JPH0445229B2 - - Google Patents
Info
- Publication number
- JPH0445229B2 JPH0445229B2 JP62303399A JP30339987A JPH0445229B2 JP H0445229 B2 JPH0445229 B2 JP H0445229B2 JP 62303399 A JP62303399 A JP 62303399A JP 30339987 A JP30339987 A JP 30339987A JP H0445229 B2 JPH0445229 B2 JP H0445229B2
- Authority
- JP
- Japan
- Prior art keywords
- air
- enclosure
- dust
- suction
- suction port
- 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 - Lifetime
Links
- 239000000428 dust Substances 0.000 claims description 35
- 239000011810 insulating material Substances 0.000 claims description 13
- 239000000843 powder Substances 0.000 claims description 9
- 238000007664 blowing Methods 0.000 claims description 6
- 230000000630 rising effect Effects 0.000 claims description 6
- 238000000034 method Methods 0.000 claims description 5
- 239000006185 dispersion Substances 0.000 claims description 4
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 4
- 238000010586 diagram Methods 0.000 description 3
- 230000005484 gravity Effects 0.000 description 3
- 239000011491 glass wool Substances 0.000 description 2
- 238000009413 insulation Methods 0.000 description 2
- 239000012774 insulation material Substances 0.000 description 2
- 239000011490 mineral wool Substances 0.000 description 2
- 238000005192 partition Methods 0.000 description 2
- 239000000377 silicon dioxide Substances 0.000 description 2
- 238000011109 contamination Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000012544 monitoring process Methods 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 230000002265 prevention Effects 0.000 description 1
- 230000008439 repair process Effects 0.000 description 1
- 230000032258 transport Effects 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Landscapes
- Prevention Of Fouling (AREA)
- Filtering Of Dispersed Particles In Gases (AREA)
Description
【発明の詳細な説明】
本発明は、保温材で覆われた蒸気タービン、ポ
ンプ等の機器を補修する際、該保温材が飛散、拡
散するのを防止できるようにした防止方法に関す
る。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for preventing heat insulating material from scattering and spreading when repairing equipment such as steam turbines and pumps covered with heat insulating material.
火力発電所等の蒸気タービン、ポンプ、給水加
熱器、バルブ、脱気器等の機器は、シリカボー
ド、グラスウール、ロツクウールその他の保温材
で覆われているので、補修に際しては、これらの
機器に対し施工してある保温装備の解体作業を先
行して実施する必要がある。通常の場合、上記機
器の稼動率を考慮し、補修を短期間で完了しなけ
ればならないので、高温で長時間に亘り運転され
ていた機器を停止させた後、周囲温度まで該機器
が冷却するのを待たずに保温装備の解体を行つて
いる。そのため、解体作業時に生じた保温材の微
粉末が、高温による上昇気流に乗つて広い範囲ま
で飛散し、周辺で運転中の他の機器に多大な影響
を与えていた。 Steam turbines, pumps, feed water heaters, valves, deaerators, and other equipment in thermal power plants are covered with silica boards, glass wool, rock wool, and other heat-insulating materials, so when repairing these equipment, It is necessary to dismantle the heat insulation equipment that has been constructed in advance. In normal cases, repairs must be completed in a short period of time considering the operating rate of the above equipment, so after the equipment has been operating at high temperatures for a long period of time, it is necessary to stop the equipment and then allow the equipment to cool down to ambient temperature. They are dismantling the heat insulation equipment without waiting for it. As a result, fine powder from the heat insulating material generated during demolition work was carried over a wide area by the rising air currents due to high temperatures, and had a significant impact on other equipment operating in the vicinity.
出願人は、先に、保温材の微粉末が飛散するの
を防止するよう機器の周囲を囲いで覆い、該囲い
に吸引集塵器を連結した飛散防止設備を提案した
が、微粉末の挙動は不安定であり、かつ囲い中の
空間に温度差があるため、高温上昇気流から外れ
た保温微粉末が短時間のうちに囲い内全域に拡散
し、囲い内の粉塵濃度が極度に上昇して、内部で
の作業環境を悪化させることがあつた。 The applicant previously proposed a scattering prevention facility in which a device is covered with an enclosure to prevent the fine powder of heat insulating material from scattering, and a suction dust collector is connected to the enclosure. is unstable and there is a temperature difference in the space inside the enclosure, so the insulating fine powder that is removed from the high-temperature rising air spreads throughout the enclosure in a short period of time, causing the dust concentration inside the enclosure to increase extremely. As a result, the internal working environment deteriorated.
本発明は、従来考慮されていなかつた囲い本体
内の内部の空気流に着目し、高温自然対流による
粉塵を乗せた気流を吸引口へ移送するよう囲い本
体内に空気流を導入し、該空気流によつて囲い本
体内に拡散する微粉末を吸引口に集めて吸引集塵
装置で集塵することができるようにした飛散、拡
散防止方法に係るものである。 The present invention focuses on the air flow inside the enclosure body, which has not been considered in the past, and introduces the air flow into the enclosure body so that the air flow carrying dust due to high temperature natural convection is transferred to the suction port. This invention relates to a method for preventing scattering and dispersion in which fine powder that is dispersed in an enclosure body by a flow is collected at a suction port and collected by a suction dust collector.
以下実施例と共に詳細に説明する。 This will be explained in detail below along with examples.
図において、蒸気タービン等の機器1を取り囲
む囲い本体2は、粉塵濃度を規定するのに必要な
作業空間を限定するような大きさを有し、上記機
器1をまたぐよう形成した支柱3……に不燃性シ
ート4を貼つて作られる。該支柱は、機器の周囲
に自立するよう適宜の柱状材料を組立てるように
しているが、蛇腹式に構成して伸縮可能にするこ
ともでき、また下端にキヤスターを設けたり、車
輪、レールを設けて移動可能に設けることもでき
る。なお、第3図に示すように、適宜の空間を有
する囲いブロツク5を形成し、該囲いブロツク5
を所要数接続して、所望の大きさの囲い本体2を
作るようにすることもできる。上記囲い本体2の
天井部、側面部はそれぞれ数枚のシートを貼り合
せて形成するとよく、例えば天井部は4枚、側面
は2〜4枚のシートで構成し、端縁に面状フアス
ナー(図示略)を設けて着脱自在に接合する。こ
のようにすれば、シートの着脱が容易であり、火
力発電所の蒸気タービンのように大きな機器へ搬
出入するときはシートを外して作業空間を広くす
ることができ、便利である。また、囲い本体内に
上記シート同様の着脱可能な間仕切りシート6を
設けて垂下するようにすれば、内容積を適切に選
択、設定でき、このため微粉塵の浮遊域を限定す
ることができる(第2図)。なお、第4図に示す
ように、機器1の断面方向のシート4は、適宜数
に分割し、各シート部辺7……をフアスナー8…
…で開閉自在に接続しておけば、機器の形状に合
わせて囲い本体内に密閉状況を作り出すことがで
きる。出入口は適宜の側面に形成することがで
き、シートの一部を区画して扉9を設け、フアス
ナー10で開閉可能に設けるとよい。 In the figure, an enclosure main body 2 surrounding equipment 1 such as a steam turbine has a size that limits the working space necessary to regulate dust concentration, and supports 3 formed to straddle the equipment 1... It is made by pasting a nonflammable sheet 4 on the The support is constructed by assembling appropriate columnar materials around the equipment so that it can stand on its own, but it can also be configured in a bellows style to make it expandable and retractable, or it can be equipped with casters, wheels, or rails at the lower end. It can also be provided movably. As shown in FIG. 3, an enclosing block 5 having an appropriate space is formed, and the enclosing block 5
It is also possible to create an enclosure body 2 of a desired size by connecting a required number of them. The ceiling and side parts of the enclosure body 2 are preferably formed by bonding several sheets together. For example, the ceiling part is made up of four sheets, the side parts are made up of two to four sheets, and the edges are provided with a sheet fastener ( (not shown) and are removably joined. In this way, it is easy to attach and detach the seat, and when transporting into and out of large equipment such as a steam turbine in a thermal power plant, the seat can be removed to enlarge the work space, which is convenient. Furthermore, if a removable partition sheet 6 similar to the above-mentioned sheet is provided in the enclosure main body so that it hangs down, the internal volume can be appropriately selected and set, and therefore the floating area of fine dust can be limited ( Figure 2). As shown in FIG. 4, the sheet 4 in the cross-sectional direction of the device 1 is divided into an appropriate number of parts, and the sides 7 of each sheet part are fastened with fasteners 8.
If you connect them so that they can be opened and closed, you can create a sealed situation inside the enclosure to match the shape of the device. The entrance/exit can be formed on an appropriate side surface, and it is preferable to partition a part of the seat and provide a door 9 which can be opened and closed with a fastener 10.
上記囲い本体2内には、上記機器から発生する
上昇気流を囲い本体の側面若しくは天井等に設け
た後記する吸引方向へ移送するよう空気流が導入
される。図において、囲い本体外に設けたブロワ
ー、コンプレツサー等の送風装置11により囲い
本体外の新鮮な外気を空気移送管12を通し空気
吐出口13から囲い本体内へ強制送風している。
該空気吐出口13は、適宜位置に適宜数設けるこ
とができ、例えば第1図に示すものでは、機器1
のほぼ中央に移動可能にスタンド14を置き、該
スタンドに両側方向に向く吐出口13,13を設
けているが、機器の下方から上方に向く吐出口を
形成したり、囲い本体2の側面に吐出口を設ける
ことができる。なお、該吐出口13の移送管12
をたわみ管で構成したり、吐出口の支承部に自在
接手を設けて、吐出口が囲い本体内で働く作業者
を避けて吸引口方向の任意の方向に向くようにし
てある。また、上記送風装置11若しくは移送管
12の途中に風量調整装置15を設け、送風量を
調整するようにしてある。この場合、囲い本体の
容積と、後記する吸引口からの吸い込み量とを併
せて検討し、囲い本体内部が常に負圧に保たれる
ようにし、囲い内部の粉塵が外部に洩れないよう
にする。この状態のもとで、囲い本体内で発塵す
る粉塵を吸引口より回収するに必要な送風量は、
吸引口からの吸込量の約15%〜25%、好ましくは
約20%程度にするとよい。 An air flow is introduced into the enclosure main body 2 so as to transfer the rising air current generated from the equipment in the direction of suction provided on the side surface or ceiling of the enclosure main body, which will be described later. In the figure, fresh outside air outside the enclosure body is forcibly blown into the enclosure body from an air outlet 13 through an air transfer pipe 12 by an air blowing device 11 such as a blower or compressor provided outside the enclosure body.
The air outlet 13 can be provided in an appropriate number at an appropriate position. For example, in the one shown in FIG.
A stand 14 is movably placed approximately in the center of the enclosure, and discharge ports 13, 13 facing both sides are provided on the stand. A discharge port can be provided. Note that the transfer pipe 12 of the discharge port 13
The discharge port is constructed of a flexible tube, or a flexible joint is provided on the support portion of the discharge port so that the discharge port can be directed in any direction toward the suction port, avoiding the operator working inside the enclosure main body. Further, an air volume adjusting device 15 is provided in the middle of the air blowing device 11 or the transfer pipe 12 to adjust the amount of air blown. In this case, consider the volume of the enclosure body and the amount of suction from the suction port (described later), and make sure that the inside of the enclosure body is always maintained at a negative pressure to prevent the dust inside the enclosure from leaking to the outside. . Under this condition, the amount of air required to collect the dust generated inside the enclosure from the suction port is:
The amount of suction from the suction port should be about 15% to 25%, preferably about 20%.
上記空気流に対向する囲い本体2の壁面には、
該空気流を吸引するよう吸引口16を形成してあ
り、該吸込口16には粉塵移送ダクト17を介し
吸引集塵装置18が接続されている。上記吸引口
16は、周囲に吸込フード19を形成し、該フー
ド19の開口縁に面フアスナー20を設け、該面
フアスナーをシートの開口部21の周縁に設けた
面フアスナー22に係合させてシートに取付ける
(第5図、第6図)。上記シートに設ける開口部は
適宜の位置に適宜数設けるとよく、上記フードを
取付けない開口部には、第7図に示すように周縁
に面フアスナー23を有する盲シート24を取付
けておけばよい。このようにすれば、吸引口を上
下左右等任意の位置に移動させることができる
し、盲シートを透明シートで形成すれば監視窓と
して利用することもできる。 On the wall of the enclosure main body 2 facing the air flow,
A suction port 16 is formed to suck the air flow, and a suction dust collector 18 is connected to the suction port 16 via a dust transfer duct 17. The suction port 16 has a suction hood 19 formed around it, a hook-and-loop fastener 20 provided at the opening edge of the hood 19, and the hook-and-loop fastener 20 engaged with a hook-and-loop fastener 22 provided at the periphery of the opening 21 of the sheet. Attach to the seat (Figures 5 and 6). An appropriate number of openings may be provided in the sheet at appropriate positions, and blind sheets 24 having hook-and-loop fasteners 23 on the periphery may be attached to the openings where the hood is not attached, as shown in FIG. . In this way, the suction port can be moved to any position such as up, down, right, left, etc., and if the blind sheet is made of a transparent sheet, it can also be used as a monitoring window.
上記吸込フードの傾斜角θは、第8図に示すよ
うに、空気吐出口13からの空気流に乗つた粉塵
がフードに衝突後、中心軸に対しβの角で進行す
るとき、β<90°であれば吸引口へ滑かに吸引さ
れると考えられる。したがつて、空気流(粉塵
流)の中心軸に対する角度をαとすると、
β=α+2θ<90° ……
の関係にあればよい。ここで、フードの半径をA
m、空気吐出口からフードまでの距離をDmとす
れば、
tanα=A/D ……
上記,式よりフードの半径及び空気吐出口
からフードまでの距離が決まれば、フードの傾斜
角θが定まる。例えば、フードの直径が2m、距
離が5mのとき、傾斜角θは、θ<39.3°となる。
なお、フードは、円錐状でも角錐状でもよく、角
錐状の場合には中心軸からフード外縁までの距離
をAの値とすればよい。実験によれば、囲い本体
の幅を10mとしたとき、中央に空気吐出口を設け
ればD=5m、フード口径2mが適当でフードの
傾斜角θは多少の余裕を見てθ<35°程度が好適
な結果を得られた。なお、上記角度αが小さく中
心軸寄りに空気流(粉塵流)が進行すれば、一層
滑かに吸引口へ流入することは明らかである。 As shown in FIG. 8, the inclination angle θ of the suction hood is determined to be β<90 when dust carried by the airflow from the air outlet 13 travels at an angle β with respect to the central axis after colliding with the hood. °, it is considered that the fluid is smoothly sucked into the suction port. Therefore, if the angle of the air flow (dust flow) with respect to the central axis is α, then the relationship β=α+2θ<90° is sufficient. Here, the radius of the hood is A
m, and if the distance from the air outlet to the hood is Dm, then tanα=A/D... From the above formula, if the radius of the hood and the distance from the air outlet to the hood are determined, the inclination angle θ of the hood is determined. . For example, when the diameter of the hood is 2 m and the distance is 5 m, the inclination angle θ is θ<39.3°.
The hood may have a conical or pyramidal shape, and in the case of a pyramidal shape, the value of A may be the distance from the central axis to the outer edge of the hood. According to experiments, when the width of the enclosure body is 10 m, if the air outlet is provided in the center, D = 5 m, the hood diameter is 2 m, and the inclination angle θ of the hood is θ < 35° with some allowance. Appropriate results were obtained. It is clear that if the angle α is small and the air flow (dust flow) advances toward the central axis, it will flow into the suction port more smoothly.
また、粉塵を搬送する空気流の速度は、保温材
の解体作業時に舞い上つた粉塵が、重力により落
下する間に吐出口から吐出されてくる空気流に乗
りながら移動し、この移動時間内に落下する距離
が吸込フードの吸込領域内であるように決定すれ
ば、集塵効果が良好となる。そして、空気流の速
度をv(m/s)、粉塵の落下速度をw(m/s)、
粉塵の落下距離(吸込フードの有効寸法)h
(m)、粉塵の移動距離l(m)とすると
h=l/v×w
ここで、保温材として使用されているシリカボ
ード、グラスウール、ロツクウール等の真比重
(粉塵比重)を約2.0とし、集塵対象の長時間浮遊
粉塵の大きさ(粒径)を4〜20μとすると、w=
0.06〜1.3(m/s)となる。また、上記のように
吸込フードの有効寸法を2mとし、移動距離の最
大を5mとすると、
v=l/h・w=5/2×(0.06〜1.3)
=0.15〜3.25(m/s)
したがつて、空気流の速度は0.15〜3.25m/s
が良く、実験の結果によれば約3m/sの流速が
良い結果を得られた。 In addition, the speed of the air flow that transports the dust is such that the dust that flies up during the dismantling work of the insulation material moves while riding on the air flow discharged from the discharge port while falling due to gravity. If the falling distance is determined to be within the suction area of the suction hood, the dust collection effect will be good. Then, the speed of the air flow is v (m/s), the falling speed of the dust is w (m/s),
Falling distance of dust (effective dimension of suction hood) h
(m), and the moving distance of dust l (m), then h=l/v×w Here, assuming that the true specific gravity (dust specific gravity) of silica board, glass wool, rock wool, etc. used as a heat insulating material is approximately 2.0, If the size (particle size) of long-suspended dust to be collected is 4 to 20 μ, w =
0.06 to 1.3 (m/s). Also, if the effective dimension of the suction hood is 2m and the maximum moving distance is 5m as mentioned above, then v=l/h・w=5/2×(0.06~1.3) =0.15~3.25 (m/s) Therefore, the speed of the air flow is 0.15 to 3.25 m/s
According to the experimental results, a flow velocity of about 3 m/s gave good results.
而して、第9図の概略図に示すように、蒸気タ
ービン等の機器1を囲い本体2で取り囲み、上記
送風装置11及び吸引集塵装置18を作動させな
がら、囲い本体内で保温材の解体作業を行うと、
保温材の微粉末は、機器から生じた上昇気流によ
り飛散しようとするが、囲い本体内に導入された
空気流25に乗つて吸込フード19を介し吸引口
16へ吸引され、集塵される。このように強制送
風された空気流によつて高温自然対流による粉塵
を乗せた空気流は、強制的に吸込フードの方向へ
と誘導され、微粉塵のほとんどすべてが吸引され
る。高温自然対流に乗らない保温材の微粉塵も、
上記強制送風された空気流25によつて該空気流
の周囲の空気が引き寄せられるような形で発生す
る誘引流26により上記空気流25へと引き寄せ
られ、吸引口へ吸引される。 As shown in the schematic diagram of FIG. 9, a device 1 such as a steam turbine is surrounded by an enclosure main body 2, and while the above-mentioned air blower 11 and suction dust collector 18 are operated, a heat insulating material is placed inside the enclosure main body. When carrying out demolition work,
The fine powder of the heat insulating material tends to be scattered by the rising airflow generated from the equipment, but it is sucked into the suction port 16 via the suction hood 19 by the airflow 25 introduced into the enclosure main body, and is collected. The airflow carrying dust due to high-temperature natural convection by the forced airflow is forcibly guided toward the suction hood, and almost all of the fine dust is sucked. Fine dust from insulation materials that do not take part in high-temperature natural convection,
The forced air flow 25 generates an induced flow 26 in such a manner that the air around the air flow is attracted, and the air is drawn toward the air flow 25 and sucked into the suction port.
本発明は以上のように構成され、囲い本体内に
発生する上昇気流を吸引口から吸引して集塵する
ようにした保温材微粉末の飛散、拡散防止方法に
おいて、上記吸引口に対向して本体内に外気を送
風する空気吐出口を設けたから、囲い本体内に指
向性を持たせた局所強制送風を行うことができ、
該局所強制送風によつて高温自然対流による粉塵
を乗せた空気流は、強制的に吸引口へと誘導さ
れ、微粉末のほとんどすべてが吸引される。この
際、上記強制送風は指向性を持つているから、粉
塵発生箇所のみを対象として上記吸引口へ誘導す
るように空気吐出口の方向を調整すれば、囲い本
体内で上記作業を行う作業者を避けて送風するこ
とができ、労働安全施行規則にも則つた安全な作
業環境を作り出すことができる。その上、上記送
風量を吸引量の15%〜25%としたので、囲い本体
内は負圧状態に保持され、床や機器との接触部等
に隙間があつたり、外気が侵入するおそれがある
ような半開放構造の囲い本体であつても、外部に
微粉塵が飛散されることはなく、また送風量の最
大値を吸引量の25%以内としたから、軟質シート
材料等で作られた囲い本体が、送風空気を受けて
膨張しようとしても、これを妨げる程の負圧を確
保することができると共に強風によつて粉塵の空
気流が攪乱されて粉塵を囲い本体内に拡散させて
しまうということもなく、また15%以上とするこ
とにより指向性をもたせた最少限の強制送風を行
うことができ、効果的に集塵することができ、大
規模な設備を必要とせずに囲い本体内の粉塵濃度
を任意の時間内で制御することができ、良好な作
業環境を提供でき、また作業場所の周辺を汚染し
ないようにすることができる。 The present invention is constructed as described above, and in a method for preventing scattering and dispersion of heat insulating material fine powder, which collects dust by suctioning upward airflow generated within an enclosure main body from a suction port, Since an air outlet for blowing outside air is provided inside the main body, it is possible to perform local forced air blowing with directionality within the enclosure main body.
Due to the local forced air flow, the air flow carrying dust due to high temperature natural convection is forcibly guided to the suction port, and almost all of the fine powder is sucked. At this time, the forced air is directional, so if you adjust the direction of the air outlet so that it directs the air to the suction port only at the location where dust is generated, the operator performing the above work inside the enclosure body can This allows the air to be blown while avoiding the above, creating a safe work environment that complies with the Industrial Safety Enforcement Regulations. Furthermore, since the air flow rate is set to 15% to 25% of the suction volume, a negative pressure is maintained inside the enclosure, which creates gaps at the floor and contact points with equipment, and there is a risk of outside air infiltrating. Even with a half-open enclosure structure like this, fine dust will not be scattered to the outside, and since the maximum air volume was set to within 25% of the suction volume, it is recommended to Even if the enclosure body tries to expand due to the blowing air, it is possible to secure enough negative pressure to prevent this expansion, and strong winds will disturb the airflow of dust and cause the dust to spread inside the enclosure body. In addition, by setting the ratio to 15% or more, it is possible to perform a minimum amount of forced air with directionality, and it is possible to collect dust effectively, without the need for large-scale equipment. It is possible to control the dust concentration within a given period of time, provide a good working environment, and prevent contamination of the surroundings of the work place.
図面は本発明の実施例を示し、第1図は断面
図、第2図は平面図、第3図は変形例の斜視図、
第4図及び第5図はシートの正面図、第6図は吸
込フード部分の拡大断面図、第7図は盲シート部
分の拡大断面図、第8図は吸込フードの傾斜角の
説明図、第9図は概略図である。
1……機器、2……囲い本体、13……空気吐
出口、16……吸引口、18……吸引集塵装置、
19……吸込フード。
The drawings show embodiments of the present invention; FIG. 1 is a sectional view, FIG. 2 is a plan view, and FIG. 3 is a perspective view of a modified example.
4 and 5 are front views of the seat, FIG. 6 is an enlarged sectional view of the suction hood portion, FIG. 7 is an enlarged sectional view of the blind seat portion, and FIG. 8 is an explanatory diagram of the inclination angle of the suction hood. FIG. 9 is a schematic diagram. 1... equipment, 2... enclosure main body, 13... air discharge port, 16... suction port, 18... suction dust collector,
19...Suction hood.
Claims (1)
み、該保温材を解体する際に発生する上昇気流を
吸引口から吸引して集塵するようにした保温材微
粉末の飛散、拡散防止方法において、上記上昇気
流を上記吸引口へ向けて移送するよう本体内へ外
気を送風する空気吐出口を設け、該吐出口からの
送風量を上記吸引口からの吸引量の15%〜25%と
し上記囲い本体内を負圧状態に保持することを特
徴とする保温材微粉末の飛散、拡散防止方法。1. In a method for preventing the scattering and dispersion of heat insulating material fine powder, which involves surrounding equipment insulated with heat insulating material with an enclosure body, and collecting dust by suctioning the rising airflow generated when the heat insulating material is dismantled through a suction port. , an air discharge port is provided for blowing outside air into the main body so as to transfer the rising airflow toward the suction port, and the amount of air blown from the discharge port is 15% to 25% of the amount of suction from the suction port, as described above. A method for preventing scattering and dispersion of heat insulating material fine powder, which is characterized by maintaining a negative pressure state within the enclosure body.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP30339987A JPH01148382A (en) | 1987-12-02 | 1987-12-02 | Equipment for preventing scattering and diffusion of fine powder of insulating material |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP30339987A JPH01148382A (en) | 1987-12-02 | 1987-12-02 | Equipment for preventing scattering and diffusion of fine powder of insulating material |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH01148382A JPH01148382A (en) | 1989-06-09 |
JPH0445229B2 true JPH0445229B2 (en) | 1992-07-24 |
Family
ID=17920557
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP30339987A Granted JPH01148382A (en) | 1987-12-02 | 1987-12-02 | Equipment for preventing scattering and diffusion of fine powder of insulating material |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH01148382A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR20160089455A (en) | 2013-12-25 | 2016-07-27 | 가부시키가이샤 고베 세이코쇼 | Method for producing ashless coal |
KR20160089438A (en) | 2013-12-25 | 2016-07-27 | 가부시키가이샤 고베 세이코쇼 | Method for producing ashless coal |
Families Citing this family (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP5082736B2 (en) * | 2007-10-05 | 2012-11-28 | 株式会社大林組 | Deposit removal method |
PL2363192T3 (en) | 2010-02-18 | 2013-05-31 | General Electric Technology Gmbh | Filter system |
JP5327298B2 (en) * | 2011-09-09 | 2013-10-30 | 株式会社大林組 | Deposit removing method and deposit removing apparatus |
Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS471508U (en) * | 1971-01-16 | 1972-08-17 |
Family Cites Families (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5196860U (en) * | 1975-01-31 | 1976-08-03 | ||
JPS60193291U (en) * | 1984-06-01 | 1985-12-23 | 石川島播磨重工業株式会社 | clean room |
-
1987
- 1987-12-02 JP JP30339987A patent/JPH01148382A/en active Granted
Patent Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS471508U (en) * | 1971-01-16 | 1972-08-17 |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR20160089455A (en) | 2013-12-25 | 2016-07-27 | 가부시키가이샤 고베 세이코쇼 | Method for producing ashless coal |
KR20160089438A (en) | 2013-12-25 | 2016-07-27 | 가부시키가이샤 고베 세이코쇼 | Method for producing ashless coal |
Also Published As
Publication number | Publication date |
---|---|
JPH01148382A (en) | 1989-06-09 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
EP0245110B1 (en) | Apparatus for generating an artificial tornado | |
JPS5925931B2 (en) | ventilation system | |
WO2002021051A1 (en) | Decorative panel for air conditioning system, air outlet unit, and air conditioning system | |
JPH01501564A (en) | Improved fluid barrier curtain system | |
JPH01266467A (en) | Method and device for preheating air for ventilation | |
JP3624808B2 (en) | Air conditioner decorative panel, air outlet unit, and air conditioner | |
JPH0445229B2 (en) | ||
JPH0411769B2 (en) | ||
US6623352B2 (en) | Vortex air barrier | |
CA1134666A (en) | Air circulating device for mixing room air | |
JPS59157432A (en) | Rearrangement type local environmental control room | |
US3974754A (en) | Controlled fluid flow systems | |
CN106705683B (en) | Cold quick-witted material receiving point dust collector that induced drafts of ring | |
CN106475210B (en) | A kind of ultra-low humidity low temperature enters the wind disintegrating apparatus | |
JPH03207925A (en) | Waste gas exhausting device | |
Cao et al. | Local ventilation | |
JP3465389B2 (en) | Cooling method and cooling device for high-temperature heating workplace | |
CN107023920A (en) | A kind of cooling system | |
JP2557672Y2 (en) | Equipment for transporting gas, etc. | |
Woods et al. | Evaluation of capture efficiencies of large push-pull ventilation systems with both visual and tracer techniques | |
CN207900272U (en) | A kind of multilayer coil pipe or so end plate processing drilling device | |
EP3450872B1 (en) | Air supply device | |
JP2936149B2 (en) | Ventilation equipment for space facilities with heat sources | |
JPH11244805A (en) | Circulating air flow type dust collector | |
CN210859361U (en) | Sound insulation and noise reduction device for fan |