JPS63151339A - Induction type aerosol feeder - Google Patents
Induction type aerosol feederInfo
- Publication number
- JPS63151339A JPS63151339A JP61296823A JP29682386A JPS63151339A JP S63151339 A JPS63151339 A JP S63151339A JP 61296823 A JP61296823 A JP 61296823A JP 29682386 A JP29682386 A JP 29682386A JP S63151339 A JPS63151339 A JP S63151339A
- Authority
- JP
- Japan
- Prior art keywords
- mixing chamber
- double pipe
- air
- flow passage
- aerosol
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
- 239000000443 aerosol Substances 0.000 title claims abstract description 26
- 230000006698 induction Effects 0.000 title claims abstract 3
- 239000000203 mixture Substances 0.000 claims description 13
- 239000008246 gaseous mixture Substances 0.000 abstract 3
- 239000002245 particle Substances 0.000 description 35
- 239000007789 gas Substances 0.000 description 21
- 238000012360 testing method Methods 0.000 description 5
- 238000009826 distribution Methods 0.000 description 4
- 239000000428 dust Substances 0.000 description 4
- 238000011109 contamination Methods 0.000 description 3
- MQIUGAXCHLFZKX-UHFFFAOYSA-N Di-n-octyl phthalate Natural products CCCCCCCCOC(=O)C1=CC=CC=C1C(=O)OCCCCCCCC MQIUGAXCHLFZKX-UHFFFAOYSA-N 0.000 description 2
- BJQHLKABXJIVAM-UHFFFAOYSA-N bis(2-ethylhexyl) phthalate Chemical compound CCCCC(CC)COC(=O)C1=CC=CC=C1C(=O)OCC(CC)CCCC BJQHLKABXJIVAM-UHFFFAOYSA-N 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 238000005259 measurement Methods 0.000 description 2
- 239000004793 Polystyrene Substances 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 238000009792 diffusion process Methods 0.000 description 1
- 238000007865 diluting Methods 0.000 description 1
- 239000004816 latex Substances 0.000 description 1
- 229920000126 latex Polymers 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 229920002223 polystyrene Polymers 0.000 description 1
- 239000004065 semiconductor Substances 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J4/00—Feed or outlet devices; Feed or outlet control devices
- B01J4/001—Feed or outlet devices as such, e.g. feeding tubes
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F23/00—Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
- B01F23/20—Mixing gases with liquids
- B01F23/21—Mixing gases with liquids by introducing liquids into gaseous media
- B01F23/213—Mixing gases with liquids by introducing liquids into gaseous media by spraying or atomising of the liquids
- B01F23/2132—Mixing gases with liquids by introducing liquids into gaseous media by spraying or atomising of the liquids using nozzles
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Organic Chemistry (AREA)
- Nozzles (AREA)
- Feeding, Discharge, Calcimining, Fusing, And Gas-Generation Devices (AREA)
Abstract
Description
【発明の詳細な説明】
産 土の1
本発明は、誘引形エアロゾル供給器に関し、とくに定濃
度エアロゾルを清浄気体で希釈し所要濃度のエアロゾル
を長期間に亘り供給するに適した誘引形エアロゾル供給
器に関する。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to an induced aerosol supply device, and in particular to an induced aerosol supply device suitable for diluting constant concentration aerosol with clean gas and supplying a required concentration of aerosol over a long period of time. Concerning vessels.
支え夏且3
半導体装置製造過程その他で必要とされるクリーンルー
ムにおける汚染拡散試験、エアフィルターの漏洩試験、
ダクト内に設置されたフィルターの現場性能試験等の目
的のため、粒子を既知濃度で含む空気が使われる。この
試験用空気は、清浄空気に標準粒子発生装置等からの粒
子を混入することにより供給されるのが普通である。し
かしこの従来方法には、標準粒子発生装置の機能上の限
界による粒度の変動、同様な原因による粒子濃度の変動
、送風機からのオイル粒子の混入等の問題があった。Support Summer 3 Contamination diffusion tests in clean rooms required in semiconductor device manufacturing processes, air filter leakage tests,
Air containing a known concentration of particles is used for purposes such as on-site performance testing of filters installed in ducts. This test air is usually supplied by mixing particles from a standard particle generator or the like into clean air. However, this conventional method has problems such as variations in particle size due to functional limitations of the standard particle generator, variations in particle concentration due to similar causes, and contamination of oil particles from the blower.
が ゛ しようと る。 へ
従って、本発明が解決しようとする問題点は、試験用空
気などのエアロゾルにおける粒度及び粒子濃度の安定化
並びにオイル粒子の混入防止にある。is trying to do so. Accordingly, the problem to be solved by the present invention is to stabilize the particle size and particle concentration in aerosol such as test air and to prevent oil particles from being mixed into the aerosol.
1 占 ・ るための−
第1図及び第2図を参照するに、本発明による誘引形エ
アロゾル供給器1においては、二重管2の内側流路3及
び外側流路4の一端を混合室5に連通し、混合室5には
さらに混合気流路6を連通させる。二重管2の内外の流
路3.4の一方の流路から」二記混合室5へ清浄気体を
送入し、その清浄気体の流れの誘引作用によって他方の
流路な介して定濃度エアロゾルを上記混合室5へ吸引し
、混合室5で生成した混合エアロゾルを上記混合気流路
6へ送出する。1. To occupy - Referring to FIGS. 1 and 2, in the induced aerosol supply device 1 according to the present invention, one end of the inner flow path 3 and the outer flow path 4 of the double pipe 2 is connected to the mixing chamber. 5, and the mixing chamber 5 is further communicated with a mixture flow path 6. Clean gas is fed into the mixing chamber 5 from one of the internal and external channels 3.4 of the double pipe 2, and a constant concentration is maintained through the other channel by the attraction of the flow of the clean gas. The aerosol is sucked into the mixing chamber 5, and the mixed aerosol generated in the mixing chamber 5 is sent to the air mixture flow path 6.
例えば、二重管2の内側流路3に清浄気体として矢印B
で示される清浄空気を送入し、矢印Aで示される屋外大
気(以下、外気という。)を定濃度エアロゾルとして外
側流路4を介し上記清浄空気流により吸引される様にす
る。For example, arrow B is added to the inner flow path 3 of the double pipe 2 as a clean gas.
The clean air shown by arrow A is introduced, and the outdoor air (hereinafter referred to as outside air) shown by arrow A is made into a constant concentration aerosol and sucked by the above clean air flow through the outer flow path 4.
m月
第2図の例を参照して作用を説明するに、オイルレスポ
ンプ11によって外気Aをエアフィルター12に通すこ
とによって清浄気体Bとする。この清浄51体Bは、オ
イルレスポンプ11の吐出圧により二重管2の一方の流
路、即ち図示例の場合の内側流路3へ送出され、さらに
内側流路3の端末から混合室5内へ噴出される。二重管
2の他方の流路、即ち図示例の場合の外側流路4は外気
Aに連通しており、混合室5内の二重管端束から清浄気
体Bが上記吐出圧によって噴出される際に外気Aが清浄
気体Bの誘引作用により混合室5内へ吸引される。The operation will be explained with reference to the example shown in FIG. This cleaning body 51 B is sent out to one flow path of the double pipe 2, that is, the inner flow path 3 in the illustrated example, by the discharge pressure of the oilless pump 11, and further from the end of the inner flow path 3 to the mixing chamber 5. It is ejected inside. The other flow path of the double tube 2, that is, the outer flow path 4 in the illustrated example, communicates with the outside air A, and the clean gas B is blown out from the double tube end bundle in the mixing chamber 5 by the above discharge pressure. During this process, outside air A is drawn into the mixing chamber 5 by the attraction of the clean gas B.
こうして混合室5内で混合された外気Aと清浄気体Bと
の混合気Cは混合気流路6を介して所要の外部装置(図
示せず)へ送出される。The mixture C of the outside air A and the clean gas B thus mixed in the mixing chamber 5 is sent to a required external device (not shown) via the mixture flow path 6.
一般に外気A、即ち屋外大気における粒度分布及び粒子
濃度は極めて安定であることが知られている。他方、外
気Aを適当なエアフィルター12によって浄化した清浄
気体Bの粒子濃度は外気におけるそれに比して遥に低く
保たれる。従って、外気Aにおける粒度分布及び粒子濃
度が安定である限り、混合室5において外気Aと清浄気
体Bとを混合して生成した混合気Cの粒度分布及び粒子
濃度を長時間に亘り安定に保つことが可能になる。It is generally known that the particle size distribution and particle concentration in outside air A, that is, outside air, are extremely stable. On the other hand, the particle concentration of the clean gas B obtained by purifying the outside air A with a suitable air filter 12 is kept much lower than that in the outside air. Therefore, as long as the particle size distribution and particle concentration in outside air A are stable, the particle size distribution and particle concentration of mixture C generated by mixing outside air A and clean gas B in mixing chamber 5 can be kept stable for a long time. becomes possible.
また、エアフィルター12で浄化後の清浄気体Bの流れ
によって外気Aを誘引することにより両党体を直接に混
合するので、ポンプからのオイル飛沫粒子その他の異物
混入のおそれがない。Further, since the two gases are directly mixed by attracting the outside air A by the flow of the clean gas B after being purified by the air filter 12, there is no risk of contamination by oil droplets or other foreign matter from the pump.
外気Aと清浄気体Bとの混合比率は、混合室5への清浄
気体Bの噴出速度を調節しその誘引作用の強さを加減す
ることによりこれを制御できるので、上記混合気C中の
粒度分布及び粒子濃度を一定範囲内で制御することが可
能である。The mixing ratio of outside air A and clean gas B can be controlled by adjusting the jetting speed of clean gas B into the mixing chamber 5 and adjusting the strength of its attracting effect, so that the particle size in the mixture C can be controlled. It is possible to control the distribution and particle concentration within certain limits.
好ましくは、混合室5内の二重管2の出口における外気
Aの誘引を確実にするため、その出口における内側流路
3及び外側流路4の端末を絞り、第1図に示される様に
内側オリフィス3a及び外側オリフィス4aを形成する
。必要に応じ、二重管2の内側流路3及び外側流路4の
入口側に第2図に示される様に流量計13を配置しても
よい。Preferably, in order to ensure the attraction of outside air A at the outlet of the double pipe 2 in the mixing chamber 5, the ends of the inner flow path 3 and the outer flow path 4 at the outlet are throttled, as shown in FIG. An inner orifice 3a and an outer orifice 4a are formed. If necessary, a flow meter 13 may be arranged on the inlet side of the inner flow path 3 and outer flow path 4 of the double pipe 2 as shown in FIG.
以上、外気Aと清浄気体Bとの混合の例について説明し
たが、懸濁粒子を含む気体からなる任意のエアロゾルに
対して本発明のエアロゾル供給器を適用できることは当
業者には明らかである。Although the example of mixing outside air A and clean gas B has been described above, it is clear to those skilled in the art that the aerosol supply device of the present invention can be applied to any aerosol made of gas containing suspended particles.
支五遣
本発明によるエアロゾル供給器1の動作特性を第3図の
装置により測定した。即ち、オイルレスポンプ11の速
度を調節することにより、エアフィルター12を介して
エアロゾル供給器1へ送出される清浄気体Bの流速を制
御し、その流量を流量計13により監視しながら混合気
C中の粒子について測定した。この場合も外気Aを二重
管2の外側波路4に供給し、清浄気体Bをその内側流路
3に供給した。The operating characteristics of the aerosol supply device 1 according to the present invention were measured using the apparatus shown in FIG. That is, by adjusting the speed of the oilless pump 11, the flow rate of the clean gas B sent to the aerosol supply device 1 via the air filter 12 is controlled, and while the flow rate is monitored by the flow meter 13, the mixture C is The particles inside were measured. In this case as well, outside air A was supplied to the outer wave path 4 of the double pipe 2, and clean gas B was supplied to the inner flow path 3 thereof.
清浄気体Bの流量の変化に対する混合器Cにおける粒子
濃度即ち発塵濃度の変化の測定結果の一例を第4図に示
す。図中、カーブPは粒径0.3μm以上の粒子濃度を
示し、カーブQは粒径0.5μm以」二の粒子濃度を示
す。同図から明らかな様に、清浄気体Bの流量を調節す
ることにより混合気C中の粒子濃度を制御することがで
きる。FIG. 4 shows an example of measurement results of changes in particle concentration, that is, dust concentration, in mixer C with respect to changes in the flow rate of clean gas B. In the figure, curve P shows the concentration of particles with a particle size of 0.3 μm or more, and curve Q shows the concentration of particles with a particle size of 0.5 μm or more. As is clear from the figure, the particle concentration in the mixture C can be controlled by adjusting the flow rate of the clean gas B.
混合気C中の粒子濃度の経時変化測定値の一例を第5図
に示す。クリーンルームにおいて問題となる粒径1μm
以下の粒子について粒子濃度が3時間以上に亘り安定し
ていることが確認された。An example of measured values of the particle concentration in the mixture C over time is shown in FIG. Particle size of 1 μm is a problem in clean rooms
It was confirmed that the particle concentrations of the following particles remained stable for more than 3 hours.
従来は、1時間以上の粒子濃度の安定を得ることは困難
であった。Conventionally, it has been difficult to stabilize the particle concentration for more than one hour.
肛艶五分浬
以」−詳細に説明した如く、本発明による誘引形エアロ
ゾル供給器は、混合室へ送入される清浄気体流の誘引作
用により定濃度エアロゾルを混合室へ吸引して混合エア
ロゾルを生成するので次の効果を奏する。As explained in detail, the induced aerosol supply device according to the present invention draws a constant concentration aerosol into the mixing chamber by the attracting action of the clean gas flow introduced into the mixing chamber to form a mixed aerosol. Since it generates , it has the following effects.
(イ) DOP(ジオクチルフタレイト)やPSE、(
ポリスチレンラテックス)などの標準粒子発生装置を用
いずに、大気塵の利用により所要粒子の供給を行うこと
ができる。(a) DOP (dioctyl phthalate), PSE, (
The required particles can be supplied by using atmospheric dust without using standard particle generators such as polystyrene latex.
(ロ)大気の粒子濃度が安定している限り、発塵、濃度
を長時間安定させることができる。(b) As long as the particle concentration in the atmosphere is stable, dust generation and concentration can be stabilized for a long time.
(ハ)誘引作用をする清浄空気流の流量調節により一定
範囲内の発塵濃度制御が可能である。(c) It is possible to control the dust concentration within a certain range by adjusting the flow rate of the clean air flow that acts as an attraction.
(ニ)極めて小型にできるので、クリーンルーム内等の
狭い場所での現場測定に利用できる。(d) Since it can be made extremely small, it can be used for on-site measurements in narrow spaces such as clean rooms.
(ホ)空気以外のエアロゾルの供給器としても使用する
ことができる。(e) It can also be used as a supply device for aerosols other than air.
(へ)エアロゾル供給器以外として、エアロゾル稀釈器
としても使用できる。(f) In addition to being an aerosol supply device, it can also be used as an aerosol diluter.
第1図は一実施例の図式的断面図、第2図は使用態様の
説明図、第3図は特性測定装置のブロック図、第4図及
び第5図は特性を示すグラフである。
1・・・エアロゾル供給器、 2・・・二重管、
3・・・内側流路、 4・・・外側流路、 5・・・
混合室、6・・・混合気流路、 11・・・オイルレス
ポンプ、12・・・エアフィルター、 13・・・流量
計、 A・・・外気、 B・・・清浄気体、 C・・
・混合気。FIG. 1 is a schematic cross-sectional view of one embodiment, FIG. 2 is an explanatory diagram of usage, FIG. 3 is a block diagram of a characteristic measuring device, and FIGS. 4 and 5 are graphs showing characteristics. 1...Aerosol supply device, 2...Double pipe,
3...Inner channel, 4...Outer channel, 5...
Mixing chamber, 6...Mixture flow path, 11...Oilless pump, 12...Air filter, 13...Flow meter, A...Outside air, B...Clean gas, C...
・Mixture.
Claims (1)
端に連通する混合室、並びに前記混合室に連通する混合
気流路を備え、前記二重管の一方の流路から上記混合室
へ送入される清浄気体流の誘引作用により前記二重管の
他方の流路を介して定濃度エアロゾルを上記混合室へ吸
引し混合されたエアロゾルを上記混合気流路へ送出して
なる誘引形エアロゾル供給器。A double pipe having an inner flow path and an outer flow path, a mixing chamber communicating with one end of the double pipe, and a mixture flow path communicating with the mixing chamber; Induction by attracting a constant concentration aerosol into the mixing chamber through the other channel of the double pipe by the attraction of the clean gas flow sent into the chamber, and sending the mixed aerosol to the mixture channel. Type aerosol supply device.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP61296823A JPS63151339A (en) | 1986-12-15 | 1986-12-15 | Induction type aerosol feeder |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP61296823A JPS63151339A (en) | 1986-12-15 | 1986-12-15 | Induction type aerosol feeder |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS63151339A true JPS63151339A (en) | 1988-06-23 |
Family
ID=17838615
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP61296823A Pending JPS63151339A (en) | 1986-12-15 | 1986-12-15 | Induction type aerosol feeder |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS63151339A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2002531260A (en) * | 1998-12-05 | 2002-09-24 | ゲーエーアー フィンナー ゲゼルシャフト ミット ベシュレンクテル ハフツング | Equipment for the generation of aerosols |
Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5226619A (en) * | 1975-08-25 | 1977-02-28 | Tsunekichi Kushishitamachi | Continuous and automatic mixing device of liquid |
-
1986
- 1986-12-15 JP JP61296823A patent/JPS63151339A/en active Pending
Patent Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5226619A (en) * | 1975-08-25 | 1977-02-28 | Tsunekichi Kushishitamachi | Continuous and automatic mixing device of liquid |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2002531260A (en) * | 1998-12-05 | 2002-09-24 | ゲーエーアー フィンナー ゲゼルシャフト ミット ベシュレンクテル ハフツング | Equipment for the generation of aerosols |
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