60207583A Granted JPS6269032A (en) 1985-09-19 1985-09-19 Dust and germ removing device for gas

Country Status (1)

Country Link
JP (1) JPS6269032A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2003028399A (en) * 2001-07-18 2003-01-29 Matsushita Seiko Co Ltd Water circuit control method
JP2014014799A (en) * 2012-07-11 2014-01-30 Oriental Metal Kk Duct removal device
CN109529505A (en) * 2018-11-27 2019-03-29 湖南省金润碲业有限公司 A kind of metal smelt spray equipment

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2003028399A (en) * 2001-07-18 2003-01-29 Matsushita Seiko Co Ltd Water circuit control method
JP2014014799A (en) * 2012-07-11 2014-01-30 Oriental Metal Kk Duct removal device
CN109529505A (en) * 2018-11-27 2019-03-29 湖南省金润碲业有限公司 A kind of metal smelt spray equipment

Also Published As

Publication number Publication date
JPH0325701B2 (en) 1991-04-08

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