JPS58101714A - Method for supplying sludge to filter press - Google Patents
Method for supplying sludge to filter pressInfo
- Publication number
- JPS58101714A JPS58101714A JP56202077A JP20207781A JPS58101714A JP S58101714 A JPS58101714 A JP S58101714A JP 56202077 A JP56202077 A JP 56202077A JP 20207781 A JP20207781 A JP 20207781A JP S58101714 A JPS58101714 A JP S58101714A
- Authority
- JP
- Japan
- Prior art keywords
- sludge
- pump
- pressure
- filter press
- tank
- 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.)
- Pending
Links
Landscapes
- Filtration Of Liquid (AREA)
Abstract
Description
【発明の詳細な説明】
この発明は、フィルタープレス等、加圧脱水機の汚泥供
給方法に関する。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for supplying sludge to a pressure dehydrator such as a filter press.
従来、フィルタープレスにおいて、汚泥の供給は、第1
図に示すように、フィルタープレス1の濾室に凝集汚泥
槽2がらポンプ3によって汚泥を供給すると同時に濾過
する作用であって、給泥開始時、ポンプ3の吐出側圧力
は配管抵抗程度で殆ど零であるが、濾室内に汚泥が充満
し、さらに濾過抵抗が増加すると、例えば4〜5Kg/
cdとな−る。Conventionally, in a filter press, sludge is supplied in the first
As shown in the figure, the pump 3 supplies sludge from the flocculated sludge tank 2 to the filtration chamber of the filter press 1 and filters it at the same time.At the start of sludge supply, the pressure on the discharge side of the pump 3 is almost equal to the piping resistance. However, if the filter chamber is filled with sludge and the filtration resistance increases, for example, 4 to 5 kg/
It becomes a CD.
すなわち、第3図に示すように、時間の経過とともに揚
程は上昇し、濾室内に汚泥が充満すると一定になるが、
反面、ポンプ3を駆動するのに要する力(軸動力)は徐
々に低下する。この揚程と軸動力をポンプ吐出量に対し
て示せば第4゛図のようになり、給泥開始時ζこは吐出
量が多いため大きな軸動力を必要とする。In other words, as shown in Figure 3, the head rises over time and becomes constant when the filter chamber is filled with sludge, but
On the other hand, the force (shaft power) required to drive the pump 3 gradually decreases. If this lifting head and shaft power are plotted against the pump discharge amount, it will be as shown in Fig. 4. At the start of mud feeding, a large shaft power is required because the discharge amount is large.
最近、フィルタープレスの大型化に伴なって一台当りの
濾過面積が増大しているが、汚泥供給を従来通りの短時
間で行なうには、給泥開始時のポンプ吐゛出量を増加す
る必要があり、ますます大きな容量のポンプが必要にな
ってきている。Recently, as filter presses have become larger, the filtration area per unit has increased, but in order to supply sludge in the same short time as before, it is necessary to increase the pump discharge volume at the start of sludge supply. Increasingly, larger capacity pumps are required.
さらに、従来の供給方法においては、フィルタープレス
の1サイクル処理時間におけるポンプ3の駆動時間の割
合が少ないため、ポンプの運転効率が悪い欠点がある。Furthermore, in the conventional supply method, since the ratio of the drive time of the pump 3 to one cycle processing time of the filter press is small, there is a drawback that the operating efficiency of the pump is low.
この発明は、上記の欠点を解消し、小容量のポンプを効
率よく稼動させるようにした汚泥の供給方法を提供する
ことを目的とする。SUMMARY OF THE INVENTION An object of the present invention is to provide a sludge supply method that eliminates the above-mentioned drawbacks and allows a small-capacity pump to operate efficiently.
すなわち、フィルタープレスの汚泥供給管路に圧力タン
クを設けることにより汚泥供給ポンプの経済的な運転を
可能にするとともに、ポンプの小WWr化を図ったもの
である。That is, by providing a pressure tank in the sludge supply line of the filter press, the sludge supply pump can be operated economically, and the WWr of the pump can be reduced.
以下、この発明の実施例を第2図に基づいて説明する。Hereinafter, an embodiment of the present invention will be described based on FIG. 2.
図示のよう(こ、フィルタープレスの汚泥供給ポンプこ
圧力タンク4を開閉弁5を介して接続し、この圧力タン
ク4に逆止弁6を介して汚泥ポンプ3を接続する。As shown in the figure, the sludge supply pump of the filter press is connected to a pressure tank 4 via an on-off valve 5, and a sludge pump 3 is connected to this pressure tank 4 via a check valve 6.
圧力タンク4にはポンプ3により汚泥槽2内の汚泥を例
えば圧力4〜6 Kp/iの範囲内の一定圧力で貯溜す
る。すなわち、圧力タンク4内が一定圧力以下になると
、それを圧力スイッチ等によって検出し、その検出信号
によってポンプ3を駆動させて、圧力タンク4内に汚泥
を供給し1一定圧力をこ達すると停止させるようにする
。この一定圧力は給泥圧力としてこの方法の最適な値と
すればよく、例えば給泥圧力を4〜5Kg/6Iとした
場合、その圧力は6に9/−程度である。The sludge in the sludge tank 2 is stored in the pressure tank 4 by the pump 3 at a constant pressure within a range of, for example, 4 to 6 Kp/i. In other words, when the pressure inside the pressure tank 4 falls below a certain level, it is detected by a pressure switch, etc., and the detection signal drives the pump 3 to supply sludge into the pressure tank 4, and stops when the pressure reaches a certain level. Let them do it. This constant pressure may be the optimal value for this method as the mud supply pressure. For example, when the mud supply pressure is set to 4 to 5 kg/6I, the pressure is about 6 to 9/-.
なお、ポンプ作動時、圧力タンク4からポンプ3への汚
泥の逆流は逆止弁6によって阻止される。Note that when the pump is in operation, the check valve 6 prevents sludge from flowing back from the pressure tank 4 to the pump 3.
上記開閉弁5は汚泥供給時のみ開放するものとし、通常
フィルタープレスは自動運転されるため、自動制御可能
な電磁弁を使用する。この開閉弁5が開くことにより、
圧力タンク4内の汚泥がその圧力1.によってフィルタ
ープレス1内に供給される。The on-off valve 5 is opened only when sludge is supplied, and since the filter press is normally operated automatically, an automatically controllable solenoid valve is used. By opening this on-off valve 5,
The sludge in the pressure tank 4 has a pressure of 1. is fed into the filter press 1 by.
なお、図中、7は汚泥槽2内に設けた攪拌装置である。In addition, in the figure, 7 is a stirring device provided in the sludge tank 2.
つぎに上記実施例の作用を説明する。Next, the operation of the above embodiment will be explained.
いま、圧力タンク4が一定圧力に保たれた状態において
、フィルタープレス1の閉板を行ない、開閉弁5が開く
と、圧力タンク4内の汚泥がその圧力によって、フィル
タープレス1内に供給されてつぎの圧搾作用に移ってい
く。Now, with the pressure tank 4 maintained at a constant pressure, when the filter press 1 is closed and the on-off valve 5 is opened, the sludge in the pressure tank 4 is supplied into the filter press 1 by the pressure. Moving on to the next squeezing action.
この給泥時間を短縮するには圧力タンク4の容量を大き
くすればよい。一方、汚泥ポンプJ3は給泥工程後から
次回の給泥工程前までに圧力タンク4内の圧力を所定の
値まであげておけばよいため、換言1れば一給泥工程以
外の時も運転して1サイクル中に圧力タンク4の圧力を
一定値まで上げておけばよいため、ポンプ3の容量は、
従来のポンプ3により直接をこ給泥していたものに比し
く給泥時間)/(1サイクルに必要な時間)程度に減少
でき、したがって軸動力も同程度に減少できる。In order to shorten this mud supply time, the capacity of the pressure tank 4 may be increased. On the other hand, the sludge pump J3 only needs to raise the pressure in the pressure tank 4 to a predetermined value after the sludge feeding process and before the next sludge feeding process. The capacity of the pump 3 is:
Compared to the conventional pump 3 that directly supplies mud, the slurry supply time can be reduced to the order of (time required for one cycle)/(time required for one cycle), and the shaft power can also be reduced to the same extent.
次表に4〜51’g/−の圧力で給泥する場合の従来方
法と本発明による方法との比較を示す。The following table shows a comparison between the conventional method and the method according to the present invention when feeding mud at a pressure of 4 to 51'g/-.
さらに、圧力タンク4を大容量として給泥による圧力変
動を小さくすれば、ポンプ3の揚程変動もその圧力変動
に対応して小さくなるため、従来のように給泥開始時の
過負荷という問題が生じない。Furthermore, if the pressure tank 4 has a large capacity to reduce pressure fluctuations caused by mud supply, the pump head fluctuations of the pump 3 will also be reduced correspondingly to the pressure fluctuations, eliminating the problem of overload at the start of mud supply as in the past. Does not occur.
なお、図では2台のフィルタープレス1を1つの圧力タ
ンク44こよって汚泥の供給を行なうようにしたが、フ
ィルタープレス1の数は任意数でよく、その数に応じて
圧力タンク4の容量を適宜に設定すればよい。In addition, in the figure, two filter presses 1 are supplied with sludge through one pressure tank 44, but the number of filter presses 1 may be arbitrary, and the capacity of the pressure tank 4 can be adjusted according to the number. It may be set as appropriate.
また、第2図をこ示すように、コンプレッサ8を圧力タ
ンク4の上部に接続して、圧縮空気を適宜に供給すれば
、ポンプ3の揚程以上の圧力で汚泥を供給することがで
きる。Furthermore, as shown in FIG. 2, if a compressor 8 is connected to the upper part of the pressure tank 4 and compressed air is supplied appropriately, sludge can be supplied at a pressure higher than the pump head of the pump 3.
以上のように、この発明の汚泥供給方法によると、圧力
タンク内の汚泥をその圧力によりフィルタープレスをこ
供給するようにしたので、フィルタープレスの1サイク
ル中に圧力タンクの圧力が一定値になるようにポンプで
汚泥を送ればよく、従来のごとく直接ポンプにより短時
間で大容量の汚泥を供給する必要がなく、小容量のポン
プを使用することができるうえに、フィルタープレスが
大型化しても、ポンプを大容量にすることなく、圧力タ
ンクの容量を大きくするだけで従来どおり短時間で給泥
がで−きる。゛
また、1サイクル中、ポンプを駆動させることができて
ポンプ駆動に時間的余裕があるため、ボンブの経済的な
運転ができる効果もある。As described above, according to the sludge supply method of the present invention, the sludge in the pressure tank is supplied to the filter press using its pressure, so that the pressure in the pressure tank becomes constant during one cycle of the filter press. In this way, sludge can only be sent with a pump, and there is no need to directly pump a large volume of sludge in a short period of time as in the past, and a small-capacity pump can be used. By simply increasing the capacity of the pressure tank, mud can be supplied in a short time as before without increasing the capacity of the pump. Furthermore, since the pump can be driven during one cycle and there is time to drive the pump, there is an effect that the bomb can be operated economically.
第1図は従来のフィルタープレスの汚泥供給概略配管図
、第2図はこの発明のフィルタープレスの汚泥供給概略
配管図、第3図及び第4図はそれぞれ時間と揚程、軸動
力及びポンプ吐中量と揚程、軸動力の関係図である。
1・・・フィルタープレス、2・・・汚泥槽、3・・・
ポンプ、4・・・圧力タンク、5・・・開閉弁特許出願
人−・・ 久保田鉄工株式会社同 代理人 鎌 1
) 文 二Figure 1 is a schematic diagram of the sludge supply piping of a conventional filter press, Figure 2 is a schematic diagram of the sludge supply piping of the filter press of the present invention, and Figures 3 and 4 are time, head, shaft power, and pump discharge time, respectively. It is a relationship diagram of quantity, lift, and shaft power. 1... Filter press, 2... Sludge tank, 3...
Pump, 4...Pressure tank, 5...Opening/closing valve Patent applicant: Kubota Iron Works Co., Ltd. Agent: Sickle 1
) Sentence 2
Claims (1)
タンクを接続し、この圧力タンクにポンプにより汚泥を
送って一定圧の汚泥を貯溜し、前記開閉弁を開放するこ
とによって圧力タンク内の汚泥をその圧力によりフィル
タープレスに供給することから成る汚泥供給方法。A pressure tank is connected to the sludge supply pipe of the filter press via an on-off valve, sludge is sent to this pressure tank by a pump to store sludge at a constant pressure, and the sludge in the pressure tank is removed by opening the on-off valve. A sludge supply method consisting of supplying sludge to a filter press under its pressure.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP56202077A JPS58101714A (en) | 1981-12-11 | 1981-12-11 | Method for supplying sludge to filter press |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP56202077A JPS58101714A (en) | 1981-12-11 | 1981-12-11 | Method for supplying sludge to filter press |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS58101714A true JPS58101714A (en) | 1983-06-17 |
Family
ID=16451567
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP56202077A Pending JPS58101714A (en) | 1981-12-11 | 1981-12-11 | Method for supplying sludge to filter press |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS58101714A (en) |
Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS56152713A (en) * | 1980-04-30 | 1981-11-26 | Tsukishima Kikai Co Ltd | Continuous pressure-supplying method for raw liquid of pressure filter |
-
1981
- 1981-12-11 JP JP56202077A patent/JPS58101714A/en active Pending
Patent Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS56152713A (en) * | 1980-04-30 | 1981-11-26 | Tsukishima Kikai Co Ltd | Continuous pressure-supplying method for raw liquid of pressure filter |
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