JPH09113435A - Measuring apparatus for dust holding amount of bag filter - Google Patents

Measuring apparatus for dust holding amount of bag filter

Info

Publication number
JPH09113435A
JPH09113435A JP29598495A JP29598495A JPH09113435A JP H09113435 A JPH09113435 A JP H09113435A JP 29598495 A JP29598495 A JP 29598495A JP 29598495 A JP29598495 A JP 29598495A JP H09113435 A JPH09113435 A JP H09113435A
Authority
JP
Japan
Prior art keywords
dust
air
test piece
filter
chamber
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
JP29598495A
Other languages
Japanese (ja)
Other versions
JP3280552B2 (en
Inventor
Akira Matsunaga
晃 松永
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.)
AMANO KOGYO GIJUTSU KENKYUSHO
Original Assignee
AMANO KOGYO GIJUTSU KENKYUSHO
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 AMANO KOGYO GIJUTSU KENKYUSHO filed Critical AMANO KOGYO GIJUTSU KENKYUSHO
Priority to JP29598495A priority Critical patent/JP3280552B2/en
Publication of JPH09113435A publication Critical patent/JPH09113435A/en
Application granted granted Critical
Publication of JP3280552B2 publication Critical patent/JP3280552B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Abstract

PROBLEM TO BE SOLVED: To obtain a measuring apparatus by which the dust holding amount of a dust filter (a bag filter) can be measured automatically by a method wherein a time-dependent change in a fiter differential pressure generated between an air-to-be- filtered storage chamber and a clean air chamber is recorded, an air suction operation is stopped when the filter differential pressure becomes a prescribed value and the compressed air is spouted from a nozzle. SOLUTION: A filter body part 1 is constituted of a test-piece mounting part 3, of a clean air chamber 4, of an air-to-be-filtered storage chamber 5 and of a floating- dust generation device. First, a test piece at a dust filter 47 is set on the test-piece mounting part 3, the floating-dust generation device is operated, and the filtering operation of the air in the air-to-be-filtered storage chamber 5 is started at a constant filtration speed. Simultaneously with the start of the filtering operation, a filter differential pressure ΔP due to the filter 47 is generated, and it is always measured and recorded by a differential pressure (ΔP) measuring and recording device. Then, when the differential pressure ΔP which is increased due to an increase in a dust accumulation amount reaches a preset value, an air suction operation by an isokinetic sampling device is stopped, and dust particles which are stuck to the test piece are blown off by the compressed air.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【発明の属する技術分野】本発明は、集塵機、集塵装
置、空気輸送装置等に使用される袋状の濾材、いわゆる
バグフィルターの濾過性能を試験する装置に関するもの
であり、特に粉塵保持量を測定するための装置に関する
ものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a bag-shaped filter material used for a dust collector, a dust collector, an air transportation device, etc., and a device for testing the filtering performance of a so-called bag filter, and more particularly to a device for testing the dust holding amount The present invention relates to a device for measuring.

【0002】なお、この明細書では空気輸送装置におい
て輸送対象となる粉粒体を含む意味で粉塵と言う。
[0002] In this specification, the term "dust" is used to mean that it includes a granular material to be transported in an air transportation device.

【0003】[0003]

【従来の技術】集塵機による除塵や空気輸送装置による
粉粒体の輸送においては、時間が経過するにつれて、バ
グフィルター表面に堆積して行く粉塵によりフィルター
通過前後の空気の圧力差(いわゆるフィルター差圧)Δ
Pが徐々に上昇する。そして、集塵では吸引風量が減少
して集塵不能の状態になり、空気輸送ではフィルターか
ら粉塵の吹き抜けやフィルターの破壊が発生する。した
がって、差圧ΔPがある値に達したとき、あるいは一定
時間経過後に、堆積した粉塵を払い落して差圧ΔPを低
下させる操作が(多くの場合自動的に)行われる。
2. Description of the Related Art In dust removal by a dust collector and transportation of powder particles by an air transportation device, dust accumulated on the surface of a bag filter as time passes, the pressure difference between air before and after passing through the filter (so-called filter differential pressure). ) Δ
P gradually rises. Then, in the dust collection, the amount of suction air decreases and the dust cannot be collected, and in air transportation, dust blows through the filter or the filter is broken. Therefore, when the differential pressure ΔP reaches a certain value or after a lapse of a certain period of time, an operation is performed (in many cases automatically) to remove the accumulated dust to reduce the differential pressure ΔP.

【0004】粉塵が堆積しても差圧ΔPの上昇が少ない
バグフィルターは、粉塵払い落し操作の間隔を長くする
ことができ、空気吸引のための動力費も少なくて済むの
で有利である。そこで、排気濃度、分離効率などの質的
能力のほかに量的な処理能力をバグフィルターについて
確認しておくことが集塵装置等を設計するために必要に
なる。
A bag filter, in which the differential pressure ΔP hardly rises even if dust is accumulated, is advantageous because the interval for dusting-off operation can be lengthened and the power consumption for air suction can be reduced. Therefore, it is necessary to confirm the quantitative treatment capacity of the bag filter in addition to the qualitative capacity such as exhaust concentration and separation efficiency in order to design the dust collector.

【0005】バグフィルターの量的性能を示すために
は、フィルター上に堆積した粉塵の単位面積当たりの質
量を粉塵負荷と呼び、ある粉塵負荷に対し濾過速度を変
化させそれに対応する差圧ΔPを測定したデータを表示
することが行われている。この場合、差圧ΔPは粉塵の
複雑な性質と濾過風速に影響されて多様に変化するか
ら、フィルターの性能を比較するには同じ粉塵、同一の
濾過風速、同一の粉塵負荷とう条件で差圧ΔPを比較し
たときΔPが低いほうが性能のよいフィルターというこ
とになる。また、同じデータから、同一の差圧ΔPで粉
塵負荷が大きいものほどよいフィルターという判定も行
う。
In order to show the quantitative performance of the bag filter, the mass per unit area of the dust accumulated on the filter is called the dust load, and the filtration speed is changed with respect to a certain dust load, and the differential pressure ΔP corresponding thereto is changed. The measured data is displayed. In this case, since the differential pressure ΔP varies variously depending on the complicated properties of dust and the filtration wind speed, the pressure difference under the same dust, the same filtration wind speed, and the same dust load condition can be compared to compare the filter performance. When ΔP is compared, the lower ΔP means a better filter. Also, from the same data, it is determined that the filter having the same differential pressure ΔP and the larger dust load is the better filter.

【0006】しかしながら、粉塵負荷という用語は、当
業界では上述の意味よりも単なるフィルターへの負荷、
負担という意味で用いられることが多く、バグフィルタ
ーの量的能力という意味ではほとんど用いられていな
い。その原因は、粉塵負荷の正確な測定が困難なことに
ある。すなわち、量的能力としての粉塵負荷を求めるに
は払い落しのたびに堆積した粉塵の質量を測定する作業
を該粉塵質量が安定するまで続けることになるが、粉塵
質量の測定には試料の着脱、粉塵の採取・秤量等、大変
な手間がかかるため、数回程度でやめてしまうことが多
い。また、測定される粉塵質量が安定するまで数百回の
測定を行なったとしても、粉塵負荷は粉塵の性質、濾過
速度等によっても変化するので、そのように苦労して得
たデータもその条件下でのみ有効なのであって普遍性あ
るものではない。単に優劣の順位が決まるにすぎないの
である。
However, the term dust load is more than a mere load on the filter in the art, rather than the above meaning.
It is often used in the sense of burden, and is rarely used in the sense of the quantitative capacity of bag filters. The cause is that it is difficult to measure the dust load accurately. That is, in order to obtain the dust load as a quantitative capacity, the work of measuring the mass of dust accumulated every time it is removed is continued until the dust mass becomes stable. However, it takes a lot of time and labor to collect and weigh dust, so it is often stopped after a few times. In addition, even if the measurement is performed several hundred times until the measured dust mass is stable, the dust load also changes depending on the nature of the dust, the filtration rate, etc. It is only valid below and is not universal. It simply determines the rank of superiority or inferiority.

【0007】従来、最も普通に行われているバグフィル
ターの量的能力の評価方法は、同一条件下で粉塵の吸引
と払い落しを繰り返して払い落し後の吸引再開直後に測
定される差圧ΔP(ベース圧損という)を記録し、徐々
に上昇するベース圧損が最終的に安定してそれ以上上昇
しなくなったときの値を比較し、それが低いフィルター
を性能がよいものと評価するである。
Conventionally, the most commonly used method for evaluating the quantitative performance of a bag filter is to repeat the suction and removal of dust under the same conditions by repeating the differential pressure ΔP measured immediately after restarting the suction. It records the (base pressure loss), compares the values when the gradually increasing base pressure loss finally becomes stable and does not rise any more, and evaluates a filter having a low value as good performance.

【0008】しかしながら、この評価方法はベース圧損
の飽和値という単なる結果だけを求めているため、その
原因を究明することが難しく、また、それを技術的に利
用することができない。そのため、ベース圧損に着目し
た評価結果は集塵機等バグフィルターを用いる機械・装
置の設計には参考にされる程度であって、実際には経験
や実績が重視されることが多い。
However, this evaluation method requires only the result of the saturation value of the base pressure loss, so that it is difficult to find the cause and it is not possible to use it technically. Therefore, the evaluation result focusing on the base pressure loss is only a reference when designing a machine / apparatus using a bag filter such as a dust collector, and in practice, experience and achievements are often emphasized.

【0009】上述のように、差圧ΔPを測定した結果か
らバグフィルターの性能を判断するよりも、粉塵負荷を
正確に測定してその結果を利用するほうが本来望ましい
ことである。このような観点から粉塵負荷と差圧ΔPと
の関係を深く考察して行くと、吸塵と払い落しを繰り返
してベース圧損が安定したときの粉塵負荷が特に重要で
あることがわかると共に、従来使われている粉塵負荷と
いう用語の意味があいまいであったことに気がつく。そ
こで本発明者は、 粉塵負荷=残留粉塵量+粉塵保持量 と定義して粉塵保持量という概念を新たに導入し、バグ
フィルターの量的能力を評価するのにこの粉塵保持量に
着目することとした。
As described above, it is essentially desirable to accurately measure the dust load and use the result rather than judging the performance of the bag filter from the result of measuring the differential pressure ΔP. From this point of view, a deep study of the relationship between the dust load and the differential pressure ΔP reveals that the dust load is particularly important when the base pressure loss becomes stable by repeating dust absorption and dust removal, and it is also used in the conventional method. We find that the term dust load, which is known, was ambiguous in meaning. Therefore, the present inventor newly introduces the concept of dust holding amount by defining dust load = residual dust amount + dust holding amount, and pays attention to this dust holding amount in order to evaluate the quantitative performance of the bag filter. And

【0010】ここで、 粉塵負荷(g/m2):フィルターの濾過面に堆積した総粉
塵質量。 残留粉塵量(g/m2):粉塵を払い落した後もフィルター
表面及びその内部に残留している粉塵の質量。 粉塵保持量(g/m2):粉塵を払い落した後、差圧ΔPが
ある値に達するまでにフィルターに新しく堆積した粉塵
量、すなわちフィルターが新たに濾過した粉塵の質量。 である。
Here, dust load (g / m 2 ): total dust mass deposited on the filtration surface of the filter. Residual dust amount (g / m 2 ): Mass of dust remaining on the filter surface and inside even after the dust is blown off. Dust holding amount (g / m 2 ): The amount of dust newly deposited on the filter until the pressure reaches a certain value after the dust is blown off, that is, the mass of dust newly filtered by the filter. It is.

【0011】粉塵保持量という概念を導入することによ
って、バグフィルターの性能を従来よりも的確に評価す
ることが可能になるが、粉塵保持量を測定する装置は、
当然のことながら従来は存在しなかった。
By introducing the concept of the dust holding amount, the performance of the bag filter can be evaluated more accurately than before, but the device for measuring the dust holding amount is
Not surprisingly, it didn't exist before.

【0012】[0012]

【発明が解決しようとする課題】そこで本発明の目的
は、バグフィルターの粉塵保持量を自動的に測定するこ
とができる粉塵保持量測定装置を提供することにある。
SUMMARY OF THE INVENTION An object of the present invention is to provide a dust holding amount measuring device capable of automatically measuring the dust holding amount of a bag filter.

【0013】本発明の他の目的は、バグフィルターの粉
塵保持量の容易な測定を可能にすることによってバグフ
ィルターの新たな性能評価手段を提供し、バグフィルタ
ーとそれを用いる集塵および空気輸送の技術向上に貢献
することにある。
Another object of the present invention is to provide a new means for evaluating the performance of a bag filter by enabling easy measurement of the dust holding amount of the bag filter, and to provide a bag filter and dust collection and air transportation using the bag filter. To contribute to the technical improvement of.

【0014】[0014]

【課題を解決するための手段】上記目的を達成すること
に成功した本発明の粉塵保持量測定装置は、 試験用粉塵を一定の濃度で含有する被濾過空気を一
時貯留可能な空間を有する被濾過空気貯留室; 一定の濃度で浮遊粉塵を含有する被濾過空気を被濾
過空気貯留室に供給し滞留させる手段; 上下に配置された状態でバグフィルター試験片を挟持
する一対の環状部材からなり、被濾過空気貯留室の頂部
開口部と分離可能に連結された試験片取付部; 上記試験片取付部を構成する環状部材の上側のもの
と一体化され、等速空気吸引手段と連結され、且つ粉塵
払い落し用圧縮空気を室内に噴射する圧縮空気噴射ノズ
ルを装着された清浄空気室; 試験片取付部およびそれと一体の清浄空気室を回動
自在に支持し、且つそれらを上記被濾過空気貯留室の頂
部開口部と連結された状態から引き離し180度旋回さ
せて反転状態になし得る、旋回可能な試験片取付部支持
部材; 等速空気吸引手段による空気吸引に基づき被濾過空
気貯留室と清浄空気室との間に生じるフィルター差圧Δ
Pを測定する手段;および 上記差圧ΔPの経時的変化を記録し差圧ΔPが所定
の値になったとき等速空気吸引手段による空気吸引を中
止させ圧縮空気噴射ノズルより圧縮空気を噴射させる制
御装置;を有することを特徴とする。
A dust holding amount measuring apparatus of the present invention that has succeeded in achieving the above object has a space having a space capable of temporarily storing filtered air containing test dust at a constant concentration. Filtered air storage chamber; Means for supplying and retaining filtered air containing suspended dust at a constant concentration in the filtered air storage chamber; consisting of a pair of annular members for sandwiching the bag filter test piece in a vertically arranged state A test piece mounting portion that is separably connected to the top opening of the filtered air storage chamber; integrated with an upper side of the annular member that constitutes the test piece mounting portion, and is connected to constant velocity air suction means, Also, a clean air chamber equipped with a compressed air injection nozzle for injecting compressed air for dust removal into the room; rotatably supporting a test piece mounting portion and a clean air chamber integrated with the test piece mounting part, and supporting them with the air to be filtered. Storage A test piece mounting part supporting member that can be swung 180 degrees apart from the state where it is connected to the top opening of the swivel, and can be turned upside down; Filtered air storage chamber and clean air based on air suction by constant velocity air suction means Pressure difference Δ between filter and chamber
Means for measuring P; and recording the change over time of the differential pressure ΔP, and when the differential pressure ΔP reaches a predetermined value, the air suction by the constant velocity air suction means is stopped and compressed air is jetted from the compressed air jet nozzle. A control device;

【0015】この粉塵保持量測定装置は、本発明者が考
案した下記の原理による粉塵保持量測定法を実施するた
めのものである。
This dust holding amount measuring device is for carrying out a dust holding amount measuring method based on the following principle devised by the present inventor.

【0016】試験用濾過装置にバグフィルター試験片を
セットし、被濾過空気の粉塵濃度m(g/m3)を一定に保
ちつつ一定の濾過速度v(m/min)で吸引濾過を行なっ
た場合、t分間濾過を続けることによりフィルター差圧
がΔPtに達したとすると、該差圧ΔPtにおける粉塵保
持量M(g/m2)は式M=mvtで表される。したがっ
て、そのときの粉塵保持量Mは、濾過を中止して払い落
した粉塵を秤量しなくても経過時間tから計算すること
ができる(粉塵濃度mおよび濾過速度vは最初に設定さ
れた濾過条件であるから一定である)。
A bag filter test piece was set in a test filtration device, and suction filtration was performed at a constant filtration rate v (m / min) while keeping the dust concentration m (g / m 3 ) of the air to be filtered constant. In this case, if the filter pressure difference reaches ΔP t by continuing the filtration for t minutes, the dust holding amount M (g / m 2 ) at the pressure difference ΔP t is expressed by the equation M = mvt. Therefore, the dust holding amount M at that time can be calculated from the elapsed time t without stopping the filtration and weighing the dust that has been shaken off (the dust concentration m and the filtration speed v are set to the initially set filtration). It is constant because it is a condition).

【0017】なお、濾過速度vは吸引されて試験片を通
過する空気の線速度であって、濾過面積をS(m2)、単
位時間当たりの吸引空気量をQ(m3/min)とすればv=
Q/Sである。
The filtration speed v is the linear velocity of air that is sucked and passes through the test piece, where the filtration area is S (m 2 ), and the amount of suction air per unit time is Q (m 3 / min). Then v =
Q / S.

【0018】[0018]

【発明の実施の形態】次に、本発明による粉塵保持量測
定装置の構成を具体例について図面を参照しながら詳細
に説明する。
BEST MODE FOR CARRYING OUT THE INVENTION Next, the structure of a dust holding amount measuring device according to the present invention will be described in detail with reference to the drawings with reference to specific examples.

【0019】本発明による測定装置の典型的な例は、図
1に示したように、濾過器である本体部分1、差圧ΔP
の測定・記録装置、シーケンシャルコントローラー、等
速吸引装置、圧縮空気供給源2等を要部とする。
A typical example of the measuring device according to the present invention is, as shown in FIG. 1, a main body portion 1 which is a filter and a differential pressure ΔP.
The measurement / recording device, the sequential controller, the constant velocity suction device, the compressed air supply source 2 and the like are the main parts.

【0020】本体部分1は、図2,3に示したように、
試験片取付部3、清浄空気室4、被濾過空気貯留室5、
および浮遊粉塵発生装置6が主要構成部材である。
The main body portion 1 is, as shown in FIGS.
Test piece attachment part 3, clean air chamber 4, filtered air storage chamber 5,
The floating dust generator 6 is a main constituent member.

【0021】試験片取付部3は、試験片Sを挟持させる
一対の環状部材7,8、環状部材7,8を連結するヒン
ジ9、および環状部材7,8のための締付け金具10
(全部で4個ある)等からなる。上側の環状部材8に
は、試験片Sに作用する吸引圧を均一化するとともに後
述する払い落しのための空気噴射を行うのに必要な空間
を持つ清浄空気室4が固定されている。
The test piece mounting portion 3 includes a pair of annular members 7 and 8 for holding the test piece S, a hinge 9 for connecting the annular members 7 and 8, and a fastening metal fitting 10 for the annular members 7 and 8.
(There are 4 in total) and so on. On the upper annular member 8, a clean air chamber 4 having a space required to equalize the suction pressure acting on the test piece S and to perform an air jet for the later-described blow-off is fixed.

【0022】この清浄空気室4は、回動自在の排気管1
1およびホース(図示せず)により、等速吸引装置(真
空ポンプ、回転数制御装置付きターボブロワー等を用い
ることができる)と連結されている。また、その頂部に
圧縮空気噴射ノズル12およびそのための圧縮空気源2
との接続管13が回動自在に装着されていて、該噴射ノ
ズル12は、試験片取付部3に取り付けられた試験片S
に向かって圧縮空気を放射状に噴射可能である。
The clean air chamber 4 includes a rotatable exhaust pipe 1
1 and a hose (not shown) are connected to a constant velocity suction device (a vacuum pump, a turbo blower with a rotation speed control device, or the like can be used). Further, a compressed air injection nozzle 12 and a compressed air source 2 therefor are provided on the top thereof.
A connecting pipe 13 for connecting the test piece S to the test piece S mounted on the test piece mounting portion 3 is rotatably mounted.
It is possible to radially inject compressed air toward.

【0023】清浄空気室4の内部には、さらに一対の試
験片支持部材50が装着されているが、これについては
後に詳述する。
A pair of test piece support members 50 are further mounted inside the clean air chamber 4, which will be described later in detail.

【0024】試験片取付部3および清浄空気室4は、図
示した測定状態では、ベースプレート14から直立する
円筒状部材15(先端に環状部材7,8と同径の環状座
体16が固定されている)の上に置かれるが、これとは
別に、ベースプレート14上の支柱17の先端にある支
軸18を旋回軸とするレバー19(図2の背面側にも同
じものがあり対になっている)によって回動自在に支持
されている。すなわち、清浄空気室4の側面から突出す
る軸20がレバー19の中間位置にある穴に緩く嵌合し
ており、レバー19を旋回させると試験片取付部3およ
び清浄空気室4は環状座体16から引き離されてレバー
19だけで支持され、かつ回動自在の状態になる。
In the measurement state shown in the drawing, the test piece mounting portion 3 and the clean air chamber 4 have a cylindrical member 15 which stands upright from the base plate 14 (an annular seat 16 having the same diameter as the annular members 7 and 8 is fixed to the tip end thereof). However, apart from this, there is a lever 19 having a support shaft 18 at the tip of the column 17 on the base plate 14 as a pivot shaft (there are the same on the rear side of FIG. It is rotatably supported by. That is, the shaft 20 protruding from the side surface of the clean air chamber 4 is loosely fitted in the hole at the intermediate position of the lever 19, and when the lever 19 is swung, the test piece mounting portion 3 and the clean air chamber 4 are separated from each other by the annular seat body. It is separated from 16, is supported only by the lever 19, and is in a rotatable state.

【0025】試験片取付部支持部材であるレバー19
は、図2において時計針方向に180度の旋回が可能で
あって、限界まで旋回させると、清浄空気室4および試
験片取付部3を横方向に移動させた上で反転状態にする
ことができる(反転状態を図2に2点鎖線で示した。レ
バー19のそれ以上の旋回はストッパー21で阻止され
る)。
Lever 19 which is a support member for the test piece mounting portion
2 is capable of turning 180 degrees in the clockwise direction in FIG. 2, and when turned to the limit, the clean air chamber 4 and the test piece attachment portion 3 can be moved laterally and then turned to the inverted state. It is possible (the inverted state is shown by a chain double-dashed line in FIG. 2. Further turning of the lever 19 is blocked by the stopper 21).

【0026】レバー19は上述の機構により清浄空気室
4を支持すると共に先端にあるU字形掛合部材22が締
付け金具23(支軸24によりベースプレート14に旋
回可能に取り付けられたボルト25およびナット26か
らなる)に掛合するようになっていて、掛合状態にした
締付け金具23を締め付けて図2で反時計針方向に押圧
する力をレバー19に加えると、軸20を介して清浄空
気室4および試験片取付部3を下方に押圧し、環状座体
16に密着させることができる。
The lever 19 supports the clean air chamber 4 by the above-mentioned mechanism, and the U-shaped engaging member 22 at the tip is provided with a tightening fitting 23 (a bolt 25 and a nut 26 pivotably attached to the base plate 14 by a support shaft 24). 2), the tightening metal fitting 23 in the engaged state is tightened, and when a force for pressing in the counterclockwise direction in FIG. 2 is applied to the lever 19, the clean air chamber 4 and the test are performed via the shaft 20. The one-sided mounting portion 3 can be pressed downward to be brought into close contact with the annular seat body 16.

【0027】なお、環状部材7の下面には、上記締め付
け状態で環状部材7と環状座体16との間を気密状態に
するためのゴム製Oリング28を固着してある。また、
清浄空気室4と円筒状部材15には差圧検出用チューブ
接続口29,30が設けられていて、これらをチューブ
で差圧ΔP測定・記録装置と接続することにより差圧Δ
Pを常時測定し記録することができるようになってい
る。
A rubber O-ring 28 is fixed to the lower surface of the annular member 7 to keep the annular member 7 and the annular seat body 16 in an airtight state in the tightened state. Also,
The clean air chamber 4 and the cylindrical member 15 are provided with differential pressure detection tube connection ports 29 and 30. By connecting these to the differential pressure ΔP measuring / recording device with a tube, the differential pressure Δ
P can be constantly measured and recorded.

【0028】円筒状部材15の直下には、装置全体を支
持するフレーム31に固定された被濾過空気貯留室5が
あるが、被濾過空気貯留室5の振動が試験片取付部3に
伝わって試験片の濾過性能に影響するのを防止するた
め、被濾過空気貯留室5の頂部の開口部と円筒状部材1
5とは直結せず、可撓性材料からなる短いホース32を
介在させてある(ベースプレート14も、振動防止のた
めのゴム製緩衝材33を介在させて被濾過空気貯留室5
の天井部に取付られている。)。
Immediately below the cylindrical member 15, there is a filtered air storage chamber 5 fixed to a frame 31 that supports the entire apparatus. The vibration of the filtered air storage chamber 5 is transmitted to the test piece mounting portion 3. In order to prevent the filtration performance of the test piece from being affected, the opening at the top of the filtered air storage chamber 5 and the cylindrical member 1
5 is not directly connected, but a short hose 32 made of a flexible material is interposed (the base plate 14 is also provided with a rubber cushioning material 33 for preventing vibration, and the filtered air storage chamber 5
It is attached to the ceiling of. ).

【0029】被濾過空気貯留室5は、対向する一対の壁
35,36が断面漏斗状に傾斜しており、それにより長
方形になっている下端開口部に浮遊粉塵発生装置6が装
着されている。
In the filtered air storage chamber 5, a pair of opposing walls 35 and 36 are inclined in a funnel-shaped cross section, and a floating dust generating device 6 is attached to the rectangular lower end opening. .

【0030】浮遊粉塵発生装置6の詳細を図4および図
5により説明すると、スクリューコンベヤ37が樋状の
粉塵貯留部38に設置されており、粉塵貯留部38に蓄
えられている粉塵Dを少しずつ、図5で左方向に送って
粉塵分散装置に供給するようになっている。スクリュー
コンベヤ37は、粉塵の詰まりを防止するため基本的に
コイルスプリング37aを用いたものにしてあり、その
ため、粉塵送りが間欠的またはそれに近いものになる
が、スパイラルギヤ状に多数の羽根を持つアジャストス
クリュー39をコイルスプリング37aの先端から少し
離して装着し、且つ、コイルスプリング37a部分によ
る粉塵送りが一時的に途絶える(または減少する)コイ
ルスプリング先端A部分に対向する部分において、アジ
ャストスクリュー39の羽根39aを上記A部分方向に
突き出させて粉塵取り込み量を多くすることにより、粉
塵の定量供給を可能にしている。
The details of the floating dust generator 6 will be described with reference to FIGS. 4 and 5. The screw conveyor 37 is installed in the gutter-shaped dust storage section 38, and the dust D stored in the dust storage section 38 is slightly discharged. Each of them is fed to the left in FIG. 5 to be supplied to the dust dispersion device. The screw conveyor 37 basically uses a coil spring 37a to prevent clogging of dust. Therefore, dust feeding is intermittent or close to that, but has a large number of blades in a spiral gear shape. The adjust screw 39 is mounted at a distance from the tip of the coil spring 37a, and the dust feed by the coil spring 37a portion is temporarily interrupted (or reduced) at a portion opposite to the coil spring tip A portion. The blade 39a is protruded in the direction of the portion A to increase the amount of dust taken in, thereby making it possible to supply a fixed amount of dust.

【0031】粉塵分散装置は、合成樹脂(たとえばナイ
ロン)の剛毛や金属線が多数放射状に植設されてなる回
転ブラシ40と、そのほぼ下半分と接するように形成さ
れたケーシング41、および回転ブラシ40の真上に、
ケーシング41内を2分するように回転ブラシ40の軸
と平行に設置された仕切り板55からなる。回転ブラシ
40をモータMで回転させ、回転する回転ブラシ40の
周面がケーシング41内に入り込む部分(図4で右半分
の部分)にスクリューコンベヤ37の先端から粉塵Dを
落としこみ、粉塵Dに強い剪断力を作用させて凝集粒子
を解砕し、解砕された粉塵を反対側から上方に飛散させ
るものである。さらに、必要に応じて回転ブラシ40の
周辺部接線方向に圧縮空気を吹き込むためのエアノズル
42が、ケーシング41の粉塵落下部直下に開口してい
る。
The dust disperser comprises a rotary brush 40 having a large number of synthetic resin (for example, nylon) bristles and metal wires radially implanted, a casing 41 formed so as to be in contact with substantially the lower half thereof, and a rotary brush. Just above 40,
The partition plate 55 is installed parallel to the axis of the rotating brush 40 so as to divide the inside of the casing 41 into two parts. The rotating brush 40 is rotated by the motor M, and the dust D is dropped from the tip of the screw conveyor 37 into the portion (the right half portion in FIG. 4) where the peripheral surface of the rotating rotating brush 40 enters the casing 41, and becomes the dust D. A strong shearing force is applied to crush aggregated particles, and the crushed dust is scattered upward from the opposite side. Further, an air nozzle 42 for blowing compressed air in the tangential direction of the peripheral portion of the rotary brush 40 is opened immediately below the dust dropping portion of the casing 41 as needed.

【0032】仕切り板55で仕切られたケーシング41
内の空間は、回転ブラシ40とモータMとの間のケーシ
ング壁の延長として被濾過空気貯留室5内に立つ衝立状
の壁56と被濾過空気貯留室5の垂直壁57で形成され
た扁平空間を経由して被濾過空気貯留室5内の空間に通
じており、該扁平空間も、仕切り板55の延長である仕
切り板55aで2分されている。
Casing 41 partitioned by a partition plate 55
The inner space is a flat wall formed by a partition wall 56 standing in the filtered air storage chamber 5 as an extension of the casing wall between the rotary brush 40 and the motor M and a vertical wall 57 of the filtered air storage chamber 5. The space communicates with the space inside the filtered air storage chamber 5, and the flat space is also divided into two parts by a partition plate 55 a which is an extension of the partition plate 55.

【0033】被濾過空気貯留室5の天井部の一隅(前記
円筒状部材15が固定されている位置の横;図2では背
面側)には、図1に略図で示した粉塵フィルター付きの
通気孔45が設けられている。すなわち、底部が被濾過
空気貯留室5に向かって解放されているフィルター装着
室46内に大きな濾過面積を持つ粉塵フィルター(バグ
フィルター)47があって、該粉塵フィルター47の外
面は被濾過空気貯留室5内の被濾過空気と接し、内側は
排気ファン48および通気孔45を経由して外気に通じ
ている。通気経路にシャッターはない。なお、排気ファ
ン48は粉塵貯留部38に試験用粉塵を投入するときな
どに作動させて粉塵が飛散するのを防止するためのもの
であり、本発明の装置に必須のものではない。
At one corner of the ceiling portion of the filtered air storage chamber 5 (side of the position where the cylindrical member 15 is fixed; rear side in FIG. 2), there is a passage with a dust filter, which is schematically shown in FIG. Pores 45 are provided. That is, there is a dust filter (bug filter) 47 having a large filtration area in the filter mounting chamber 46 whose bottom is opened toward the filtered air storage chamber 5, and the outer surface of the dust filter 47 is the filtered air storage chamber. In contact with the air to be filtered in the chamber 5, the inside communicates with the outside air via the exhaust fan 48 and the ventilation hole 45. There is no shutter in the ventilation path. The exhaust fan 48 is provided to prevent dust from scattering by operating when the test dust is put into the dust reservoir 38, and is not essential to the device of the present invention.

【0034】次にこの装置の使用方法を説明する。最初
にバグフィルターの試験片Sを試験片取付部3にセット
するが、その場合は、図2に実線で示した測定状態から
レバー19先端のU字形掛合部材22と締付け金具23
との掛合を解除し、レバー19を時計針方向に180度
旋回させる。レバー19によって回動可能に支持された
清浄空気室4およびそれと一体の試験片取付部3は上下
を反転させ、試験片取付部3が上を向いた鎖線表示の状
態にする。この状態で、締付け金具10による環状部材
7,8の締付けを解除し、ヒンジ9を利用して環状部材
7を(図2では紙面奥方向に)旋回させることにより、
試験片取付部3の環状部材7−8間が開いた状態にす
る。次いで環状部材7,8に挟持させるのに適当な大き
さに裁断した試験片Sを環状部材8上に置き、環状部材
7を原位置に復帰させて締付け金具10を締めると、環
状部材7,8間に試験片Sが気密に挟持される。
Next, a method of using this device will be described. First, the test piece S of the bag filter is set on the test piece mounting portion 3. In that case, from the measurement state shown by the solid line in FIG.
And the lever 19 is turned 180 degrees clockwise. The clean air chamber 4 rotatably supported by the lever 19 and the test piece mounting portion 3 integrated with the clean air chamber 4 are turned upside down, so that the test piece mounting portion 3 is in a state shown by a chain line pointing upward. In this state, the tightening of the annular members 7, 8 by the tightening metal fitting 10 is released, and the annular member 7 is swung (in the direction toward the back of the paper in FIG. 2) by using the hinge 9,
The annular member 7-8 of the test piece attachment portion 3 is opened. Next, the test piece S cut into a size suitable for being sandwiched by the annular members 7 and 8 is placed on the annular member 8, the annular member 7 is returned to the original position, and the tightening fitting 10 is tightened. The test piece S is hermetically sandwiched between the eight.

【0035】なお、上述のように清浄空気室4を反転さ
せて行う試験片取付け操作中は、図3に鎖線で表示した
位置に旋回する試験片支持部材50の先端50aが試験
片Sの中央部付近を支えて、試験片Sが弛むのを防止す
る(試験片支持部材50とその支持機構を図6も参照し
ながら説明すると、この部材はほぼT字状に曲げ加工さ
れた鋼線からなり、それよりも十分重い鋼板製のバラン
スウェイト51に脚部50bにおいて固定されている。
バランスウェイト51は、清浄空気室4の壁から清浄空
気室4の中心に向かって立つ支柱52の先端に、支軸5
3により、垂直面内で回動可能なように支持されてい
る。試験片支持部材50は、その直線的な先端50aの
部分がバランスウェイト51を含む平面と直交するよう
な配置でバランスウェイト51に固定されているから、
バランスウェイト51が回動しても、先端50aは常に
試験片Sと平行な状態にある。バランスウェイト51
は、支軸53による支持位置Oが重心Gから離れている
ことにより生じる回転モーメントによって回動するが、
回動方向は清浄空気室4の姿勢によって反転し、且つ回
動可能範囲はa部またはb部が清浄空気室4の壁面に当
接することにより制限される。清浄空気室4が反転して
いる試験片取付け時は、上記回転モーメントがバランス
ウェイト51をそのa部が清浄空気室4の壁面に当接す
る方向に回動させ、当接後もその状態を維持させる。そ
の状態で、バランスウェイト51は試験片支持部材50
をその先端50aが試験片Sとほぼ接する鎖線表示の位
置に保持して、取付ける試験片に弛みが生じるのを防
ぐ。清浄空気室4が図3のように正立状態にある測定時
は、b部が清浄空気室4の壁面に当接する方向にバラン
スウェイト51が回動し、先端50aは試験片Sから十
分離れた位置にあるから、濾過試験に影響を及ぼすこと
はない。試験片支持部材およびバランスウェイトの形状
や材料は、上述のような自動的試験片支持と退避が可能
な範囲で任意に変更可能であることは言うまでもな
い。)。
During the test piece mounting operation performed by reversing the clean air chamber 4 as described above, the tip 50a of the test piece support member 50 that swivels to the position shown by the chain line in FIG. The test piece S is supported by supporting the vicinity of the portion to prevent the test piece S from loosening. (The test piece supporting member 50 and its supporting mechanism will be described with reference to FIG. 6 as well. This member is made of a steel wire bent into a substantially T shape. And is fixed to the balance weight 51 made of a steel plate which is heavier than that in the leg portion 50b.
The balance weight 51 is attached to the tip of the support column 52 standing from the wall of the clean air chamber 4 toward the center of the clean air chamber 4, and the support shaft 5 is attached.
It is supported by 3 so as to be rotatable in a vertical plane. The test piece support member 50 is fixed to the balance weight 51 in such an arrangement that the linear tip portion 50a thereof is orthogonal to the plane including the balance weight 51.
Even if the balance weight 51 rotates, the tip 50a is always parallel to the test piece S. Balance weight 51
Rotates due to the rotation moment generated when the support position O by the support shaft 53 is separated from the center of gravity G,
The rotating direction is reversed depending on the posture of the clean air chamber 4, and the rotatable range is limited by the a portion or the b portion contacting the wall surface of the clean air chamber 4. When the test piece is mounted with the clean air chamber 4 inverted, the above-mentioned rotational moment causes the balance weight 51 to rotate in the direction in which the portion a of the balance weight abuts against the wall surface of the clean air chamber 4, and the state is maintained even after the abutment. Let In that state, the balance weight 51 becomes the test piece support member 50.
Is held at a position indicated by a chain line where its tip 50a is almost in contact with the test piece S to prevent the test piece to be attached from being loosened. At the time of measurement when the clean air chamber 4 is in the upright state as shown in FIG. 3, the balance weight 51 rotates in the direction in which the portion b contacts the wall surface of the clean air chamber 4, and the tip 50a is sufficiently separated from the test piece S. It does not affect the filtration test because it is in the open position. It goes without saying that the shapes and materials of the test piece support member and the balance weight can be arbitrarily changed within the range in which the automatic test piece support and the withdrawal as described above are possible. ).

【0036】一方、粉塵貯留部38には粉塵D(試験用
標準粉体)を適量入れておく(後述する濾過試験の吸引
サイクル中も粉塵の一部がこの貯留部38に残っている
必要がある。)。
On the other hand, an appropriate amount of dust D (standard powder for testing) is put in the dust storage section 38 (a part of the dust needs to remain in the storage section 38 even during the suction cycle of the filtration test described later). is there.).

【0037】次いでレバー19を旋回させてレバー19
および試験片取付部3を原位置に復帰させる。締付け金
具23を締め付けると、試験片取付部3の環状部材7,
8が環状座体16に密着し、図2の測定可能状態にな
る。
Then, the lever 19 is rotated to move the lever 19
And the test piece attachment part 3 is returned to the original position. When the tightening fitting 23 is tightened, the annular member 7 of the test piece mounting portion 3
8 comes into close contact with the annular seat body 16 and becomes in the measurable state of FIG.

【0038】その後、等速吸引装置と浮遊粉塵発生装置
6を作動させると、一定の濾過速度v(m/min)で、被
濾過空気貯留室5内の空気の濾過が始まる。浮遊粉塵発
生装置6においては、スクリューコンベヤ37で定量供
給された粉塵Dが回転ブラシ40の回転に巻き込まれ、
凝集粒子は強い剪断力を受けて解砕された後、高速で上
方に飛散する。このとき、図4において時計針方向に回
転する回転ブラシ40がブロワの作用をして、被濾過空
気貯留室5からダクト状部分58経由でケーシング41
内に入りダクト状部分59に放出される気流を発生させ
るので、上記解砕された粉塵はこの気流に乗ってダクト
状部分59を上昇し、被濾過空気貯留室5の上部空間に
放出される。このようにして、回転ブラシ40が発生す
る気流は粉塵を被濾過空気貯留室5内に搬送すると同時
に該室内の空気を撹拌して粉塵濃度を均一化する。な
お、エアノズル42から空気噴射を行うと、上記回転ブ
ラシ40の回転による粉塵分散を助けると共に粉塵量が
多いとき回転ブラシ40駆動用モータMの負荷を軽減す
るのに役立つ。
After that, when the constant velocity suction device and the suspended dust generating device 6 are operated, the filtration of the air in the filtered air storage chamber 5 starts at a constant filtration speed v (m / min). In the floating dust generator 6, the dust D supplied in a fixed amount by the screw conveyor 37 is caught in the rotation of the rotating brush 40,
The agglomerated particles are crushed by a strong shearing force, and then scattered upward at a high speed. At this time, the rotating brush 40 rotating in the clockwise direction in FIG. 4 acts as a blower, and the casing 41 passes from the filtered air storage chamber 5 via the duct-shaped portion 58.
Since the airflow that enters inside and is discharged to the duct-shaped portion 59 is generated, the crushed dust rides on this airflow to rise in the duct-shaped portion 59 and is discharged to the upper space of the filtered air storage chamber 5. . In this way, the air flow generated by the rotating brush 40 conveys the dust into the filtered air storage chamber 5 and at the same time agitates the air in the chamber to homogenize the dust concentration. The air injection from the air nozzle 42 helps to disperse the dust due to the rotation of the rotary brush 40 and to reduce the load of the rotary brush 40 driving motor M when the dust amount is large.

【0039】粉塵分散装置付属のエアノズル42から空
気噴射を行わない場合、またはエアノズル42からの空
気噴射を行なう場合でも単位時間当たりの噴射空気量が
試験片S経由で吸引される空気量よりも少ないとき、被
濾過空気貯留室5への空気の補給は僅かに負圧になった
被濾過空気貯留室5内に通気孔45から粉塵フィルター
47経由で装置外空気が流入することにより自動的に行
われる。このとき粉塵フィルター47による通気抵抗が
大きいと差圧ΔPの測定値に影響するので、粉塵フィル
ター47の濾過面積は試験片Sのそれよりも十分大きく
してある。
Even when air is not jetted from the air nozzle 42 attached to the dust dispersing device, or even when air is jetted from the air nozzle 42, the amount of jetted air per unit time is smaller than the amount of air sucked through the test piece S. At this time, the supply of air to the filtered air storage chamber 5 is automatically performed by the outside air of the device flowing from the ventilation hole 45 through the dust filter 47 into the filtered air storage chamber 5 having a slightly negative pressure. Be seen. At this time, if the ventilation resistance of the dust filter 47 is large, it affects the measured value of the differential pressure ΔP, so the filtration area of the dust filter 47 is made sufficiently larger than that of the test piece S.

【0040】また、試験片S経由で吸引される空気量よ
りも多量の空気をエアノズル42から噴射したときは、
被濾過空気貯留室5内の過剰空気が粉塵フィルター47
を経由して通気孔45から装置外に放出され、室内が加
圧状態になるのが防止される(排気ファン48は作動さ
せない)。このとき、放出された空気に含まれていた粉
塵は粉塵フィルター47に捕集される。
When a larger amount of air than the amount of air sucked through the test piece S is jetted from the air nozzle 42,
Excess air in the filtered air storage chamber 5 causes dust filter 47
The air is discharged from the ventilation hole 45 to the outside of the device via the air vent, and the pressure in the room is prevented (the exhaust fan 48 is not operated). At this time, the dust contained in the released air is collected by the dust filter 47.

【0041】上述のようにして、被濾過空気貯留室5内
は試験中ほぼ大気圧に維持され、且つ粉塵濃度m(g/
m3)は一定に保たれる。ただし、上述のようにして粉塵
が循環する被濾過空気貯留室5内の粉塵濃度は、平均す
れば一定でも、場所による若干の濃度ムラがあり得る。
しかし、この濃度ムラも、被濾過空気がホース32と円
筒状部材15からなる円筒状部分をゆっくり上昇して試
験片に達する間に解消する。つまり、上記円筒状部分は
被濾過空気の粉塵濃度を均一化し且つ気流を試験片方向
のみに向かうものに整流する調整空間の役割もしてい
る。
As described above, the inside of the filtered air storage chamber 5 is maintained at about atmospheric pressure during the test, and the dust concentration m (g / g / g
m 3 ) is kept constant. However, even if the dust concentration in the filtered air storage chamber 5 in which the dust circulates as described above is constant on average, there may be some concentration unevenness depending on the location.
However, this concentration unevenness is also eliminated while the air to be filtered slowly rises in the cylindrical portion composed of the hose 32 and the cylindrical member 15 and reaches the test piece. That is, the cylindrical portion also serves as an adjusting space for making the dust concentration of the filtered air uniform and rectifying the air flow only toward the test piece.

【0042】濾過開始と同時にフィルター差圧ΔPが生
じるので、それを、差圧検出用チューブ接続口29,3
0に接続された差圧ΔP測定・記録装置により常時測定
し、記録する。粉塵蓄積量が増すに伴い上昇する差圧Δ
Pがあらかじめ設定された値(たとえば150mmH2O)
に達したならば、等速吸引装置による空気吸引を中止
し、スクリューコンベヤ37および回転ブラシ40も停
止させる。次いで、圧縮空気噴射ノズル12から試験片
Sに向かって圧縮空気を短時間噴射させて試験片Sに衝
撃を与え、付着した粉塵を払い落す。
A filter differential pressure ΔP is generated at the same time as the start of filtration.
A differential pressure ΔP measuring / recording device connected to 0 is constantly measured and recorded. Differential pressure Δ that increases as the amount of accumulated dust increases
P is a preset value (eg 150 mmH 2 O)
When the value reaches, the air suction by the constant velocity suction device is stopped, and the screw conveyor 37 and the rotating brush 40 are also stopped. Next, compressed air is jetted from the compressed air jet nozzle 12 toward the test piece S for a short time to give a shock to the test piece S, and the adhered dust is blown off.

【0043】粉塵払い落し過程で試験片Sから払い落さ
れた粉塵は、一部は直接、大部分は被濾過空気貯留室5
の断面漏斗状の側壁35,36に衝突したのち、粉塵貯
留部38まで落下し、被濾過空気の調製に再利用され
る。また、粉塵フィルター47上の粉塵が多くなったと
きは、濾過休止期間中に、振動付与装置53により該フ
ィルターに振動を与えて付着粉塵を払い落す(それによ
り払い落された粉塵も粉塵貯留部38に落下する)。こ
れらにより、試験用粉塵は試験片Sから漏れるもの以外
はすべて装置内で循環することになる。
The dust blown off from the test piece S during the dust blow-off process is partly directly, and most of the dust is the filtered air storage chamber 5.
After colliding with the side walls 35 and 36 having a funnel-shaped cross section, it falls to the dust storing section 38 and is reused for preparing the air to be filtered. Further, when the amount of dust on the dust filter 47 increases, the vibration imparting device 53 vibrates the filter to remove the adhered dust during the suspension period of filtration (the dust thus removed is also the dust storage unit). 38). As a result, all the test dust except the one leaking from the test piece S circulates in the apparatus.

【0044】上記の濾過−濾過中止−払い落しを、ベー
ス圧損が安定するのに十分なサイクル数(通常数百
回)、シーケンシャルコントローラーにより自動的に反
復させる。図7はその一例のタイムチャートである。
The above-mentioned filtration-suspension of filtration-shuffling is automatically repeated by a sequential controller for a sufficient number of cycles (usually several hundreds) to stabilize the base pressure loss. FIG. 7 is a time chart of an example thereof.

【0045】前述の式M=mvtを用いれば、試験片S
を装置にセットしたままで、各サイクルにおける粉塵保
持量Mを求めることができ、また、その経時的変化を知
ることができる。なお、このときの粉塵濃度mは、次の
方法で実測することができる。まず、最初の(または初
期の任意の)サイクルにおける濾過だけが終った後、払
い落しのための圧縮空気噴射を行うことなく全装置の作
動を停止し、等速吸引装置による空気吸引を行いなが
ら、試験片取付部3を前述の試験片取付けの際と同様に
して反転状態にする。試験片上の堆積粉塵は空気吸引に
より試験片に引き付けられた状態に保たれるので、反転
操作によって剥がれ落ちることはない。反転状態になっ
た後は、粉塵付着面が上を向いていて粉塵剥落のおそれ
はないから、空気吸引を停止して試験片Sを試験片取付
部3から外す。外した粉塵付き試験片Sの質量を測定
し、試験片S自身の質量との差として粉塵負荷を求め
る。
Using the above equation M = mvt, the test piece S
The dust holding amount M in each cycle can be obtained with the device set in the apparatus, and its change over time can be known. The dust concentration m at this time can be measured by the following method. First, after only the filtration in the first (or any of the initial) cycles is completed, the operation of all the devices is stopped without performing the compressed air injection for blow-off, and the air is sucked by the constant velocity suction device. The test piece mounting portion 3 is turned over in the same manner as when mounting the test piece. The accumulated dust on the test piece is kept attracted to the test piece by air suction, so it does not come off due to the reversing operation. After the reversal state, since the dust adhering surface faces upward and there is no possibility of dust falling off, the air suction is stopped and the test piece S is removed from the test piece mounting portion 3. The mass of the removed test piece S with dust is measured, and the dust load is obtained as a difference from the mass of the test piece S itself.

【0046】次いで粉塵付き試験片Sを再び試験片取付
部3に取付け、試験片取付部3を測定状態に復帰させた
のち、噴射ノズル12から圧縮空気を噴射して付着粉塵
の払い落しを行う。払い落しを終わった試験片Sについ
て(望ましくは差圧ΔPが設定値に達するまでの濾過と
払い落しを行なった試験片Sについて)、上記粉塵負荷
の測定の場合と同様にして試験片取付部3からの取り外
しと質量測定を行い、残留粉塵量を求める。上述のよう
にして測定された粉塵負荷と残留粉塵量の差として粉塵
保持量Mを求め、m=M/vtの関係式を用いて粉塵濃
度mを求める。
Then, the test piece S with dust is attached to the test piece mounting portion 3 again, the test piece mounting portion 3 is returned to the measurement state, and then compressed air is jetted from the jet nozzle 12 to remove the attached dust. . For the test piece S that has been removed (preferably, for the test piece S that has been filtered and blown off until the differential pressure ΔP reaches the set value), the test piece attachment part is the same as in the case of measuring the dust load. Remove from 3 and perform mass measurement to obtain the amount of residual dust. The dust holding amount M is obtained as the difference between the dust load measured as described above and the residual dust amount, and the dust concentration m is obtained using the relational expression of m = M / vt.

【0047】ベース圧損が安定するまで濾過−濾過中止
−払い落しを繰り返した後に堆積している粉塵の量を実
測したり付着状態を観察したりする必要がある場合も、
上記と同様にして粉塵を付着させたまま試験片Sを取り
外し、必要な観察や測定を行うことができる。
Even when it is necessary to actually measure the amount of dust accumulated or observe the adhered state after repeating filtration-stopping filtration-shuffling until the base pressure loss becomes stable,
In the same manner as above, the test piece S can be removed with the dust adhering thereto, and necessary observation and measurement can be performed.

【0048】[0048]

【発明の効果】上述のように、本発明によればバグフィ
ルターの粉塵保持量を自動的に測定することが可能にな
り、粉塵保持量以外の性能値の測定や粉塵付着状態の観
察も容易になるから、バグフィルターとそれを用いる集
塵装置および空気輸送装置の設計を従来よりも合理的に
行うことが可能になる。
As described above, according to the present invention, it becomes possible to automatically measure the dust retention amount of the bag filter, and it is easy to measure the performance value other than the dust retention amount and observe the dust adhesion state. Therefore, it becomes possible to more rationally design the bag filter and the dust collecting device and the air transportation device using the bag filter.

【0049】また、濾過試験装置においては測定中粉塵
濃度を一定に保たれることが重要であるが、前記実施例
の装置では、被濾過空気貯留室と一体の粉塵分散装置を
設け、被濾過空気貯留室には粉塵フィルター付き通気孔
を設けて、そこで粉塵を一定濃度で含有する被濾過空気
を継続的に発生させるようにしたので、技術的に困難な
粉塵濃度の安定化が達成されているだけでなく、高価な
濾過試験用粉体が装置内で完全に循環利用されるという
特長がある。
Further, it is important to keep the dust concentration constant during the measurement in the filtration test device, but in the device of the above-mentioned embodiment, a dust dispersion device integrated with the air storage chamber to be filtered is provided to A ventilation hole with a dust filter was provided in the air storage chamber to continuously generate filtered air containing dust at a constant concentration, so that technically difficult dust concentration stabilization was achieved. Not only that, it has the advantage that expensive filtration test powder is completely recycled in the equipment.

【0050】さらに、清浄空気室内に試験片支持部材を
設けた構造は、試験片が柔らかい場合も弛みなく取り付
けることを可能にし、また、試験片取付部を(したがっ
て試験片を)大口径のものにして精度の高い試験を行う
ことを可能にする。
Further, the structure in which the test piece support member is provided in the clean air chamber enables the test piece to be attached without slack even when the test piece is soft, and the test piece attachment portion (and hence the test piece) has a large diameter. Therefore, it is possible to perform a highly accurate test.

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

【図1】 本発明による測定装置の構成の概要を示す説
明図である。
FIG. 1 is an explanatory diagram showing an outline of the configuration of a measuring apparatus according to the present invention.

【図2】 図1の測定装置の本体部分1を示す正面図で
ある。
FIG. 2 is a front view showing a main body portion 1 of the measuring apparatus of FIG.

【図3】 図1の本体部分1の上半部を示す一部破断左
側面図である。
3 is a partially cutaway left side view showing an upper half portion of a main body portion 1 of FIG. 1. FIG.

【図4】 図1の本体部分1の浮遊粉塵発生装置6の一
部破断正面図である。
FIG. 4 is a partially cutaway front view of the floating dust generator 6 of the main body portion 1 of FIG.

【図5】 上記浮遊粉塵発生装置6の一部破断右側面図
である。
5 is a partially cutaway right side view of the floating dust generator 6. FIG.

【図6】 図3の試験片支持部材50およびバランスウ
ェイト51を示し、A図は図3と同じ方向から見た図、
B図はその左側面図である。
6 shows the test piece support member 50 and balance weight 51 of FIG. 3, FIG. 6A being a view seen from the same direction as FIG.
Figure B is a left side view thereof.

【図7】 図1の測定装置による濾過試験の一例のタイ
ムチャートである。
7 is a time chart of an example of a filtration test by the measuring device of FIG.

【符号の説明】[Explanation of symbols]

1:本体部分 2:圧縮空気供給源 3:試験片取付部 4:清浄空気室 5:被濾過空気貯留室 6:浮遊粉塵発生装置 7,8:環状部材 12:圧縮空気噴射ノズル 19:レバー(試験片取付部支持部材) 29,30:差圧検出用チューブ接続口 37:スクリューコンベヤ 38:粉塵貯留部 39:アジャストスクリュー 40:回転ブラシ 45:通気孔 47:粉塵フィルター 50:試験片支持部材 51:バランスウェイト S:試験片 1: Main body part 2: Compressed air supply source 3: Test piece mounting part 4: Clean air chamber 5: Filtered air storage chamber 6: Floating dust generator 7,8: Annular member 12: Compressed air injection nozzle 19: Lever ( 29,30: Tube connection port for differential pressure detection 37: Screw conveyor 38: Dust storage 39: Adjust screw 40: Rotating brush 45: Vent 47: Dust filter 50: Test piece support 51 : Balance weight S: Test piece

【手続補正書】[Procedure amendment]

【提出日】平成7年12月1日[Submission date] December 1, 1995

【手続補正1】[Procedure amendment 1]

【補正対象書類名】図面[Document name to be amended] Drawing

【補正対象項目名】図5[Correction target item name] Fig. 5

【補正方法】変更[Correction method] Change

【補正内容】[Correction contents]

【図5】 [Figure 5]

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】 試験用粉塵を一定の濃度で含有する被濾
過空気を一時貯留可能な空間を有する被濾過空気貯留
室;一定の濃度で浮遊粉塵を含有する被濾過空気を被濾
過空気貯留室に供給し滞留させる手段;上下に配置され
た状態でバグフィルター試験片を挟持する一対の環状部
材からなり、被濾過空気貯留室の頂部開口部と分離可能
に連結された試験片取付部;上記試験片取付部を構成す
る環状部材の上側のものと一体化され、等速空気吸引手
段と連結され、且つ粉塵払い落し用圧縮空気を室内に噴
射する圧縮空気噴射ノズルを装着された清浄空気室;試
験片取付部およびそれと一体の清浄空気室を回動自在に
支持し、且つそれらを上記被濾過空気貯留室の頂部開口
部と連結された状態から引き離し180度旋回させて反
転状態になし得る、旋回可能な試験片取付部支持部材;
等速空気吸引手段による空気吸引に基づき被濾過空気貯
留室と清浄空気室との間に生じるフィルター差圧ΔPを
測定する手段;および、上記差圧ΔPの経時的変化を記
録し差圧ΔPが所定の値になったとき等速空気吸引手段
による空気吸引を中止させ圧縮空気噴射ノズルより圧縮
空気を噴射させる制御装置;を有することを特徴とする
バグフィルターの粉塵保持量測定装置。
1. A filtered air storage chamber having a space capable of temporarily storing filtered air containing test dust at a fixed concentration; filtered air containing chamber containing suspended dust at a fixed concentration. Means for supplying and accumulating in the above; a test piece attachment part which is composed of a pair of annular members for sandwiching the bag filter test piece in a state of being vertically arranged, and is separably connected to the top opening part of the filtered air storage chamber; A clean air chamber that is integrated with the upper side of the annular member that constitutes the test piece mounting portion, is connected to a constant velocity air suction means, and is equipped with a compressed air injection nozzle that injects compressed air for dust removal into the room. A test piece mounting portion and a clean air chamber integral therewith can be rotatably supported, and they can be turned 180 degrees apart from the state in which they are connected to the top opening of the filtered air storage chamber to be turned to an inverted state. , Turn Rotatable test piece mounting part support member;
Means for measuring the filter pressure difference ΔP generated between the filtered air storage chamber and the clean air chamber based on the air suction by the constant velocity air suction means; and the change over time of the pressure difference ΔP is recorded so that the pressure difference ΔP is A dust filter amount measuring device for a bag filter, comprising: a control device for stopping air suction by a constant velocity air suction means when a predetermined value is reached and injecting compressed air from a compressed air injecting nozzle.
【請求項2】 試験用粉塵を一定の濃度で含有する被濾
過空気を一時貯留可能な空間を有し、粉塵フィルター付
きの通気孔を備えた被濾過空気貯留室;浮遊粉塵を連続
的かつ定量的に発生させて被濾過空気貯留室に供給す
る、被濾過空気貯留室の底部開口部に接続された浮遊粉
塵発生装置;上下に配置された状態でバグフィルター試
験片を挟持する一対の環状部材からなり、被濾過空気貯
留室の頂部開口部と分離可能に連結された試験片取付
部;上記試験片取付部を構成する環状部材の上側のもの
と一体化され、等速空気吸引手段と連結され、且つ粉塵
払い落し用圧縮空気を室内に噴射する圧縮空気噴射ノズ
ルを装着された清浄空気室;試験片取付部およびそれと
一体の清浄空気室を回動自在に支持し、且つそれらを上
記被濾過空気貯留室の頂部開口部と連結された状態から
引き離し180度旋回させて反転状態になし得る、旋回
可能な試験片取付部支持部材;等速空気吸引手段による
空気吸引に基づき被濾過空気貯留室と清浄空気室との間
に生じるフィルター差圧ΔPを測定する手段;および、
上記差圧ΔPの経時的変化を記録し差圧ΔPが所定の値
になったとき等速空気吸引手段による空気吸引を中止さ
せ圧縮空気噴射ノズルより圧縮空気を噴射させる制御装
置;を有することを特徴とするバグフィルターの粉塵保
持量測定装置。
2. A filtered air storage chamber having a space capable of temporarily storing air to be filtered containing test dust at a constant concentration and having a ventilation hole with a dust filter; continuous and quantitative determination of suspended dust. Floating dust generating device connected to the bottom opening of the filtered air storage chamber that is generated and supplied to the filtered air storage chamber; a pair of annular members that sandwich the bag filter test pieces in a state of being vertically arranged And a test piece mounting portion separably connected to the top opening of the filtered air storage chamber; integrated with an upper part of an annular member constituting the test piece mounting portion and connected to a constant velocity air suction means. And a clean air chamber equipped with a compressed air injection nozzle for injecting compressed air for dust removal into the room; rotatably supporting the test piece mounting portion and the clean air chamber integrated therewith, and supporting them. The top of the filtered air storage chamber Swivelable test piece mounting part support member that can be separated from the state in which it is connected to the opening part and swiveled 180 degrees to be in an inverted state; filtered air storage chamber and clean air chamber based on air suction by constant velocity air suction means Means for measuring the filter pressure difference ΔP occurring between
A control device for recording the time-dependent change of the differential pressure ΔP and stopping the air suction by the constant velocity air suction means when the differential pressure ΔP reaches a predetermined value and injecting compressed air from the compressed air injecting nozzle. Dust retention measuring device of the characteristic bag filter.
【請求項3】 清浄空気室内に、該清浄空気室が反転状
態に置かれたとき取付けられる試験片の中央部付近に自
動的に接近して試験片を支持し、清浄空気室が正立状態
にある測定時は試験片から離れた位置に退避し得る試験
片支持部材を有することを特徴とする請求項1または2
に記載の粉塵保持量測定装置。
3. The clean air chamber automatically approaches the vicinity of a central portion of a test piece attached when the clean air chamber is placed in an inverted state to support the test piece, and the clean air chamber is in an upright state. 3. A test piece support member that can be retracted to a position away from the test piece during measurement in 1).
The device for measuring the amount of dust retained according to.
JP29598495A 1995-10-20 1995-10-20 Measuring device for bag filter dust retention Expired - Lifetime JP3280552B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP29598495A JP3280552B2 (en) 1995-10-20 1995-10-20 Measuring device for bag filter dust retention

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP29598495A JP3280552B2 (en) 1995-10-20 1995-10-20 Measuring device for bag filter dust retention

Publications (2)

Publication Number Publication Date
JPH09113435A true JPH09113435A (en) 1997-05-02
JP3280552B2 JP3280552B2 (en) 2002-05-13

Family

ID=17827639

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Cited By (9)

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CN102121895A (en) * 2011-01-21 2011-07-13 苏州科盛过滤技术有限公司 Mobile test instrument for dust collecting bag
CN103203331A (en) * 2013-04-03 2013-07-17 南京信息职业技术学院 Silent dust recovery device for sand and dust test chamber
CN103411867A (en) * 2013-07-23 2013-11-27 国家电网公司 Multifunctional corrosivity test platform for filtering materials
CN103792173A (en) * 2014-02-26 2014-05-14 福建鑫华股份有限公司 Method for testing dust resistance of filter material
CN104474981A (en) * 2014-11-10 2015-04-01 江汉大学 Dust aerosol generator with adjustable dust generating mass
CN105259093A (en) * 2015-11-16 2016-01-20 攀钢集团工程技术有限公司 Filter-bag type dust removing experiment system
CN105953060A (en) * 2016-07-08 2016-09-21 山东水泊焊割设备制造有限公司 Laser bracket
CN106769742A (en) * 2017-03-01 2017-05-31 西安科技大学 A kind of dust suppressant, dust-proofing agent dust removing effects test device and method of testing
CN108613910A (en) * 2017-07-31 2018-10-02 海宁文硕科技咨询有限公司 A kind of filter bag detection device of improvement

Cited By (14)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102121895A (en) * 2011-01-21 2011-07-13 苏州科盛过滤技术有限公司 Mobile test instrument for dust collecting bag
CN103203331A (en) * 2013-04-03 2013-07-17 南京信息职业技术学院 Silent dust recovery device for sand and dust test chamber
CN103203331B (en) * 2013-04-03 2015-01-14 南京信息职业技术学院 Silent dust recovery device for sand and dust test chamber
CN103411867B (en) * 2013-07-23 2015-11-18 国家电网公司 A kind of multifunctional filter material erosion test platform
CN103411867A (en) * 2013-07-23 2013-11-27 国家电网公司 Multifunctional corrosivity test platform for filtering materials
CN103792173A (en) * 2014-02-26 2014-05-14 福建鑫华股份有限公司 Method for testing dust resistance of filter material
CN103792173B (en) * 2014-02-26 2016-06-29 福建鑫华股份有限公司 A kind of method of testing of the anti-dust performance of the filtering material for filter bag
CN104474981A (en) * 2014-11-10 2015-04-01 江汉大学 Dust aerosol generator with adjustable dust generating mass
CN105259093A (en) * 2015-11-16 2016-01-20 攀钢集团工程技术有限公司 Filter-bag type dust removing experiment system
CN105953060A (en) * 2016-07-08 2016-09-21 山东水泊焊割设备制造有限公司 Laser bracket
CN106769742A (en) * 2017-03-01 2017-05-31 西安科技大学 A kind of dust suppressant, dust-proofing agent dust removing effects test device and method of testing
CN106769742B (en) * 2017-03-01 2023-02-21 西安科技大学 Dust suppressant and dust suppressant dedusting effect testing device and testing method
CN108613910A (en) * 2017-07-31 2018-10-02 海宁文硕科技咨询有限公司 A kind of filter bag detection device of improvement
CN108613910B (en) * 2017-07-31 2020-06-16 威海畅享海天新材料科技有限公司 Improved filter bag detection device

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