JPH0131290Y2 - - Google Patents
Info
- Publication number
- JPH0131290Y2 JPH0131290Y2 JP12521583U JP12521583U JPH0131290Y2 JP H0131290 Y2 JPH0131290 Y2 JP H0131290Y2 JP 12521583 U JP12521583 U JP 12521583U JP 12521583 U JP12521583 U JP 12521583U JP H0131290 Y2 JPH0131290 Y2 JP H0131290Y2
- Authority
- JP
- Japan
- Prior art keywords
- tube
- filter
- tubes
- filter tube
- fluid
- 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
Links
- 239000012530 fluid Substances 0.000 claims description 10
- 239000011521 glass Substances 0.000 claims description 5
- 239000000919 ceramic Substances 0.000 claims description 4
- 238000000926 separation method Methods 0.000 claims description 4
- 239000000463 material Substances 0.000 claims description 2
- ODINCKMPIJJUCX-UHFFFAOYSA-N Calcium oxide Chemical compound [Ca]=O ODINCKMPIJJUCX-UHFFFAOYSA-N 0.000 description 4
- 230000008602 contraction Effects 0.000 description 3
- 230000035882 stress Effects 0.000 description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 3
- 235000012255 calcium oxide Nutrition 0.000 description 2
- 239000000292 calcium oxide Substances 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 230000032683 aging Effects 0.000 description 1
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 1
- 238000011001 backwashing Methods 0.000 description 1
- 238000010828 elution Methods 0.000 description 1
- 239000010419 fine particle Substances 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 238000012856 packing Methods 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 238000005192 partition Methods 0.000 description 1
- 238000007789 sealing Methods 0.000 description 1
- 238000005245 sintering Methods 0.000 description 1
Description
【考案の詳細な説明】
耐熱性および耐薬品性の高いアルミナ等の微細
粒子の焼結により作られるフイルタ管は、流体内
に含まれる粒子の除去装置、或はセラミツクフイ
ルタ管に充填した生石灰に注水を行つて生石灰と
水との間の反応熱を利用するる熱源装置等に利用
することができる。このものは、強度が低いた
め、パツキン等の密封手段を使用しつつ片持ち状
態において装置に組込まれるのを普通とするので
あるが、このような構成のものにおいては装置を
通して流される流体に効率の高い流れを与え難
く、フイルタ管の支持部に使用されるパツキンに
ついても、老化、成分の溶出等の問題点があり、
焼結セラミツクフイルタ管の高い耐熱性および耐
薬品性を充分に生かし得ない。[Detailed description of the invention] A filter tube made by sintering fine particles such as alumina, which has high heat resistance and chemical resistance, can be used as a device for removing particles contained in a fluid, or as a ceramic filter tube filled with quicklime. It can be used in a heat source device, etc. that utilizes the heat of reaction between quicklime and water by injecting water. Due to its low strength, it is usually installed in a device in a cantilevered state using sealing means such as a gasket, but with such a configuration, the efficiency of the fluid flowing through the device is low. It is difficult to provide a high flow of water, and the packing used for supporting the filter tube also has problems such as aging and elution of components.
The high heat resistance and chemical resistance of the sintered ceramic filter tube cannot be fully utilized.
本案は、上記の焼結セラミツクフイルタ管(以
下、単にフイルタ管と言う。)の固有の性質を充
分に生かすと共に、過大の応力がフイルタ管に加
わらないようにした分離、反応装置を提供するこ
とを目的とするもので、本案を図について説明す
れば次の如くである。 The purpose of this invention is to provide a separation and reaction device that takes full advantage of the unique properties of the sintered ceramic filter tube (hereinafter simply referred to as filter tube) and prevents excessive stress from being applied to the filter tube. The purpose of this proposal is as follows, and the main purpose of the proposal can be explained with reference to figures.
図において、1,2は長さが等しいフイルタ
管、3はフイルタ管1,2の下端1a,2aの間
を連ねるガラス製曲管、4,5はフイルタ管1,
2の上端1b,2bに連なるガラス製直管であ
る。フイルタ管1,2と、曲管3と、直管4,5
とは、平行部に各1本のフイルタ管が接結されて
いるU字管6を構成する。 In the figure, 1 and 2 are filter tubes of equal length, 3 is a curved glass tube connecting the lower ends 1a and 2a of the filter tubes 1 and 2, and 4 and 5 are the filter tubes 1 and 2.
It is a straight glass tube connected to the upper ends 1b, 2b of 2. Filter pipes 1 and 2, bent pipe 3, and straight pipes 4 and 5
constitutes a U-shaped tube 6 in which one filter tube is connected to each parallel portion.
7はU字管6におけるガラス部分と同質の材料
より成る器体で、U字管6は、フイルタ管1,2
をこの器体7の内部に置いて、器体7の頂部8に
より懸吊支持される。器体7の断面形は、図示の
如く円形とされるのを普通とするが、必要に応じ
て他の形状、例えば楕円形にされる。9,10は
器体7上に設けられた流体の流出入口部、11は
ドレーンパイプ等に接続される流体の排出口であ
る。 7 is a container made of the same material as the glass portion of the U-shaped tube 6;
is placed inside this vessel 7 and is suspended and supported by the top 8 of the vessel 7. The cross-sectional shape of the vessel body 7 is generally circular as shown in the figure, but it may be made into another shape, for example, an oval shape, if necessary. Numerals 9 and 10 are fluid inlet and outlet portions provided on the vessel body 7, and 11 is a fluid outlet connected to a drain pipe or the like.
器体7にはフイルタ管1,2間における流体の
流れを案内する部分を設けることができる。第3
図および第4図はこの案内が隔板12により行わ
れるようにした場合を示す。 The container body 7 can be provided with a portion that guides the flow of fluid between the filter tubes 1 and 2. Third
The figures and FIG. 4 show a case in which this guidance is performed by a diaphragm 12.
フイルタ管1,2の壁を通る流体の流れの方向
は、流体がフイルタ管1,2に流入する方向また
は流体がフイルタ管1,2より流出する方向とさ
れるが、装置が分離装置として使用される場合に
は、分離されるべき流体がU字管6より器体7内
に向つて流れるように流れ方向が選定される。 The direction of fluid flow through the walls of the filter tubes 1, 2 is the direction in which the fluid flows into the filter tubes 1, 2 or the direction in which the fluid flows out from the filter tubes 1, 2, but if the device is used as a separator, In this case, the flow direction is selected so that the fluid to be separated flows from the U-shaped tube 6 into the container body 7.
分離または反応に使用された装置は、適当な媒
体を使用して逆洗法により洗滌されて次の使用に
待機させられる。 The equipment used for the separation or reaction is cleaned by backwashing using a suitable medium and made ready for the next use.
以上において説明した本案による装置は、空間
利用率を高くすると共にフイルタ管に過大の応力
が加わらないようにされているものである。フイ
ルタ管1,2に過大の応力が加わらないのは、器
体7の頂部8に生じる水平方向の膨張収縮の量が
U字管6の曲管3に生じる水平方向の膨張収縮の
量に等しいと云う条件と、U字管6に生じる膨張
収縮が垂直方向において二つの脚部につき偏差を
伴うことなく起ると云う条件とが成立しているこ
とによる。 The device according to the present invention described above has a high space utilization rate and is designed to prevent excessive stress from being applied to the filter tube. Excessive stress is not applied to the filter tubes 1 and 2 because the amount of horizontal expansion and contraction that occurs at the top 8 of the vessel body 7 is equal to the amount of horizontal expansion and contraction that occurs at the bent tube 3 of the U-shaped tube 6. This is because the following conditions are satisfied, and the condition that the expansion and contraction occurring in the U-shaped tube 6 occurs in the vertical direction without any deviation between the two legs.
第1図は本案による分離または反応装置の垂直
断面図、第2図は第1図の−線方向にとられ
た横断面図、第3図および第4図は第1図および
第2図に示すものの変形を示す垂直断面図および
横断面図である。
1,2……フイルタ管、1a,2a……フイル
タ管の下端、1b,2b……フイルタ管の上端、
3……曲管、4,5……直管、6……U字管、7
……器体、8……器体の頂部、9,10……器体
上の流出入口部、11……排出口、12……隔
板。
Figure 1 is a vertical sectional view of the separation or reaction apparatus according to the present invention, Figure 2 is a cross sectional view taken in the - line direction of Figure 1, and Figures 3 and 4 are similar to Figures 1 and 2. FIG. 6 is a vertical and cross-sectional view showing a modification of what is shown. 1, 2... Filter tube, 1a, 2a... Lower end of filter tube, 1b, 2b... Upper end of filter tube,
3...Bent pipe, 4,5...Straight pipe, 6...U-shaped pipe, 7
... vessel body, 8... top of vessel body, 9, 10... outlet/inlet portion on vessel body, 11... discharge port, 12... partition plate.
Claims (1)
これらのフイルタ管1,2に直列に連なるガラス
製曲管3および直管4,5とにより、平行部に各
1本のフイルタ管が接合されているU字管6を構
成し、U字管6のガラス部分と同質の材料より成
つていて流体の流出入口部9,10を設けられた
器体7の頂部8により、フイルタ管1,2を器体
7の内部に置いて、U字管6を懸吊支持させたこ
とを特徴とする、焼結セラミツクフイルタ管を使
用する分離または反応装置。 Two sintered filter tubes 1 and 2 of equal length,
A curved glass tube 3 and straight tubes 4 and 5 connected in series to these filter tubes 1 and 2 constitute a U-shaped tube 6 in which one filter tube is connected to each parallel portion. The top part 8 of the container body 7 is made of the same material as the glass part 6 and is provided with fluid inlet and outlet sections 9 and 10. A separation or reaction device using a sintered ceramic filter tube, characterized in that the tube 6 is suspended and supported.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP12521583U JPS6035711U (en) | 1983-08-12 | 1983-08-12 | Separation or reaction equipment using sintered ceramic filter tubes |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP12521583U JPS6035711U (en) | 1983-08-12 | 1983-08-12 | Separation or reaction equipment using sintered ceramic filter tubes |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS6035711U JPS6035711U (en) | 1985-03-12 |
JPH0131290Y2 true JPH0131290Y2 (en) | 1989-09-26 |
Family
ID=30285172
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP12521583U Granted JPS6035711U (en) | 1983-08-12 | 1983-08-12 | Separation or reaction equipment using sintered ceramic filter tubes |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS6035711U (en) |
Families Citing this family (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS6433319A (en) * | 1987-07-28 | 1989-02-03 | Kajima Corp | Earthquake isolation floor |
JP2010201549A (en) * | 2009-03-03 | 2010-09-16 | Fuji Xerox Co Ltd | Microchannel device, separation method, and separator |
-
1983
- 1983-08-12 JP JP12521583U patent/JPS6035711U/en active Granted
Also Published As
Publication number | Publication date |
---|---|
JPS6035711U (en) | 1985-03-12 |
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