JPH0125629Y2 - - Google Patents
Info
- Publication number
- JPH0125629Y2 JPH0125629Y2 JP1984034802U JP3480284U JPH0125629Y2 JP H0125629 Y2 JPH0125629 Y2 JP H0125629Y2 JP 1984034802 U JP1984034802 U JP 1984034802U JP 3480284 U JP3480284 U JP 3480284U JP H0125629 Y2 JPH0125629 Y2 JP H0125629Y2
- Authority
- JP
- Japan
- Prior art keywords
- perforated plate
- water
- diameter
- holes
- hole
- 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
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 43
- 239000000463 material Substances 0.000 claims description 7
- 239000002245 particle Substances 0.000 claims description 7
- 238000005342 ion exchange Methods 0.000 claims description 6
- 230000007423 decrease Effects 0.000 claims description 3
- 239000011148 porous material Substances 0.000 claims 1
- NWUYHJFMYQTDRP-UHFFFAOYSA-N 1,2-bis(ethenyl)benzene;1-ethenyl-2-ethylbenzene;styrene Chemical compound C=CC1=CC=CC=C1.CCC1=CC=CC=C1C=C.C=CC1=CC=CC=C1C=C NWUYHJFMYQTDRP-UHFFFAOYSA-N 0.000 description 9
- 239000003456 ion exchange resin Substances 0.000 description 8
- 229920003303 ion-exchange polymer Polymers 0.000 description 8
- 238000011001 backwashing Methods 0.000 description 7
- 239000011347 resin Substances 0.000 description 2
- 229920005989 resin Polymers 0.000 description 2
- 239000003957 anion exchange resin Substances 0.000 description 1
- 239000003729 cation exchange resin Substances 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 230000008602 contraction Effects 0.000 description 1
- 230000006378 damage Effects 0.000 description 1
- 238000009792 diffusion process Methods 0.000 description 1
- 239000000945 filler Substances 0.000 description 1
- 150000002500 ions Chemical class 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000008213 purified water Substances 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 230000008929 regeneration Effects 0.000 description 1
- 238000011069 regeneration method Methods 0.000 description 1
Landscapes
- Treatment Of Liquids With Adsorbents In General (AREA)
- Treatment Of Water By Ion Exchange (AREA)
- Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
Description
【考案の詳細な説明】
この考案はイオン交換塔、の下部鏡板上などに
設置する充填材支持機構を兼ねる集、散水装置に
関するもので、処理水を得るために下向流で集水
する際は水頭損失が余り大きくならず且つ、スケ
ールや夾雑物によつて閉塞されず、又、逆洗など
のために上向流で散水する際は均一な散水効果を
得ることができる様にしたものである。[Detailed description of the invention] This invention relates to a collection and water sprinkling device that doubles as a filler support mechanism and is installed on the lower head plate of an ion exchange tower. The water head loss is not too large, and it is not blocked by scale or foreign matter, and it is possible to obtain a uniform watering effect when watering in an upward flow for backwashing etc. It is.
第1図はイオン交換塔で、その下端鏡部1上に
は集水散水装置2を設ける。従来の集散水装置は
第2図に一部を拡大して示した様に、その上に支
持する充填層3のイオン交換樹脂の粒径よりも可
成り直径が大きい孔4′,5′を多数有する上部多
孔板4と下部多孔板5の間にイオン交換樹脂の粒
径より網目6′が小さい網材6、例えばサランネ
ツトを挟み、上下多孔板の孔4′,5′を上下方向
に揃えて設置している。しかし、これでは上下多
孔板の大きな孔4′,5′内に露出する網材の大き
な開口比により処理水を下降流で通水する集水時
は水頭損失が少なく、動力費も低減し、また閉塞
も防止されるが、逆洗などのために上向流で通水
する散水時は開口比の大きいことが災いして偏流
が起り、均等散水性能が著しく悪く、逆洗しても
イオン交換樹脂が性能を充分に回復しないとか、
回復するにしても所要時間が非常にかゝり逆洗水
の使用量が莫大になるとかの欠点がある。このた
め上下の多孔板の孔径を小さくし、開口比を小さ
くすると集水時は水頭損失が大きくなると共に、
孔や網目は夾雑物で詰り易く、最悪の場合は破壊
の虞がある。 FIG. 1 shows an ion exchange tower, and a water collecting and sprinkling device 2 is provided on the mirror section 1 at the lower end of the tower. As shown in a partially enlarged view of FIG. 2, the conventional water collection and distribution device has holes 4' and 5' whose diameter is considerably larger than the particle size of the ion exchange resin of the packed bed 3 supported above. A mesh material 6, for example Sarannet, whose mesh 6' is smaller than the particle size of the ion exchange resin is sandwiched between the upper perforated plate 4 and the lower perforated plate 5, which have a large number, and the holes 4' and 5' of the upper and lower perforated plates are aligned in the vertical direction. It is installed. However, with this, due to the large opening ratio of the mesh material exposed in the large holes 4' and 5' of the upper and lower perforated plates, there is less water head loss when collecting water by flowing the treated water in a downward flow, and the power cost is also reduced. It also prevents blockages, but when water is passed in an upward flow for backwashing, etc., the large opening ratio causes uneven flow, resulting in extremely poor uniform watering performance, and even when backwashing, ion If the replacement resin does not restore performance sufficiently,
Even if recovery occurs, it takes a very long time and requires a huge amount of backwash water. Therefore, if the hole diameter of the upper and lower perforated plates is made smaller and the aperture ratio is made smaller, the water head loss will increase when water is collected, and
The holes and meshes are easily clogged with foreign matter, and in the worst case, there is a risk of destruction.
又、偏流をなるべく防止するため逆洗水の入口
(集水時は処理水の出口を兼ねる)7の上方にバ
ツフル8を設ける例もあるが、充分ではない。特
にイオン交換塔は樹脂の性能を回復させるため
に、過塔、その他の処理塔に較べて、逆洗のた
めの散水時における均等散水性能に対し要求基準
が高い。 In addition, there is an example in which a baffle 8 is provided above the backwash water inlet (which also serves as the treated water outlet when collecting water) 7 in order to prevent drifting as much as possible, but this is not sufficient. In particular, in order to restore the performance of the resin, ion exchange towers have higher requirements for uniform water sprinkling performance during water sprinkling for backwashing than filter towers and other treatment towers.
そこで本考案は上部多孔板4、中間の網材6は
従来通りであるが、下部多孔板の孔の径を上部多
孔板よりも小さくし、これにより処理水を下向流
で通水する集水時は水頭損失は僅かに増大する
が、逆洗の際の散水時、塔内全域に均等に散水で
きる様にしたのである。 Therefore, in the present invention, the upper perforated plate 4 and the middle mesh material 6 are the same as before, but the diameter of the holes in the lower perforated plate is made smaller than that of the upper perforated plate, which allows the treated water to flow downward. Although the head loss increases slightly when water is used, water can be sprayed evenly throughout the tower during backwashing.
第3図及び第4図は本考案の集散水装置の夫々
一部を示すもので、上部多孔板4の孔4′は従来
と同様にイオン交換樹脂の粒径より可成り大き
く、又、網材6の網目6′はイオン交換樹脂の粒
径より小さいが、上部多孔板の孔と同配置で、上
下方向に揃つた下部多孔板9の孔の直径Dは上部
多孔板よりも小さい。 Figures 3 and 4 show parts of the water collection and distribution device of the present invention, in which the holes 4' of the upper perforated plate 4 are considerably larger than the particle size of the ion exchange resin as in the conventional case, and the holes 4' are made of a mesh. Although the mesh 6' of the material 6 is smaller than the particle size of the ion exchange resin, the diameter D of the holes in the lower perforated plate 9, which are arranged in the same way as the holes in the upper perforated plate and are aligned in the vertical direction, is smaller than that of the upper perforated plate.
通常、イオン交換樹脂の粒径は0.3〜1.2mm程度
であるため、上部多孔板の孔4′の直径は約20mm、
網材の網目6′は一辺が約0.2mmの正方形であるの
に対し本案の下部多孔板の孔径Dは約4mmであ
る。 Normally, the particle size of ion exchange resin is about 0.3 to 1.2 mm, so the diameter of the holes 4' in the upper perforated plate is about 20 mm.
The mesh 6' of the mesh material is a square with each side of about 0.2 mm, whereas the hole diameter D of the lower perforated plate of the present invention is about 4 mm.
そして、好ましくは下部多孔板9の孔は板の下
面での直径が上記の様に小さく、板の上面では上
部多孔板4の孔4′と直径が同じか、或いはそれ
より大きくし、これによつて処理水を下向流で通
水する集水時の水頭損失の増大を可及小さくす
る。このため第3図の実施例は下部多孔板の孔は
板の上面から途中までは上部多孔板の孔と同径の
円筒部8a、その下に下向きに直径が減小するテ
ーパ部8b、テーパ部8bの中心に直径Dの板下
面に開通した小径円筒部8cを有し、又、第4図
の実施例の孔は板上面の直径が上部多孔板の孔
4′と同じ、板下面の直径がDのテーパ部8dか
らなる。 Preferably, the diameter of the holes in the lower perforated plate 9 on the lower surface of the plate is small as described above, and on the upper surface of the plate, the diameter is the same as or larger than that of the holes 4' in the upper perforated plate 4. Therefore, the increase in water head loss during collection when the treated water is passed in a downward flow is minimized. Therefore, in the embodiment shown in FIG. 3, the holes in the lower perforated plate have a cylindrical portion 8a having the same diameter as the hole in the upper perforated plate from the upper surface of the plate to the middle, a tapered portion 8b whose diameter decreases downward, and a tapered portion 8b below which has the same diameter as the hole in the upper perforated plate. The center of the portion 8b has a small diameter cylindrical portion 8c with a diameter D open to the lower surface of the plate, and the hole in the embodiment shown in FIG. It consists of a tapered portion 8d with a diameter of D.
これによつて処理水を得る集水時、下部多孔板
の孔が上部多孔板と同直径のものに較べ僅かに水
頭損失は上昇するが、閉塞は起らず、逆洗の際の
散水時は下部多孔板の孔の直径Dなる小径部から
逆洗水が集散水装置上に支持されているイオン交
換樹脂の充填層中に集散水装置の全面から均等に
上向きに噴出し、充填層を均等に洗浄してイオン
交換樹脂の性能を一様に回復する。尚、水頭損失
が僅かに上昇するだけで集水できる理由は上部多
孔板の孔4′は従来通り大きく且つ下部多孔板の
孔は下向きに直径が小さくなつたテーパ部8b,
8dを有して板の上面では大きく、板の下面では
小さくなつているので水頭損失には孔径すべてを
小さくするときの様な大きな影響は無い。この実
施例の様に上部多孔板の孔4′の径20mm、下部多
孔板の孔の径4mmの場合、計算によると孔Dの部
分の流速は0.5m/sec、縮流及び拡散による圧力
損失0.023mmAg程度で、差圧増加分は微小でしか
ないからで、むしろ、孔Dの径よりも集散水板全
体に開けられた集散水孔の数の方が水頭損失に及
ぼす影響は大きいと言える。 As a result, when collecting treated water, the head loss is slightly higher than when the holes in the lower perforated plate have the same diameter as the upper perforated plate, but no blockage occurs, and when water is sprinkled during backwashing. Backwash water is spouted upwards evenly from the entire surface of the water collector into the packed bed of ion exchange resin supported on the water collector and sprinkler from the small diameter part of the hole of the lower perforated plate, and the packed bed is Wash evenly to restore the performance of the ion exchange resin. The reason why water can be collected with only a slight increase in water head loss is that the holes 4' in the upper perforated plate are as large as before, and the holes in the lower perforated plate have a tapered portion 8b whose diameter decreases downward.
8d, which is large on the top surface of the plate and small on the bottom surface of the plate, so the head loss is not affected as much as when all the hole diameters are made small. As in this example, if the diameter of hole 4' in the upper perforated plate is 20 mm and the diameter of the hole in the lower perforated plate is 4 mm, the flow velocity at hole D is calculated to be 0.5 m/sec, and the pressure loss due to contraction and diffusion. This is about 0.023mmAg, and the increase in differential pressure is only minute.In fact, it can be said that the number of water collection holes drilled throughout the water collection and distribution plate has a greater influence on water head loss than the diameter of hole D. .
又、イオン交換樹脂の充填層が混床型の場合は
陽イオン交換樹脂と、陰イオン交換樹脂の完全分
離が行え、その結果、再生薬剤と逆洗洗浄水の使
用量が節約でき、次に処理水を得る際の純水純度
の向上を図ることができる。 In addition, when the ion exchange resin packed bed is a mixed bed type, the cation exchange resin and anion exchange resin can be completely separated, and as a result, the amount of regeneration agent and backwashing water used can be saved. It is possible to improve the purity of purified water when obtaining treated water.
こうして本考案によれば集水時と散水時の予盾
する要求を両方とも満足し、構造が簡単なため任
意の材質が選定でき、製作、加工が容易である等
の種々な特長を有する集散水装置を提供すること
ができる。尚、上下多孔板は孔を揃えた方が加工
の際、上下同時に孔あけできるので安価に製作で
きるが、必ずしも孔を揃える必要はない。 In this way, the present invention satisfies the requirements for protection during both water collection and water sprinkling, and has various features such as simple structure, any material can be selected, and easy manufacturing and processing. Water equipment can be provided. It should be noted that if the holes in the upper and lower perforated plates are aligned, the holes can be made at the same time on the upper and lower sides during processing, so they can be manufactured at a lower cost, but it is not always necessary to align the holes.
第1図はイオン交換塔の断面図、第2図は同上
に使用されている従来の集散水装置の一部の拡大
断面図、第3図は本考案による集散水装置の一実
施例の一部の拡大断面図、第4図は同じく本考案
の他の一実施例の集散水装置の一部の拡大断面図
で、図中、4は上部多孔板、4′はその孔、6は
網材、6′はその網目、9は下部多孔板、Dはそ
の孔の直径を示す。
Figure 1 is a cross-sectional view of the ion exchange tower, Figure 2 is an enlarged cross-sectional view of a part of the conventional water collector and sprinkler used in the above, and Figure 3 is an example of an embodiment of the water collector and sprinkler according to the present invention. FIG. 4 is an enlarged sectional view of a part of the water collection and distribution device according to another embodiment of the present invention, in which 4 is the upper perforated plate, 4' is the hole thereof, and 6 is the mesh. 6' indicates the mesh, 9 indicates the lower perforated plate, and D indicates the diameter of the hole.
Claims (1)
径よりも小さい網目を有する網材を挟んだイオン
交換塔用集散水装置において、 上部多孔板の孔を充填層の粒径より大にし、
又、下部多孔板の孔には下向きに直径が小さくな
るテーパ部を設け、該孔の上面での直径を上部多
孔板の孔と同じか、それより大きくすると共に、
下面での直径を上部多孔板の孔よりも小さくした
ことを特徴とするイオン交換塔用集散水装置。[Scope of Claim for Utility Model Registration] In a water collection and distribution device for an ion exchange tower in which a mesh material having a mesh size smaller than the particle size of the packed bed supported above is sandwiched between upper and lower perforated plates, the holes in the upper perforated plate are larger than the particle size of the packed bed,
Further, the hole in the lower perforated plate is provided with a tapered part whose diameter decreases downward, and the diameter at the upper surface of the hole is made equal to or larger than that of the hole in the upper perforated plate,
A water collection and distribution device for an ion exchange tower, characterized in that the diameter at the bottom surface is smaller than the pores in the upper perforated plate.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP3480284U JPS60148031U (en) | 1984-03-13 | 1984-03-13 | Water collector and sprinkler device for ion exchange tower |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP3480284U JPS60148031U (en) | 1984-03-13 | 1984-03-13 | Water collector and sprinkler device for ion exchange tower |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS60148031U JPS60148031U (en) | 1985-10-01 |
JPH0125629Y2 true JPH0125629Y2 (en) | 1989-08-01 |
Family
ID=30538512
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP3480284U Granted JPS60148031U (en) | 1984-03-13 | 1984-03-13 | Water collector and sprinkler device for ion exchange tower |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS60148031U (en) |
Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS4944031U (en) * | 1972-07-20 | 1974-04-18 | ||
JPS5835740A (en) * | 1981-08-25 | 1983-03-02 | Nec Corp | Optical head |
-
1984
- 1984-03-13 JP JP3480284U patent/JPS60148031U/en active Granted
Patent Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS4944031U (en) * | 1972-07-20 | 1974-04-18 | ||
JPS5835740A (en) * | 1981-08-25 | 1983-03-02 | Nec Corp | Optical head |
Also Published As
Publication number | Publication date |
---|---|
JPS60148031U (en) | 1985-10-01 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CA1290704C (en) | Air/water distributor underdrain | |
EP2711340B1 (en) | Ion exchanging apparatus | |
JPH0125629Y2 (en) | ||
US20020166807A1 (en) | Underdrain filtration system with stamped perforations | |
CA2016404C (en) | Underdrain strainer assembly | |
CN211837001U (en) | SOx/NOx control dust removal integrated device | |
CN210936169U (en) | High-efficient belt cleaning device is used to agricultural machine | |
JP4593086B2 (en) | Filtration device | |
JPH053040Y2 (en) | ||
CN211972960U (en) | Ecological permeable road for garden construction | |
JPH027611Y2 (en) | ||
CN213760635U (en) | Prevent running valveless filter of material | |
JPS6341066Y2 (en) | ||
JPS6321315Y2 (en) | ||
CN213132069U (en) | Horizontal filtering sand cylinder | |
JP2001252576A (en) | Ion exchange resin tower and liquid treating device | |
JP2592777B2 (en) | Filtration tank | |
JPS6355967B2 (en) | ||
JP3710614B2 (en) | Liquid processing tower | |
JPH063442U (en) | Liquid collection structure in packed tower | |
JPS6341058Y2 (en) | ||
JPH0626348Y2 (en) | Ion exchange tower | |
JPH0824823B2 (en) | Hollow fiber module | |
JPH0487793U (en) | ||
JPS646912Y2 (en) |