JPS6113074Y2 - - Google Patents
Info
- Publication number
- JPS6113074Y2 JPS6113074Y2 JP1982067858U JP6785882U JPS6113074Y2 JP S6113074 Y2 JPS6113074 Y2 JP S6113074Y2 JP 1982067858 U JP1982067858 U JP 1982067858U JP 6785882 U JP6785882 U JP 6785882U JP S6113074 Y2 JPS6113074 Y2 JP S6113074Y2
- Authority
- JP
- Japan
- Prior art keywords
- flow
- fluid
- water
- treated
- large number
- 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 18
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 18
- 239000000969 carrier Substances 0.000 claims description 6
- 230000005484 gravity Effects 0.000 claims description 6
- 238000005192 partition Methods 0.000 claims description 5
- 230000004308 accommodation Effects 0.000 claims description 4
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 2
- 239000007789 gas Substances 0.000 description 2
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 239000010800 human waste Substances 0.000 description 1
- 239000010842 industrial wastewater Substances 0.000 description 1
- 238000005342 ion exchange Methods 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 239000011347 resin Substances 0.000 description 1
- 229920005989 resin Polymers 0.000 description 1
- 239000010865 sewage Substances 0.000 description 1
- 239000010802 sludge Substances 0.000 description 1
- 238000001179 sorption measurement Methods 0.000 description 1
- 238000004065 wastewater treatment Methods 0.000 description 1
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/10—Biological treatment of water, waste water, or sewage
Landscapes
- Biological Treatment Of Waste Water (AREA)
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
- Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
Description
【考案の詳細な説明】
本考案は、廃水処理用流動床、イオン交換塔、
活性炭吸着塔などの反応塔型水処理装置やガス反
応塔装置への流体供給流路途中に介装する流体用
デイストリビユータに関する。[Detailed description of the invention] The invention is based on a fluidized bed for wastewater treatment, an ion exchange tower,
The present invention relates to a fluid distributor installed in a fluid supply flow path to a reaction tower type water treatment device such as an activated carbon adsorption tower or a gas reaction tower device.
従来のデイストリビユータは、流路を構成する
管路内に、それを横断する方向に分散させて一個
又は複数個の遮蔽部材を設け、流動流体を分散さ
せるか、又は槽内への流入箇所を横断面方向に等
間隔になるように多数設けて横断面方向で均一な
流動状態が得られるように構成するものであつ
た。 Conventional distributors provide one or more shielding members distributed in the transverse direction within the pipe constituting the flow path to disperse the flowing fluid or to prevent the flowing fluid from flowing into the tank. The structure was such that a large number of the fluids were provided at equal intervals in the cross-sectional direction so that a uniform flow state could be obtained in the cross-sectional direction.
ところが、デイストリビユータへの流入箇所に
おいて、管路の中心側程流速が大になることを前
提として、それら流体を均流化するように遮蔽部
材を配置するものであり、流入箇所での流速分布
が乱れた場合には均流化が不良となる欠点があつ
た。又、流入箇所を多数個設けた場合でも、個々
の流出難易により流速の不均衡を生じる欠点があ
つた。 However, at the point where the fluid flows into the distributor, it is assumed that the flow velocity increases toward the center of the pipe, and a shielding member is arranged to equalize the flow of the fluid. There was a drawback that if the distribution was disturbed, flow equalization would be poor. Further, even when a large number of inflow points are provided, there is a drawback that the flow velocity becomes unbalanced due to the difficulty of each outflow.
本考案は、上記の点に鑑み、デイストリビユー
タへの流入箇所での流速分布の変化いかんにかか
わらず良好に均流化できるようにすることを目的
とする。 In view of the above points, it is an object of the present invention to enable good flow equalization regardless of changes in the flow velocity distribution at the point where the flow flows into the distributor.
次に、本考案の実施例を例示図に基いて詳述す
る。 Next, embodiments of the present invention will be described in detail based on illustrative drawings.
筒状の処理槽1の下方側にデイストリビユータ
2を設けると共に、デイストリビユータ2の上方
に生物膜付着担体3…の流動層4を形成し、か
つ、処理槽1の下部に被処理水の供給路5を、他
方、上部に処理済水の取出路6を夫々接続し、し
尿や都市下水あるいは産業廃水等の被処理水をデ
イストリビユータ2で均流化した後に担体3…に
接続させ、担体3に付着させた活性汚泥の作用に
より生物化学的酸素要求量を低減化するように水
処理装置を構成してある。 A distributor 2 is provided below the cylindrical treatment tank 1, a fluidized bed 4 of biofilm-attached carriers 3 is formed above the distributor 2, and the water to be treated is placed in the lower part of the treatment tank 1. On the other hand, a treated water outlet 6 is connected to the upper part, and after the water to be treated such as human waste, urban sewage, or industrial wastewater is equalized by the distributor 2, it is connected to the carrier 3... The water treatment device is configured so that the biochemical oxygen demand is reduced by the action of the activated sludge attached to the carrier 3.
前記デイストリビユータ2には、被処理水流動
方向視において格子状に、かつ、流路Rを横断す
る方向に並ぶ状態で仕切壁7…を設けて分割流路
r…が区画形成され、そして、仕切壁7…の上下
夫々にメツシユ8,8を設けて担体収容室9…を
形成すると共に、収容室9…夫々に、被処理水よ
りもやや比重の大きい担体10の多数を収容して
ある。 The distributor 2 is provided with partition walls 7 arranged in a grid pattern in the direction of flow of the water to be treated and arranged in a direction crossing the flow path R to form divided flow paths r. Meshes 8, 8 are provided on the upper and lower sides of the partition walls 7, respectively, to form carrier storage chambers 9, and each of the storage chambers 9 accommodates a large number of carriers 10 having a specific gravity slightly larger than that of the water to be treated. be.
前記担体10…は、収容室9…夫々に対して互
いに等しいあるいはほぼ等しい占有率で、かつ、
内部での相対流動を許容する状態で収容されてい
る。 The carriers 10 occupy the respective storage chambers 9 at equal or approximately equal occupancy rates, and
It is housed in a state that allows relative flow inside.
従つて、流動の大きい分割流路rでは、第3図
のイに示すように、被処理水の圧力によつてメツ
シユ8に押し付けられる担体10…の量が多くな
つて流路rに沿う方向に長い固定床が形成される
状態となり、大きな流動抵抗を受けさせ、他方、
流速の小さい流路rでは、第3図のロに示すよう
に、上述の場合とは逆に、流路rに沿う方向に短
い固定床が形成される状態に、あるいは、ほとん
ど固定床が形成されない状態となり、被処理水に
付与される流動抵抗が減少し、流速分布いかんに
かかわらず、分割流路r…を経た後の被処理水の
流速を互いに均一化するのである。又、デイスト
リビユータ2に入る前の流速分布が変化しても、
上記作用が各収容室9…において起り、連続的に
均一化した流速が得られるのである。 Therefore, in the divided flow path r where the flow is large, as shown in FIG. This results in the formation of a long fixed bed, subjecting it to large flow resistance, and on the other hand,
In the flow path r where the flow velocity is low, as shown in FIG. 3B, contrary to the above case, a short fixed bed is formed in the direction along the flow path r, or almost a fixed bed is formed. Therefore, the flow resistance applied to the water to be treated is reduced, and the flow velocity of the water to be treated after passing through the divided channels r is made uniform regardless of the flow velocity distribution. Also, even if the flow velocity distribution before entering the distributor 2 changes,
The above action occurs in each storage chamber 9, and a continuously uniform flow rate is obtained.
前記メツシユ8,8に代えて、金属製あるいは
樹脂製の網等、要するに、収容室9…から担体1
0…を流出させる事無く被処理水を通過させられ
るものであれば各種のものが採用でき、それらを
して網様体8と総称する。 Instead of the meshes 8, 8, metal or resin nets, etc., are used to connect the carrier 1 from the storage chamber 9...
Various types of reticular bodies 8 can be used as long as they allow the water to be treated to pass through without causing any 0 to flow out.
上記デイストリビユータ2は、担体10…とし
て被処理水の比重よりやや小さいものを収容室9
…に収容し、被処理水の下降流路の途中に設ける
ようにしても良い。 The distributor 2 has a carrier 10 that is slightly smaller than the specific gravity of the water to be treated in a storage chamber 9.
... and may be provided in the middle of the downward flow path of the water to be treated.
本考案は、液体のみならず気体の流路にも適用
できる。 The present invention can be applied not only to liquid channels but also to gas channels.
以上要するに、本考案による流体用デイストリ
ビユータは、流体R途中に、それを横断する方向
に仕切壁7…を並設して多数の分割流路r…を区
画形成すると共に、前記分割流路r…夫々におい
て、流体の通過を許容する網様体8をその上下に
設けて担体収容室9を形成し、前記流体Rが上昇
流であるときは被処理水よりもやや比重の大きい
担体10の多数を、また前記流体Rが下降流であ
るときは被処理水よりもやや比重の小さい担体1
0の多数を、前記収容室9…夫々に、前記収容室
9内での流動を許容する状態で収容してある事を
特徴とする。 In summary, the fluid distributor according to the present invention has partition walls 7 disposed in parallel in the middle of the fluid R in a direction transverse thereto to form a large number of divided flow paths r. In each of r..., a carrier storage chamber 9 is formed by providing a net-like body 8 above and below that allows passage of the fluid, and when the fluid R is in an upward flow, a carrier 10 having a specific gravity slightly larger than that of the water to be treated is provided. When the fluid R is flowing downward, the carrier 1 has a specific gravity slightly smaller than that of the water to be treated.
0 are accommodated in each of the accommodation chambers 9 in a state that allows them to flow within the accommodation chambers 9.
つまり、流速の大きい流路rでは、その流体の
圧力によつて流動方向下手側の網様体8に対して
押圧される担体10…の量が多くなり、他方、流
速の小さい流路rでは、網様体8に対して押圧さ
れる担体10…の量が少なくなり、デイストリビ
ユータ2への流入箇所での流速分布に応じ、自ず
と流動抵抗に差を生じさせ、流速の大きい流路r
側での流動を抑えて流速の小さい流路r側へ流れ
込ませることができ、デイストリビユータ2への
流入箇所での流速分布の変化いかんにかかわら
ず、良好に均流化できるようになつた。 In other words, in the channel r where the flow velocity is high, the amount of carriers 10 that are pressed against the mesh body 8 on the downstream side in the flow direction by the pressure of the fluid increases, while in the channel r where the flow velocity is low. , the amount of the carrier 10 pressed against the net-like body 8 is reduced, which naturally causes a difference in flow resistance depending on the flow velocity distribution at the point where it flows into the distributor 2, and the flow path r where the flow velocity is high.
It is possible to suppress the flow on the side and direct the flow to the flow path r side where the flow velocity is low, and it has become possible to achieve good flow equalization regardless of changes in the flow velocity distribution at the point where it flows into the distributor 2. .
図面は本考案に係る流体用デイストリビユータ
の実施例を示し、第1図は水処理装置の概略縦断
面図、第2図は第1図の−線断面図、第3図
はイ,ロは作用説明図である。
7……仕切壁、8……網様体、9……担体収容
室、10……担体、R……流路、r……分割流
路。
The drawings show an embodiment of the fluid distributor according to the present invention, in which Fig. 1 is a schematic longitudinal cross-sectional view of a water treatment device, Fig. 2 is a cross-sectional view taken along the - line in Fig. 1, and Fig. 3 is a cross-sectional view of the water treatment device. is an action explanatory diagram. 7... Partition wall, 8... Net-like body, 9... Carrier storage chamber, 10... Carrier, R... Channel, r... Divided channel.
Claims (1)
…を並設して多数の分割流路r…を区画形成する
と共に、前記分割流路r…夫々において、流体の
通過を許容する網様体8をその上下に設けて担体
収容室9を形成し、前記流体Rが上昇流であると
きは被処理水よりもやや比重の大きい担体10の
多数を、また前記流路Rが下降流であるときは被
処理水よりもやや比重の小さい担体10の多数
を、前記収容室9…夫々に、前記収容室9内での
流動を許容する状態で収容してある事を特徴とす
る流体用デイストリビユータ。 A partition wall 7 is installed in the middle of the flow path R in a direction that crosses it.
are arranged in parallel to form a large number of divided channels r..., and in each of the divided channels r..., net-like bodies 8 that allow passage of fluid are provided above and below to form a carrier storage chamber 9. When the fluid R is an upward flow, a large number of carriers 10 having a specific gravity slightly larger than that of the water to be treated are used, and when the flow path R is a downward flow, a large number of carriers 10 having a specific gravity slightly lower than that of the water to be treated are used. A fluid distributor characterized in that a large number of fluids are accommodated in each of the accommodation chambers 9 in a state that allows flow within the accommodation chambers 9.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP1982067858U JPS58171229U (en) | 1982-05-10 | 1982-05-10 | Fluid distributor |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP1982067858U JPS58171229U (en) | 1982-05-10 | 1982-05-10 | Fluid distributor |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS58171229U JPS58171229U (en) | 1983-11-15 |
JPS6113074Y2 true JPS6113074Y2 (en) | 1986-04-23 |
Family
ID=30077661
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP1982067858U Granted JPS58171229U (en) | 1982-05-10 | 1982-05-10 | Fluid distributor |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS58171229U (en) |
-
1982
- 1982-05-10 JP JP1982067858U patent/JPS58171229U/en active Granted
Also Published As
Publication number | Publication date |
---|---|
JPS58171229U (en) | 1983-11-15 |
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