JPH04137707U - Solid-liquid separation device using vortex flow - Google Patents
Solid-liquid separation device using vortex flowInfo
- Publication number
- JPH04137707U JPH04137707U JP8912591U JP8912591U JPH04137707U JP H04137707 U JPH04137707 U JP H04137707U JP 8912591 U JP8912591 U JP 8912591U JP 8912591 U JP8912591 U JP 8912591U JP H04137707 U JPH04137707 U JP H04137707U
- Authority
- JP
- Japan
- Prior art keywords
- water
- solid
- liquid separation
- flow
- separation device
- 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
Links
- 239000007788 liquid Substances 0.000 title claims abstract description 11
- 238000000926 separation method Methods 0.000 title claims description 20
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 36
- 239000007787 solid Substances 0.000 claims abstract description 9
- 230000000903 blocking effect Effects 0.000 claims abstract description 5
- 239000010842 industrial wastewater Substances 0.000 abstract description 2
- 239000010865 sewage Substances 0.000 abstract description 2
- 239000010419 fine particle Substances 0.000 description 7
- 230000005484 gravity Effects 0.000 description 3
- 239000004576 sand Substances 0.000 description 3
- 238000010586 diagram Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 238000005406 washing Methods 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 238000004062 sedimentation Methods 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
Abstract
(57)【要約】
【目的】 上下水、産業排水等に含有されている懸濁物
質を、生起される渦流によつて捕捉する固液分離装置に
関する。
【構成】 孔径とピツチを同一にすることによつて均等
な通過面積を持つ通水孔を多数設けた流路を阻止する手
段を、懸濁物質を含有する被処理水の流速方向にほぼ直
交する面内に、適宜間隔を置いて平行にかつ複数段に配
設した。
(57) [Summary] [Purpose] This invention relates to a solid-liquid separator that captures suspended solids contained in water, sewage, industrial wastewater, etc. using the generated eddies. [Structure] A means for blocking a flow path, which has a large number of water passage holes with an equal passage area by making the hole diameter and pitch the same, is arranged almost perpendicular to the flow velocity direction of the water to be treated containing suspended solids. They were arranged parallel to each other in multiple stages at appropriate intervals within the same plane.
Description
【0001】0001
この考案は、上下水、産業排水等に含有されている懸濁物質を、生起される渦 流によつて捕捉する固液分離装置に関するものである。 This idea removes suspended solids contained in water, sewage, industrial wastewater, etc. by the vortex generated. The present invention relates to a solid-liquid separator that captures a stream.
【0002】0002
従来、被処理水に含有される懸濁物質の固液分離としては、微細粒子を重力沈 降を主に利用して分離する傾斜板方式が多数を占めていた。 Traditionally, solid-liquid separation of suspended solids contained in treated water has been carried out by gravity sedimentation of fine particles. The majority was the inclined plate method, which mainly used the rain to separate the parts.
【0003】0003
この場合、微細粒子は軽量なため重力沈降作用のみでは沈降時間が長くなり、 また分離容積も大きくなる欠点が生じていた。 In this case, since the fine particles are lightweight, settling due to gravity alone will take a long time to settle. Further, there was a drawback that the separation volume became large.
【0004】0004
そこで考案者等はこれらの欠点を除くため、孔径とピツチを同一にすることに よつて均等な通過面積を持つ通水孔を多数設けた流路を阻止する手段を、懸濁物 質を含有する被処理水の流速方向にほぼ直交する面内に、適宜間隔を置いて平行 にかつ複数段に配設したことを特徴とする渦流による固液分離装置を提案するも のである。 Therefore, in order to eliminate these drawbacks, the inventors decided to make the hole diameter and pitch the same. Therefore, a means for blocking a flow path with a large number of water holes with a uniform passage area is Parallel at appropriate intervals in a plane almost perpendicular to the flow velocity direction of the water to be treated containing water. We also propose a solid-liquid separation device using vortex flow, which is characterized by being arranged in multiple stages. It is.
【0005】[0005]
次にこの考案を添付図面にしたがつて詳細に説明する。 従来は図1に示すように水流に対してほぼ直交する面内に、適宜間隔をおいて 配設された、複数のフイン13により生起される渦流現象を利用し、重力の作用 に加えて、流体抗力や慣性力の作用をも推進力とした強制的かつ動的固液分離手 段を先に提案したが、この考案はこの渦流による分離現象をさらに発展した固液 分離装置を提供することを目的とする。 Next, this invention will be explained in detail with reference to the accompanying drawings. Conventionally, as shown in Figure 1, water is placed at appropriate intervals in a plane that is almost perpendicular to the water flow. By utilizing the vortex phenomenon caused by the plurality of fins 13 arranged, the action of gravity is In addition to this, a forced and dynamic solid-liquid separation method that uses fluid drag and inertial force as a driving force is also available. Although the stage was first proposed, this idea is a further development of the solid-liquid separation phenomenon caused by this vortex flow. The purpose is to provide a separation device.
【0006】 この考案の一実施例として、図1は懸濁物質を含有する被処理水1に凝集剤2 を注入して、混合槽3で急速攪拌して形成させた微細フロツクを有する混合水6 を、多数の小孔が一面に穿設される整流板4を通して層流状態にして、流路阻止 手段である、後述する分離槽5で渦流現象による固液分離を行なつて、流出水7 として処理するプロセスを示している。[0006] As an example of this invention, FIG. Mixed water 6 having fine flocs formed by injecting and rapidly stirring in mixing tank 3 is made into a laminar flow state through a rectifier plate 4 with many small holes perforated on one side, and the flow path is blocked. Solid-liquid separation is performed by a vortex phenomenon in a separation tank 5, which will be described later, and the effluent water 7 is It shows the process to be processed as follows.
【0007】 前述した固液分離槽5は、図2、図3のこの考案の実施例に示すように、微細 粒子を含有する混合水6の流路内に、多数の通水孔8を有する複数の多孔板9が 、流速方向にほぼ直交する面内に適宜間隔10を置いて、平行かつ複数列配設さ れて形成されている。[0007] The above-mentioned solid-liquid separation tank 5 has fine particles as shown in the embodiment of this invention shown in FIGS. 2 and 3. A plurality of perforated plates 9 having a large number of water passage holes 8 are provided in the flow path of the mixed water 6 containing particles. , arranged in parallel in multiple rows at appropriate intervals of 10 in a plane substantially perpendicular to the flow velocity direction. It is formed by
【0008】 通水孔8を通過した混合水6は、混合水量と多孔板9の通水孔8の孔径とピツ チにより決まる通水孔8の流速と、多孔板9相互の間隔10によつて生起される 渦流11によつて、懸濁物質が各多孔板9上に分離捕捉される。さらに凝集性懸 濁質の場合には、既に沈積している懸濁質12との接触によつても、微細粒子の 捕捉が促進される。[0008] The mixed water 6 that has passed through the water holes 8 is determined by the amount of mixed water, the hole diameter of the water holes 8 of the perforated plate 9, and the diameter of the water holes 8 of the perforated plate 9. This is caused by the flow velocity of the water passage holes 8 determined by the The vortex 11 separates and traps suspended matter on each perforated plate 9. In addition, cohesive In the case of suspended solids, contact with suspended solids 12 that has already settled may also cause fine particle formation. Acquisition is facilitated.
【0009】 この考案は混合水6の流速方向が多孔板9の面に対して垂直方向が最も望まし いのであるが、排泥手段(排出通路8’)を考慮した図7の山形形状、図8の谷 形形状、その他図9の湾曲形状等でもよく、またこれらの複合形や類似する形式 で渦流が生起されるものであれば差し支えない。[0009] In this design, it is most desirable that the flow velocity direction of the mixed water 6 is perpendicular to the surface of the perforated plate 9. However, the chevron shape in Figure 7 and the valley in Figure 8 take into consideration the mud removal means (discharge passage 8'). It may be a curved shape as shown in Figure 9, or a combination of these shapes or similar shapes. There is no problem as long as a vortex is generated.
【0010】 また混合水6の流入方向については、上向流又は下向流や横向流についても、 同様の渦流現象を生じれば差し支えない。0010 Regarding the inflow direction of the mixed water 6, also regarding the upward flow, the downward flow, or the horizontal flow. There is no problem if a similar vortex phenomenon occurs.
【0011】 更に分離槽5の形状は、図7ないし図9に示すように、中空の立方体や、中空 の六角柱体等の上下面に通水孔8を設けたモジユ−ルを、又はその側壁が貫通状 態とされるモジユ−ルを、あるいはそれらのブロツク化したものを、縦横に積載 したものであつても、同様の分離現象を有するものであれば、もちろん可能であ る。[0011] Furthermore, the shape of the separation tank 5 may be a hollow cube or a hollow cube, as shown in FIGS. 7 to 9. A module with water holes 8 on the upper and lower surfaces of a hexagonal prism, etc., or a module with a through-shaped side wall. Modules or their blocks are stacked vertically and horizontally. Of course, it is possible even if the separation phenomenon is similar. Ru.
【0012】 なお通水孔8の形状は、円形、角形等、要するに通過流に対して渦流を生じる 形状であれば、拘束されるものではない。0012 Note that the shape of the water passage hole 8 is circular, square, etc., in short, it creates a vortex flow with respect to the passing flow. As long as it has a shape, there are no restrictions.
【0013】 洗浄については、懸濁物質が除去され多孔板9上に載積した懸濁質は、分離後 の流出水7あるいは別途の洗浄水を逆方向に流下させることによつて、濃縮フロ ツクは順次に通水孔8から容易に除去され、整流板4を下方に通過した後、排出 用孔20(図1に示す)から排出される。なお、図7、図8においては排出通路 8’を通つてフロツクが排出される。[0013] Regarding washing, suspended solids are removed and the suspended solids loaded on the perforated plate 9 are washed after separation. By flowing the effluent water 7 or separate washing water in the opposite direction, the concentrated flow The water is easily removed from the water holes 8 one after another, and after passing through the current plate 4 downward, it is discharged. It is discharged through the use hole 20 (shown in FIG. 1). In addition, in Figures 7 and 8, the discharge passage The floc is discharged through 8'.
【0014】 この考案は既存の砂ろ過槽の前段に用いれば、砂ろ過槽の負荷を大幅に軽減で き、被処理水の濁度の変動に体しても緩衝作用の役目をなし、砂ろ過槽の寿命を 長持ちさせることができる。[0014] If this idea is used in the front stage of an existing sand filter tank, it can significantly reduce the load on the sand filter tank. It also acts as a buffer against fluctuations in the turbidity of the water being treated, extending the life of the sand filter tank. It can last a long time.
【0015】[0015]
この考案は以上のように、全く新しい渦流による微細粒子の強制分離、それに 加えて沈積微細粒子との接触による捕捉促進による分離装置なので、特に微細な 粒子の分離にすぐれており、装置のモジユ−ル化、ブロツク化も図ることが可能 である等の効果を有する。 As mentioned above, this idea is based on the forced separation of fine particles using a completely new vortex flow, and In addition, since it is a separation device that promotes capture through contact with deposited fine particles, it is particularly effective against fine particles. Excellent in separating particles, and allows equipment to be made into modules or blocks. It has the following effects.
【図1】この考案を示す処理系統図である。FIG. 1 is a processing system diagram showing this invention.
【図2】その渦流分離状態を示す概略説明図である。FIG. 2 is a schematic explanatory diagram showing the vortex separation state.
【図3】多孔板配置の斜視図である。FIG. 3 is a perspective view of a perforated plate arrangement.
【図4】使用可能な中空立方体形の流路阻止手段の斜視
図である。FIG. 4 is a perspective view of a usable hollow cube-shaped flow path blocking means;
【図5】同様の中空六角柱体の手段を示す斜視図であ
る。FIG. 5 is a perspective view of a similar hollow hexagonal prism means;
【図6】前記図4、図5に示すものの縦断面図である。FIG. 6 is a longitudinal cross-sectional view of what is shown in FIGS. 4 and 5. FIG.
【図7】この考案の他の実施例を示す概略縦断面図であ
る。FIG. 7 is a schematic vertical sectional view showing another embodiment of the invention.
【図8】この考案の他の実施例を示す概略縦断面図であ
る。FIG. 8 is a schematic vertical sectional view showing another embodiment of the invention.
【図9】この考案の他の実施例を示す概略縦断面図であ
る。FIG. 9 is a schematic longitudinal sectional view showing another embodiment of the invention.
【図10】従来の渦流による分離を示した概略縦断面図
である。FIG. 10 is a schematic vertical cross-sectional view showing separation by conventional vortex flow.
1 被処理水 2 凝集剤 3 混合槽 4 整流板 5 分離槽 6 混合水 7 流出水 8 通水孔 9 多孔板 10 適宜間隔 11 渦流 12 懸濁質 13 フイン 1 Water to be treated 2 Flocculant 3 Mixing tank 4 Current plate 5 Separation tank 6 Mixed water 7 Runoff water 8 Water hole 9 Perforated plate 10 Appropriate intervals 11 Eddy current 12 Suspended matter 13 Finn
Claims (2)
均等な通過面積を持つ通水孔を多数設けた流路を阻止す
る手段を、懸濁物質を含有する被処理水の流速方向にほ
ぼ直交する面内に、適宜間隔を置いて平行にかつ複数段
に配設したことを特徴とする渦流による固液分離装置。Claim 1: A means for blocking a flow path in which a large number of water passage holes having an equal passage area by making the hole diameter and pitch the same is provided in the flow velocity direction of the water to be treated containing suspended solids. A solid-liquid separation device using a vortex flow, characterized in that a plurality of stages are arranged in parallel at appropriate intervals in substantially orthogonal planes.
する手段が多孔板であることを特徴とする請求項1記載
の渦流による固液分離装置。2. A solid-liquid separation device using a vortex flow according to claim 1, wherein the means for blocking the flow path having a large number of water holes is a perforated plate.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP8912591U JPH0618562Y2 (en) | 1991-10-04 | 1991-10-04 | Solid-liquid separation device using vortex flow |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP8912591U JPH0618562Y2 (en) | 1991-10-04 | 1991-10-04 | Solid-liquid separation device using vortex flow |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH04137707U true JPH04137707U (en) | 1992-12-22 |
JPH0618562Y2 JPH0618562Y2 (en) | 1994-05-18 |
Family
ID=31930928
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP8912591U Expired - Lifetime JPH0618562Y2 (en) | 1991-10-04 | 1991-10-04 | Solid-liquid separation device using vortex flow |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH0618562Y2 (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2002239305A (en) * | 2001-02-14 | 2002-08-27 | Toyota Motor Corp | Coolant filtering method and apparatus therefor |
-
1991
- 1991-10-04 JP JP8912591U patent/JPH0618562Y2/en not_active Expired - Lifetime
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2002239305A (en) * | 2001-02-14 | 2002-08-27 | Toyota Motor Corp | Coolant filtering method and apparatus therefor |
JP4578696B2 (en) * | 2001-02-14 | 2010-11-10 | トヨタ自動車株式会社 | Coolant filtration method and apparatus |
Also Published As
Publication number | Publication date |
---|---|
JPH0618562Y2 (en) | 1994-05-18 |
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