JPH0123527Y2 - - Google Patents

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Publication number
JPH0123527Y2
JPH0123527Y2 JP8247684U JP8247684U JPH0123527Y2 JP H0123527 Y2 JPH0123527 Y2 JP H0123527Y2 JP 8247684 U JP8247684 U JP 8247684U JP 8247684 U JP8247684 U JP 8247684U JP H0123527 Y2 JPH0123527 Y2 JP H0123527Y2
Authority
JP
Japan
Prior art keywords
tank
vacuum
filter
separation
liquid
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
Application number
JP8247684U
Other languages
Japanese (ja)
Other versions
JPS61814U (en
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed filed Critical
Priority to JP8247684U priority Critical patent/JPS61814U/en
Publication of JPS61814U publication Critical patent/JPS61814U/en
Application granted granted Critical
Publication of JPH0123527Y2 publication Critical patent/JPH0123527Y2/ja
Granted legal-status Critical Current

Links

Description

【考案の詳細な説明】 イ 考案の目的 「産業上の利用分野」 本考案は真空ろ過機に関するもので、ろ材を用
いたろ過装置、いわゆる自動式フイルターを用い
る自動式紙供給装置、工作機械の汚液処理、その
他各種産業部門に応用可能である。
[Detailed explanation of the invention] A. Purpose of the invention: ``Industrial application field'' This invention relates to a vacuum filter, and includes a filtration device using a filter medium, an automatic paper feeding device using a so-called automatic filter, and a machine tool. It can be applied to sewage treatment and other various industrial sectors.

「従来の技術」 従来、ろ材を自動的に供給排出しながら真空吸
引作用を利用してろ過および清浄液の排出を行う
装置として、例えば特開昭58−17811号の「真空
フイルター」が提案されているが、該装置は下記
のごとき欠陥がある。
``Prior Art'' Conventionally, for example, the ``vacuum filter'' disclosed in Japanese Patent Application Laid-open No. 17811-1983 has been proposed as a device that automatically supplies and discharges filter media and uses vacuum suction to filter and discharge cleaning liquid. However, this device has the following defects.

「考案が解決しようとする問題点」 (1) ろ過作業が間欠的に行われるので非能率的で
ある。
``Problems that the invention attempts to solve'' (1) It is inefficient because filtration work is performed intermittently.

(2) ろ過直後の真空タンクが大形で汚液流入口が
高くなる。したがつて、工作機械等の汚液の排
出口が低い場合、ポンプでくみ上げて真空フイ
ルターに供給する必要がある。
(2) The vacuum tank immediately after filtration is large and the sewage inlet is high. Therefore, if the discharge port of machine tools or the like is low, it is necessary to pump up the dirty liquid and supply it to the vacuum filter.

(3) 真空タンクの大きさが制限される関係上処理
流量も制限されてこれを増大することが困難で
ある。
(3) Since the size of the vacuum tank is limited, the processing flow rate is also limited and it is difficult to increase this.

(4) 従来は真空タンクにたまつた清浄液を排出す
る際に早く排出する必要から加圧排出を行う
と、逆止弁がなかつたため、ろ材を急激に持ち
上げ、ろ材上のスラツジによるケーキ状の堆積
層を破壊し、ろ過の際のケーキ効果が損われ
た。
(4) Conventionally, when draining the cleaning liquid accumulated in the vacuum tank, pressurized discharge was used to discharge the cleaning liquid quickly, but because there was no check valve, the filter medium was suddenly lifted up, causing a cake-like formation due to sludge on the filter medium. , and the cake effect during filtration was impaired.

ロ 考案の構成 「問題点を解決するための手段」 本考案は上記従来方式の欠陥を解消するため、
真空タンクと別に分離タンクを設置し、両者を逆
止弁で連結することにより連続自動運転が円滑に
行えるようになり、その他前記の欠点が除去され
た。
B. Composition of the invention ``Means for solving the problems'' In order to eliminate the defects of the above-mentioned conventional method, the present invention
By installing a separation tank separate from the vacuum tank and connecting the two with a check valve, continuous automatic operation can be performed smoothly, and other drawbacks mentioned above have been eliminated.

「作用」 (1) ろ過作業の連続自動運転が円滑に行える。"action" (1) Continuous automatic operation of filtration work can be performed smoothly.

(2) ろ過直後の真空タンクを小さくすることが可
能となり、したがつて流入口を低くし、供給用
のポンプが不要となつて安価に供給できる。
(2) It is possible to reduce the size of the vacuum tank immediately after filtration, which lowers the inlet, eliminates the need for a supply pump, and enables inexpensive supply.

(3) 真空室を自由に大きくすることが可能とな
り、処理量が増大する。
(3) It becomes possible to freely enlarge the vacuum chamber, increasing the throughput.

(4) 逆止弁の設置により、連続運転中常時排液に
加圧して行うことが可能となり排液ポンプが無
くても排液口を高くすることが可能となり、既
設タンクの高さに柔軟に対応できることとな
る。また従来法のごときケーキ状堆積層の破壊
がなくなつた。
(4) By installing a check valve, it is possible to pressurize the drain at all times during continuous operation, making it possible to raise the drain port even without a drain pump, making it flexible to the height of the existing tank. This means that it will be possible to respond to Furthermore, the destruction of the cake-like deposited layer, which was the case with the conventional method, was eliminated.

「実施例」 本考案の真空ろ過機の原理的な説明を第1図に
ついて行うと、上部3の汚液流入タンクと、下部
1の真空タンクとによつて密着圧接されてろ材4
が設置され、真空タンク1の上部のろ材に接した
部分は多孔板2となつている。真空タンク1は逆
止弁7,8を通つて、別の分離タンク5,6に連
結されている。
``Example'' The principle of the vacuum filtration machine of the present invention will be explained with reference to FIG.
is installed, and the upper part of the vacuum tank 1 in contact with the filter medium is a perforated plate 2. The vacuum tank 1 is connected to further separation tanks 5, 6 through check valves 7, 8.

最初タンク1,5,6は逆止弁7,8,9,1
0によつて大気開放されているので、タンク3に
汚液が流入すると液自重によつて汚液はろ材4を
通つてろ過され、清浄液は真空タンク1の中に落
下するが、自然落下ではろ過量が少ない為、タン
ク3の中の液面が上昇すると、レベル計17によ
つてあらかじめ設定されたレベルを検知して自動
的に電磁弁13を開き、エゼクター11によつて
分離タンク5、続いて真空タンク1は真空状態と
なり強制ろ過が行なわれる。
Initially tanks 1, 5, 6 have check valves 7, 8, 9, 1
Since the tank 3 is open to the atmosphere, when the dirty liquid flows into the tank 3, it is filtered through the filter material 4 due to its own weight, and the clean liquid falls into the vacuum tank 1, but it does not fall naturally. Since the amount of filtration is small, when the liquid level in the tank 3 rises, the level meter 17 detects the preset level and automatically opens the solenoid valve 13, and the ejector 11 removes the liquid from the separation tank 5. Then, the vacuum tank 1 is brought into a vacuum state and forced filtration is performed.

この際、真空タンク1、分離タンク5は逆止弁
9,10によつて大気と遮断され真空状態が保た
れる。ただし分離タンク6はレベルスイツチ18
の信号により電磁弁14によつて加圧空気は遮断
され大気開放となつている。タンク5及び1が真
空状態になると、汚液流入タンク3の中の汚液は
ろ材4によつて急速にろ過され、清浄液は真空タ
ンク1及び分離タンク5の中に流入する。更に真
空状態が続き、分離タンク5の中の清浄液がタン
ク内に充満してくると、レベルスイツチ15が、
あらかじめ設定されたレベルを検知し、自動的に
電磁切換弁12を動作させエア回路は切換えられ
る。切換えられたエア回路により、分離タンク5
からエゼクターに接続されていた回路は、今度は
逆に電磁弁13,14を通つてきた圧力回路につ
ながり、分離タンク5は加圧状態となり、中に充
満していた清浄液は逆止弁9を通つて外部に排出
される。同時に、一方、分離タンク6は電磁切換
弁12によつて切換えられた回路によつて真空状
態となり、タンク1を通つた清浄液は引続いてタ
ンク6の中に流入してくる。分離タンク5に設け
られたレベルスイツチ16によつてタンク5の中
の液の排出終了は検知され、自動的に電磁切換弁
12は初期の状態に換えられる。この時、分離タ
ンク6の中に入つている清浄液は排液が完了しレ
ベルスイツチ19がONになるまで電磁弁14は
開となつていて加圧排出が行なわれる。分離タン
ク5の中の液の排出と、分離タンク6の中への清
浄液の流入は同時に始まるが、ろ材4の抵抗によ
り、タンク6の中の液の充満する時間と、タンク
5の中の液の排出時間は、タンク5の中の液の排
出時間の方が短時間で終了する。従つて、タンク
6の中の液があふれることは起らない。
At this time, the vacuum tank 1 and the separation tank 5 are isolated from the atmosphere by check valves 9 and 10 to maintain a vacuum state. However, the separation tank 6 has a level switch 18.
In response to this signal, the pressurized air is shut off by the solenoid valve 14 and the air is opened to the atmosphere. When the tanks 5 and 1 are in a vacuum state, the dirty liquid in the dirty liquid inlet tank 3 is rapidly filtered by the filter medium 4, and the clean liquid flows into the vacuum tank 1 and the separation tank 5. When the vacuum condition continues and the cleaning liquid in the separation tank 5 fills up, the level switch 15
A preset level is detected and the electromagnetic switching valve 12 is automatically operated to switch the air circuit. Due to the switched air circuit, separation tank 5
The circuit that was connected to the ejector is now conversely connected to the pressure circuit that passed through the solenoid valves 13 and 14, and the separation tank 5 becomes pressurized, and the cleaning liquid that was filled inside is passed through the check valve 9. is discharged to the outside through. At the same time, on the other hand, the separation tank 6 is brought into a vacuum state by the circuit switched by the electromagnetic switching valve 12, and the cleaning liquid that has passed through the tank 1 continues to flow into the tank 6. A level switch 16 provided in the separation tank 5 detects the completion of discharging the liquid in the tank 5, and automatically switches the electromagnetic switching valve 12 to its initial state. At this time, the solenoid valve 14 remains open and the cleaning liquid contained in the separation tank 6 is pressurized and discharged until the draining is completed and the level switch 19 is turned on. The discharge of the liquid in the separation tank 5 and the inflow of the cleaning liquid into the separation tank 6 start at the same time, but due to the resistance of the filter medium 4, the time for the liquid to fill in the tank 6 and the flow of the cleaning liquid in the tank 5 are delayed. The time required to drain the liquid from the tank 5 is shorter than the time required to drain the liquid from the tank 5. Therefore, the liquid in the tank 6 will not overflow.

以上のようにろ過と清浄液の排出は自動的に連
続して行なわれるが、時間の経過と共にろ材の上
にはろ過された固形物が堆積して、ろ材が目づま
りしてろ過速度が遅くなつてくる、そして汚液流
入タンク3の中の液面が上昇してレベル計17が
これを検知すると、自動的に電磁弁13によつて
供給空気圧回路は遮断される。供給空気圧回路が
遮断されると、すべての真空吸引動作と加圧動作
は中止される。
As described above, filtration and cleaning fluid discharge are performed automatically and continuously, but as time passes, filtered solids accumulate on the filter media, clogging the filter media and slowing down the filtration speed. When the liquid level in the dirty liquid inflow tank 3 rises and the level meter 17 detects this, the supply air pressure circuit is automatically shut off by the solenoid valve 13. When the supply air pressure circuit is interrupted, all vacuum suction and pressurization operations are discontinued.

タンク1の中は、この時真空吸引の動作が中止
されるわけであるが、タンクが小さいため、常に
清浄液が充満の状態になつており、真空吸引が中
止されると空気層が無いため、及び逆止弁7,9
のため負圧とはならない。また空気層が若干存在
していても容積が小さいためろ布を通つて、急速
に負圧から解放される。従つて、ろ布は多孔板2
に密着して、はりついていた状態からすぐ解放さ
れろ布の移動は楽に行なえる状態となる。
At this time, the vacuum suction inside tank 1 is stopped, but because the tank is small, it is always full of cleaning fluid, and when the vacuum suction is stopped, there is no air space. , and check valves 7 and 9
Therefore, there is no negative pressure. Furthermore, even if some air space exists, since the volume is small, it passes through the filter cloth and is rapidly released from the negative pressure. Therefore, the filter cloth is the perforated plate 2
The filter cloth is immediately released from the stuck state, and the filter cloth can be moved easily.

この状態でろ布4は巻き取られて、ろ過面には
新しいろ布面が設置され固形物の堆積した古いろ
布は逆り出され外部に排出される。
In this state, the filter cloth 4 is wound up, a new filter cloth surface is installed on the filtration surface, and the old filter cloth on which solid matter has accumulated is turned out and discharged to the outside.

これらのろ布の動作はあらかじめ設定されたシ
ーケンス回路のタイマー等により自動的に行なわ
れ、設定が終ると、先にストツプされていた電磁
弁13は元に戻され、再び真空吸引ろ過の動作は
続けられる。
These filter cloth operations are automatically performed by a preset sequence circuit timer, etc., and when the settings are completed, the previously stopped solenoid valve 13 is returned to its original state, and the vacuum suction filtration operation is resumed. I can continue.

ハ 考案の効果 本考案により得られる効果は次の通りである。C. Effect of the idea The effects obtained by the present invention are as follows.

(1) ろ過作業の連続自動運転が円滑に行える。(1) Continuous automatic operation of filtration work can be performed smoothly.

(2) 真空タンクを小形にすることが可能となり、
ポンプが不要となつて価格が安く提供できる。
(2) The vacuum tank can be made smaller,
Since no pump is required, the price can be lowered.

(3) 真空室を自由に大きくできるので処理量が増
大する。
(3) The vacuum chamber can be enlarged freely, increasing the throughput.

(4) ケーキ状堆積層の破壊によるろ過効果の低下
がない。
(4) There is no reduction in filtration effectiveness due to destruction of the cake-like sediment layer.

【図面の簡単な説明】[Brief explanation of the drawing]

第1図は本考案実施の1例を示す全体の構成図
である。 図中の符号はそれぞれ下記部材を示す。1:真
空タンク、2:多孔板、3:汚液流入タンク、
4:ろ材、5:分離タンク、6:分離タンク、
7:逆止弁、8:逆止弁、9:逆止弁、10:逆
止弁、11:エアエゼクター、12:電磁切換
弁、13:電磁弁、14:電磁弁、15:レベル
スイツチ、16:レベルスイツチ、17:レベル
計、18:レベルスイツチ、19:レベルスイツ
チ。
FIG. 1 is an overall configuration diagram showing one example of implementing the present invention. The symbols in the drawings indicate the following members, respectively. 1: Vacuum tank, 2: Perforated plate, 3: Sewage inflow tank,
4: Filter medium, 5: Separation tank, 6: Separation tank,
7: Check valve, 8: Check valve, 9: Check valve, 10: Check valve, 11: Air ejector, 12: Solenoid switching valve, 13: Solenoid valve, 14: Solenoid valve, 15: Level switch, 16: Level switch, 17: Level meter, 18: Level switch, 19: Level switch.

Claims (1)

【実用新案登録請求の範囲】 1 上部を大気開放とし下部を開放とした汚液流
入タンクを上に置き、上部を多孔板とした真空
タンクを下に置き、両者の中間にろ材をはさん
でなるものにおいて、該真空タンクに直列に別
の分離タンクを逆止弁を介して連結させてなる
真空ろ過機。 2 前記分離タンクを2個以上設置してなる実用
新案登録請求の範囲第1項に記載の真空ろ過
機。 3 前記分離タンク2個を設け、各分離タンクに
は上下のレベルスイツチを内蔵し、その下部が
逆止弁を介して前記真空タンクと大気に連結せ
られ、その上部が電磁切換弁を介して圧力空気
開閉用電磁弁およびエアエゼクタに接続されて
なる実用新案登録請求の範囲第1項に記載の真
空ろ過機。
[Scope of Claim for Utility Model Registration] 1. A sewage inflow tank with the upper part open to the atmosphere and the lower part open is placed on top, a vacuum tank with a perforated plate on the top is placed below, and a filter material is sandwiched between the two. A vacuum filter comprising another separation tank connected in series to the vacuum tank via a check valve. 2. The vacuum filtration machine according to claim 1, which is provided with two or more separation tanks. 3 The two separation tanks are provided, and each separation tank has a built-in upper and lower level switch, the lower part of which is connected to the vacuum tank and the atmosphere via a check valve, and the upper part of which is connected to the atmosphere via an electromagnetic switching valve. The vacuum filtration machine according to claim 1, which is connected to a solenoid valve for opening and closing pressurized air and an air ejector.
JP8247684U 1984-06-05 1984-06-05 vacuum filtration machine Granted JPS61814U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP8247684U JPS61814U (en) 1984-06-05 1984-06-05 vacuum filtration machine

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP8247684U JPS61814U (en) 1984-06-05 1984-06-05 vacuum filtration machine

Publications (2)

Publication Number Publication Date
JPS61814U JPS61814U (en) 1986-01-07
JPH0123527Y2 true JPH0123527Y2 (en) 1989-07-19

Family

ID=30630224

Family Applications (1)

Application Number Title Priority Date Filing Date
JP8247684U Granted JPS61814U (en) 1984-06-05 1984-06-05 vacuum filtration machine

Country Status (1)

Country Link
JP (1) JPS61814U (en)

Also Published As

Publication number Publication date
JPS61814U (en) 1986-01-07

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