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JP2008149308A - Wastewater purification apparatus - Google Patents

Wastewater purification apparatus Download PDF

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JP2008149308A
JP2008149308A JP2006357322A JP2006357322A JP2008149308A JP 2008149308 A JP2008149308 A JP 2008149308A JP 2006357322 A JP2006357322 A JP 2006357322A JP 2006357322 A JP2006357322 A JP 2006357322A JP 2008149308 A JP2008149308 A JP 2008149308A
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type filter
filter
belt conveyor
spring
accordion
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Kimihiko Okanoe
公彦 岡上
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Abstract

<P>PROBLEM TO BE SOLVED: To provide a wastewater purification apparatus which can enhance a back washing efficiency and can realize microfiltration in a small area by using an accordion-type filter. <P>SOLUTION: An accordion-type filter 11 is constructed hollow-cylindrically and stretchably in an accordion-like folded form. The accordion-type filter 11 is installed in a folded state by utilizing the force of a spring 14 in a normal state. In back washing, the filter 11 is stretched against the force of the spring 14. Thus, the back washing effect can be enhanced, and the deposit on the surface of the outer circumference of the filter 11 can be precipitated on a discharge belt conveyor 7. Consequently, the back washing effect can be enhanced, and microfiltration can be realized in a small area. <P>COPYRIGHT: (C)2008,JPO&INPIT

Description

この発明は、廃水を浄化する廃水浄化装置に関する。  The present invention relates to a wastewater purification device that purifies wastewater.

従来の逆洗式フイルタは、濾紙を折畳んでリング状に配置し、廃水の浄化時には外周表面から内部方向に廃水を流通させ、逆洗時には内部から外周表面方向に浄化時の2倍以上の流速で浄化水を流して逆洗していた。
また、従来の他の逆洗式フイルタは、つる巻き状バネを用い、廃水の浄化時にはつる巻き状バネの外周表面から内部方向に廃水を流通させ、逆洗時には内部から外周表面方向に浄化水を流して、ばねを伸ばして逆洗していた。
The conventional backwash type filter folds the filter paper and arranges it in a ring shape. When purifying the wastewater, the wastewater flows from the outer peripheral surface to the inner direction. It was backwashed with purified water at a flow rate.
In addition, other conventional backwash type filters use a helical spring, and when purifying wastewater, the wastewater is circulated inward from the outer peripheral surface of the helical spring, and during backwashing, purified water is passed from the inside toward the outer peripheral surface. The back was washed by extending the spring.

発明が解決しょうとする課題Problems to be solved by the invention

従来の逆洗式フイルタは、上記の如く構成され、濾紙を折畳んでリング状に配置したものは、精密濾過は可能であるが、逆洗効果は殆どなく、直ぐにフイルタが目詰まりを起こし実情にそぐわない。
一方、つる巻き状バネを用いたものは、逆洗効果は得られるが、通水面積が少なく、かつ、精密濾過は殆ど不可能であり実情にそぐわない。
The conventional backwash type filter is constructed as described above, and the filter paper folded and arranged in a ring shape can be microfiltered, but there is almost no backwashing effect, and the filter is immediately clogged. It does n’t fit.
On the other hand, a device using a helical spring can provide a backwashing effect, but has a small water flow area and is almost impossible to perform microfiltration, which is not suitable for the actual situation.

この発明は、蛇腹式フイルタを、例えば、濾紙、もしくは、濾布を、中空筒状に、かつ、伸縮自在に蛇腹状に折畳んで構成し、常時は、ばね力により折畳んだ状態で設置し、逆洗時には、ばね力に抗して蛇腹式フイルタを伸ばすことにより、逆洗効果を高めると共に、小面積で精密濾過が可能な廃水浄化装置を提供することを目的とする。  The present invention comprises a bellows type filter, for example, a filter paper or a filter cloth, which is folded in a hollow cylindrical shape and a bellows shape that can be expanded and contracted, and is normally installed in a state folded by a spring force. And at the time of backwashing, it aims at providing the waste water purification apparatus which can raise a backwashing effect by extending a bellows type filter against a spring force, and can perform microfiltration with a small area.

上記課題解決手段は、廃水が注ぎ込まれる浄化槽内に、沈殿物を浄化槽外に排出するベルトコンベアと、中空筒状に、かつ、伸縮自在に蛇腹状に折畳まれて構成され、常時はバネ力により折畳まれ、外周表面から内部方向に廃水を通過させて浄化する蛇腹式フイルタを備え、逆洗時には蛇腹式フイルタの内部から外周表面方向に逆流させて、バネ力に抗して蛇腹式フイルタを伸ばすようにして構成した。  The means for solving the above problems are configured in a septic tank into which waste water is poured, a belt conveyor that discharges precipitates to the outside of the septic tank, a hollow cylinder, and a bellows that is telescopically folded. The bellows type filter that is folded by the inner surface and purifies by passing waste water from the outer peripheral surface to the inside, and backwashing from the inside of the bellows type filter to the outer surface during backwashing, resisting the spring force It was configured to stretch.

以下この発明の実施の形態を図1及び図2に基づいて説明する。
図1は、この発明の一実施例を示す側面断図、図2は、図1の正面断面図で、図において、工作機1からの廃液2は、吸着剤収納容器3を介して浄化槽4のダーティタンク5内に注ぎ込まれる。
吸着剤収納容器3内には、水酸化マグネシュウムを主成分とする吸着剤6が、例えば、布袋に詰められて設置されており、水酸化マグネシュウムから廃液中に溶出するOH基により、廃液2のpH値を9〜10に保って廃液2の劣化を防ぐと共に、常時、廃液2中のマグネシュウムイオン濃度が10ppm程度になるように溶出して、廃水2中の微粒子の凝集作用を促進する。
An embodiment of the present invention will be described below with reference to FIGS.
1 is a side sectional view showing an embodiment of the present invention, FIG. 2 is a front sectional view of FIG. 1, and in the figure, waste liquid 2 from a machine tool 1 is passed through an adsorbent storage container 3 to a septic tank 4. It is poured into the dirty tank 5.
In the adsorbent storage container 3, an adsorbent 6 containing magnesium hydroxide as a main component is placed, for example, in a cloth bag, and the waste liquid 2 is removed by OH groups eluted from the magnesium hydroxide into the waste liquid. While maintaining the pH value at 9 to 10 to prevent the waste liquid 2 from deteriorating, it always elutes so that the magnesium ion concentration in the waste liquid 2 is about 10 ppm to promote the aggregating action of the fine particles in the waste water 2.

図3は、水酸化マグネシュウムの電荷0ポイント特性を示し、横軸にpH値を、縦軸に濃度をとっており、電荷0ポイント:pH12より低いpH領域の液中においては、
Mg(OH)=Mg(OH)OHの平衡から、Mg(OH)が生じやすく、Mg(OH)の表面は+に帯電し、また、液中にはOHが多くなり塩基性を示す。
このため、廃液2のpH値は9〜10に保たれ、クーラント液・洗浄液等の劣化に伴うpH値の低下は阻止され、また、冷却配管中等の錆発生等の予防にも対応できる。
また、廃液2中の微粒子・微細油等は−に帯電しており、+に帯電したMg(OH)の表面に吸引されて、微粒子・微細油等のそれぞれの相互間距離は、互いに引力が働く距離よりも狭くなって凝集し、廃液2中の微粒子の沈殿速度を速め、微細油は液面に浮上する。
さらに、Mg(OH)は、常に廃液中のマグネシュウムイオン濃度が10ppm程度になるように、マグネシュウムイオン溶出する性状があり、このマグネシュウムイオンにより廃液中の微粒子の凝集作用を促進する。
FIG. 3 shows the charge zero point characteristics of magnesium hydroxide, the horizontal axis represents the pH value, and the vertical axis represents the concentration. Charge 0 point: In a liquid in a pH region lower than pH 12,
From the equilibrium of Mg (OH) 2 = Mg (OH) + OH , Mg (OH) + is likely to occur, the surface of Mg (OH) 2 is charged to +, and OH is increased in the liquid. Shows basicity.
For this reason, the pH value of the waste liquid 2 is maintained at 9 to 10, and a decrease in the pH value due to deterioration of the coolant liquid, the cleaning liquid, etc. is prevented, and it is possible to cope with the prevention of the occurrence of rust in the cooling pipes.
In addition, the fine particles, fine oil, etc. in the waste liquid 2 are charged to-, and are attracted to the surface of Mg (OH) 2 charged to +, and the mutual distances between the fine particles, fine oil, etc. are mutually attractive. Becomes narrower than the working distance, and agglomerates to increase the precipitation rate of the fine particles in the waste liquid 2, and the fine oil floats to the liquid surface.
Further, Mg (OH) 2 has a property of elution of magnesium ions so that the concentration of magnesium ions in the waste liquid is always about 10 ppm, and this magnesium ion promotes the aggregating action of fine particles in the waste liquid.

このようにして廃液2中の微粒子は、ダーティタンク5内に設置されたベルトコンベア7上に沈殿し、ダーティタンク5外に排出される。
ベルトコンベア7は、例えば、1分間の移動速度を10cmと非常にゆっくりと設定して、ベルトコンベア7上に沈殿堆積した微粒子を廃液2中に拡散させないようにする。
また、ベルトコンベア7に突起8を設け、この突起8がダーティタンク5の廃液2中から液面9外に出る際、突起8の上表面が液面9に対してほぼ平行状態になるように設け、突起8上に堆積した微粒子の廃液2中への拡散を防止する。
突起8の上表面の液面9に対する角度は、ほぼ平行状態が理想的であるが、突起8上に堆積した微粒子を掬い取るように、若干角度を持たせる必要が有る。
In this way, the fine particles in the waste liquid 2 settle on the belt conveyor 7 installed in the dirty tank 5 and are discharged out of the dirty tank 5.
For example, the belt conveyor 7 sets the moving speed for 1 minute as very slow as 10 cm so that the fine particles deposited on the belt conveyor 7 are not diffused into the waste liquid 2.
Further, a protrusion 8 is provided on the belt conveyor 7, and when the protrusion 8 comes out of the liquid surface 9 from the waste liquid 2 of the dirty tank 5, the upper surface of the protrusion 8 is substantially parallel to the liquid surface 9. Provided to prevent the fine particles deposited on the protrusions 8 from diffusing into the waste liquid 2.
The angle of the upper surface of the protrusion 8 with respect to the liquid surface 9 is ideally in a substantially parallel state, but it is necessary to have a slight angle so as to scavenge the fine particles deposited on the protrusion 8.

ベルトコンベア7上に沈殿しない微粒子は、ダーティタンク5内の廃液2と共に、ポンプ10によって蛇腹式フイルタ11を介してクリーンタンク12内に汲上げられ、蛇腹式フイルタ11の外周表面から内部方向に廃液2が流れ、蛇腹式フイルタ11の外周表面で濾過される。
蛇腹式フイルタ11は、濾紙もしくは濾布を中空筒状で、かつ、アコーデオン式、もしくは、小田原ちょうちん式に伸縮自在に蛇腹状に折畳まれて構成され、図4に示す如く、パンチングメタル等からなる間隙を多数有する容器13内に設置され、ばね14のばね力により、常時折畳んだ状態にされている。
逆洗時には、ポンプ10を逆回転させてクリーンタンク12内の浄化液を、蛇腹式フイルタ11の内部から外周表面方向に流し、図5に示す如く、ばね14のばね力に抗して蛇腹式フイルタ11を伸ばして逆洗を効果的に行う。
この逆洗でベルトコンベア7上に沈殿堆積した微粒子は、ベルトコンベア7によりダーティタンク5外に排出される。
このようにして浄化されたクリーンタンク12内の浄化水は、ポンプ15によって工作機1に送り込まれる。
The fine particles that do not settle on the belt conveyor 7 are pumped into the clean tank 12 by the pump 10 through the bellows filter 11 together with the waste liquid 2 in the dirty tank 5, and the waste liquid flows inward from the outer peripheral surface of the bellows filter 11. 2 flows and is filtered on the outer peripheral surface of the bellows type filter 11.
The bellows type filter 11 is configured by folding a filter paper or a filter cloth into a hollow cylindrical shape and an accordion type or an Odawara lantern in a bellows shape so as to be freely stretchable. As shown in FIG. It is installed in a container 13 having a large number of gaps, and is always folded by the spring force of the spring 14.
At the time of backwashing, the pump 10 is rotated in the reverse direction so that the cleaning liquid in the clean tank 12 flows from the inside of the bellows type filter 11 toward the outer peripheral surface, and the bellows type is resisted against the spring force of the spring 14 as shown in FIG. The filter 11 is extended to perform backwashing effectively.
The fine particles deposited and deposited on the belt conveyor 7 by this backwashing are discharged out of the dirty tank 5 by the belt conveyor 7.
The purified water in the clean tank 12 thus purified is sent to the machine tool 1 by the pump 15.

図6はこの発明の他の実施例を示す正面断面図で、突起8を、図7に示すように、ベルトコンベア7上の微粒子16を廃液2と共に掬い取るように、突起8の上表面が液面9に対して可也の角度になるように傾斜して設けられ、かつ、図8に示すように、ベルトコンベア7の幅方向に、液面9に対して、例えば、3度〜5度傾斜させて、微粒子16と共に掬い取られた廃液2を、ゆっくりと、かつ、微粒子16を廃液2中に拡散さないようにダーティタンク5内に戻す。
この場合、突起8のベルトコンベア7の幅方向の距離は長く、微粒子16と共に掬い取られた廃液2をゆっくりと、かつ、微粒子16を廃液2中に拡散させずにダーティタンク5内に戻すことができる。
FIG. 6 is a front sectional view showing another embodiment of the present invention. As shown in FIG. 7, the upper surface of the protrusion 8 is formed so that the fine particles 16 on the belt conveyor 7 are scooped together with the waste liquid 2 as shown in FIG. For example, 3 to 5 degrees with respect to the liquid level 9 in the width direction of the belt conveyor 7 as shown in FIG. The waste liquid 2 scooped together with the fine particles 16 is slowly returned to the dirty tank 5 so as not to diffuse the fine particles 16 into the waste liquid 2.
In this case, the distance of the protrusion 8 in the width direction of the belt conveyor 7 is long, and the waste liquid 2 scooped together with the fine particles 16 is slowly returned to the dirty tank 5 without diffusing the fine particles 16 into the waste liquid 2. Can do.

図9はこの発明のさらに他の実施例を示す正面断面図で、アジャスター17により、突起8のベルトコンベア7の幅方向への傾斜を付けている。
即ち、図2の実施例においてアジャスター17を設けることにより、図6の実施例の効果を得るものである。
FIG. 9 is a front sectional view showing still another embodiment of the present invention. The adjuster 17 inclines the protrusion 8 in the width direction of the belt conveyor 7.
That is, the effect of the embodiment of FIG. 6 is obtained by providing the adjuster 17 in the embodiment of FIG.

なお、上記実施例は、ばね14の押圧力によって蛇腹式フイルタ11を折畳んだが、ばね14の引っ張り力によって蛇腹式フイルタ11を折畳んでもよい。
即ち、例えば、ばね14を2個、ダーティタンク5の壁面上端部から吊り下げ、この2個のばね14のそれぞれの下端面に支持板の両端部を取り付け、この支持板に蛇腹式フイルタ11の下面を固定し、常時はばね14の引っ張り力によって蛇腹式フイルタ11を折畳み、逆洗時はばね14の引っ張り力に抗して蛇腹式フイルタ11を伸ばしてもよい。
さらに、ポンプ10を逆回転可能なポンプとして、濾過時、並びに、逆洗時とも、1台のポンプで対応したが、濾過時用のポンプと逆洗時用のポンプとを、それぞれ別個に設けても良い。
In the above embodiment, the bellows type filter 11 is folded by the pressing force of the spring 14, but the bellows type filter 11 may be folded by the pulling force of the spring 14.
That is, for example, two springs 14 are suspended from the upper end of the wall surface of the dirty tank 5, and both ends of the support plate are attached to the lower ends of the two springs 14, and the bellows type filter 11 is attached to the support plate. The lower surface may be fixed, and the bellows type filter 11 may be folded by the pulling force of the spring 14 at all times, and the bellows type filter 11 may be extended against the pulling force of the spring 14 during backwashing.
In addition, the pump 10 is a pump that can be rotated in reverse, and one pump is used for both filtration and backwashing. However, a pump for filtration and a pump for backwashing are provided separately. May be.

発明の効果The invention's effect

蛇腹式フイルタを、中空筒状に、かつ、伸縮自在に蛇腹状に折畳んで構成し、常時はばね力により折畳んだ状態で設置し、逆洗時には、ばね力に抗して蛇腹式フイルタを伸ばすことにより、逆洗効果を高めると共に、小面積で精密濾過が可能な廃水浄化装置を構成することが出来る。  The bellows type filter is configured to be folded in a hollow cylindrical and bellows shape that can be expanded and contracted, and is always installed in a folded state by a spring force. During backwashing, the bellows type filter is resisted against the spring force. By extending the length, it is possible to increase the backwashing effect and to constitute a waste water purification device capable of precision filtration with a small area.

この発明の廃水浄化装置の一実施例を示す側面断面図。  Side surface sectional drawing which shows one Example of the waste water purification apparatus of this invention. 〔図1〕の正面断面図。  FIG. 1 is a front sectional view of FIG. 水酸化マグネシュウムの電荷0ポイント特性を示す図。  The figure which shows the electric charge 0 point characteristic of magnesium hydroxide. 〔図1〕に示すばねの折畳んだ状態を示す図。  The figure which shows the state which the spring shown in FIG. 1 folded. 〔図1〕に示すばねの伸びた状態を示す図。  The figure which shows the state which the spring shown in FIG. 1 extended. この発明の廃水浄化装置の他の一実施例を示す正面断面図。  Front sectional drawing which shows another Example of the waste water purification apparatus of this invention. 〔図6〕に示す突起の側断面図。  FIG. 6 is a side sectional view of the protrusion shown in FIG. 〔図6〕に示す突起の正面図。  The front view of the processus | protrusion shown in FIG. この発明の廃水浄化装置のさらに他の実施例を示す正面断面図。  Front sectional drawing which shows the further another Example of the waste water purification apparatus of this invention.

符号の説明Explanation of symbols

2:廃液
4:浄化槽
5:ダーティタンク
6:吸着剤
7:ベルトコンベア
8:突起
11:蛇腹式フイルタ
12:クリーンタンク
14:ばね
2: Waste liquid 4: Septic tank 5: Dirty tank 6: Adsorbent 7: Belt conveyor 8: Protrusion 11: Bellows filter 12: Clean tank 14: Spring

Claims (1)

廃水が注ぎ込まれる浄化槽内に設置され、沈殿物を浄化槽外に排出するベルトコンベアと、
中空筒状に、かつ、伸縮自在に蛇腹状に折畳まれて構成され、常時はばね力により折畳まれて前記浄化槽内に設置され、外周表面から内部方向に廃水を通過させて浄化する蛇腹式フイルタを備え、
逆洗時は、液体前記蛇腹式フイルタの内部から外周表面方向に逆流させ、前記ばね力に抗して前記蛇腹式フイルタを伸ばし、前記蛇腹式フイルタの外周表面に付着していた付着物を、前記ベルトコンベア上に沈殿させるようにしたことを特徴とする廃水浄化装置。
A belt conveyor installed in the septic tank into which the waste water is poured, and discharging the sediment out of the septic tank;
A bellows that is formed in a hollow cylindrical shape and is foldable into an accordion-like shape, and is normally folded by a spring force and installed in the septic tank, and purifies by passing waste water from the outer peripheral surface to the inside. With an expression filter,
At the time of backwashing, the liquid is caused to flow backward from the inside of the bellows type filter toward the outer peripheral surface, the bellows type filter is stretched against the spring force, and the adhering matter adhering to the outer peripheral surface of the bellows type filter, A wastewater purification apparatus characterized in that it is allowed to settle on the belt conveyor.
JP2006357322A 2006-12-18 2006-12-18 Wastewater purification apparatus Pending JP2008149308A (en)

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Application Number Priority Date Filing Date Title
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Application Number Priority Date Filing Date Title
JP2006357322A JP2008149308A (en) 2006-12-18 2006-12-18 Wastewater purification apparatus

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2018118139A (en) * 2018-05-07 2018-08-02 株式会社リヒトラブ pencil case

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2018118139A (en) * 2018-05-07 2018-08-02 株式会社リヒトラブ pencil case

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