JPH0334261Y2 - - Google Patents
Info
- Publication number
- JPH0334261Y2 JPH0334261Y2 JP1983000598U JP59883U JPH0334261Y2 JP H0334261 Y2 JPH0334261 Y2 JP H0334261Y2 JP 1983000598 U JP1983000598 U JP 1983000598U JP 59883 U JP59883 U JP 59883U JP H0334261 Y2 JPH0334261 Y2 JP H0334261Y2
- Authority
- JP
- Japan
- Prior art keywords
- sludge
- pressure
- pump
- tank
- pressurized
- 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
- 239000010802 sludge Substances 0.000 claims description 39
- 238000000034 method Methods 0.000 description 3
- 238000010586 diagram Methods 0.000 description 2
- 230000015271 coagulation Effects 0.000 description 1
- 238000005345 coagulation Methods 0.000 description 1
- 230000016615 flocculation Effects 0.000 description 1
- 238000005189 flocculation Methods 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Landscapes
- Treatment Of Sludge (AREA)
Description
【考案の詳細な説明】
この考案は、フイルタープレスなどの加圧脱水
機の汚泥供給装置に関する。[Detailed Description of the Invention] This invention relates to a sludge supply device for a pressure dehydrator such as a filter press.
通常、加圧脱水機においては、凝集混和槽など
の汚泥槽からポンプによつて汚泥を供給すると同
時に過作用を行つている。このため、脱水機が
圧搾機構を有すると有しないとにかかわらず、供
給圧力が高いほど過率がよいこととなる。しか
しながら、ポンプによる供給圧力は、通常15Kg/
cm2程度が最大であり、それ以上の供給圧力を得る
ことができない。 Normally, in a pressurized dehydrator, sludge is supplied by a pump from a sludge tank such as a flocculation mixing tank, and at the same time, overaction is performed. Therefore, regardless of whether the dehydrator has a squeezing mechanism or not, the higher the supply pressure, the better the excess rate. However, the supply pressure by the pump is usually 15Kg/
The maximum supply pressure is about cm2 , and it is not possible to obtain a supply pressure higher than that.
また、汚泥供給を加圧タンクによつて行なう手
段も考案されているが、この手段で得られる供給
最大圧力は10Kg/cm2前後が限度である。 In addition, a method of supplying sludge using a pressurized tank has been devised, but the maximum supply pressure that can be obtained with this method is limited to around 10 kg/cm 2 .
この考案の目的は加圧脱水機における汚泥供給
圧力を高めて脱水効率を高めることにある。 The purpose of this invention is to increase the sludge supply pressure in the pressure dehydrator to improve dewatering efficiency.
すなわち、この考案は、汚泥槽から加圧脱水機
の汚泥供給ポンプへの配管に加圧タンクを介設し
てその加圧タンク内の汚泥をポンプに供給可能と
したものであり、この様に構成することにより、
加圧脱水機に供給される汚泥圧力は加圧タンクに
よる加圧とポンプの有効圧(吸入圧と吐出圧の差
であり、ポンプによる加圧)との和となり、ポン
プのみ或は加圧タンクのみでは得られなかつた高
い汚泥供給圧力を得ることができ、脱水効率を高
めることができる。 That is, in this invention, a pressurized tank is interposed in the piping from the sludge tank to the sludge supply pump of the pressure dewatering machine, and the sludge in the pressurized tank can be supplied to the pump. By configuring
The sludge pressure supplied to the pressure dehydrator is the sum of the pressure applied by the pressure tank and the effective pressure of the pump (the difference between suction pressure and discharge pressure, and the pressure applied by the pump). It is possible to obtain a high sludge supply pressure that could not be obtained by using the method alone, and it is possible to improve the dewatering efficiency.
以下、この考案の実施例を添付図面に基づいて
説明する。 Hereinafter, embodiments of this invention will be described based on the accompanying drawings.
第1図に示すように、凝集混和槽などの汚泥槽
(図示せず)から汚泥供給ポンプ1への配管に、
加圧タンク2を介設し、このタンク2に流量調節
弁3、開閉弁4を介してコンプレツサー5を接続
し、コンプレツサー5を駆動させた状態で調節弁
3を調節することによりタンク2内圧力を調節可
能とする。なお、図中9は汚泥槽から加圧タンク
2への配管に介設された開閉弁である。 As shown in FIG. 1, in the piping from a sludge tank (not shown) such as a coagulation mixing tank to the sludge supply pump 1,
A pressurized tank 2 is provided, a compressor 5 is connected to the tank 2 via a flow rate control valve 3 and an on-off valve 4, and the pressure inside the tank 2 is adjusted by adjusting the control valve 3 while the compressor 5 is driven. be adjustable. In addition, 9 in the figure is an on-off valve interposed in the piping from the sludge tank to the pressurized tank 2.
ポンプ1から加圧脱水機6への配管にはこの配
管内の汚泥圧力を検出する圧力検出器兼用の圧力
伝送器7を介設し、この伝送器7の検出値を制御
器8に送り込み、制御器8により前記検出値に基
づきポンプ1の回転数及び調節弁3の開閉度合を
調節する。 A pressure transmitter 7 which also serves as a pressure detector for detecting the sludge pressure in this pipe is interposed in the pipe from the pump 1 to the pressure dehydrator 6, and the detected value of the transmitter 7 is sent to the controller 8. The controller 8 adjusts the rotational speed of the pump 1 and the degree of opening and closing of the control valve 3 based on the detected value.
実施例は以上のように構成されており、つぎに
その作用について説明する。 The embodiment is configured as described above, and its operation will be explained next.
まず、第2図に示すように汚泥供給当初は高い
供給圧力を必要としないため、開閉弁9を開き開
閉弁4を閉じて、ポンプ1のみによつて汚泥を加
圧脱水機6に供給する。したがつて、実施例のご
とく汚泥槽からポンプ1への配管にタンク2を介
設せずとも、汚泥槽と加圧タンク2とを別々の配
管により切換弁を介してポンプ1に接続し、切換
弁によつて汚泥を汚泥槽又は加圧タンクからポン
プ1に選択的に供給可能としてもよい。 First, as shown in FIG. 2, since high supply pressure is not required at the beginning of sludge supply, the on-off valve 9 is opened and the on-off valve 4 is closed, and the sludge is supplied to the pressurized dehydrator 6 only by the pump 1. . Therefore, instead of interposing the tank 2 in the piping from the sludge tank to the pump 1 as in the embodiment, the sludge tank and the pressurized tank 2 can be connected to the pump 1 via a switching valve through separate piping, Sludge may be selectively supplied to the pump 1 from a sludge tank or a pressurized tank using a switching valve.
ポンプ1のみによる供給を続行し、その供給圧
力を伝送器7により制御器8に伝送し、制御器8
により伝送器7の検出値又は供給時間が所望値に
なると、開閉弁9が閉じられ開閉弁4が開かれ、
以後、伝送器7の検出値に基づき制御器8により
調節弁3の開閉度及びポンプ1の回転数が調節さ
れ、加圧タンク2内の汚泥圧力及びポンプ1の吐
出圧力が調節されて、加圧脱水機6に汚泥供給が
所望圧で続行される。 Supply by only the pump 1 is continued, and the supply pressure is transmitted to the controller 8 by the transmitter 7.
When the detected value of the transmitter 7 or the supply time reaches the desired value, the on-off valve 9 is closed and the on-off valve 4 is opened.
Thereafter, the controller 8 adjusts the opening/closing degree of the control valve 3 and the rotation speed of the pump 1 based on the detected value of the transmitter 7, and adjusts the sludge pressure in the pressurized tank 2 and the discharge pressure of the pump 1. Sludge is continued to be supplied to the pressure dehydrator 6 at a desired pressure.
この作用時、脱水機6への汚泥供給圧力は加圧
タンク2内の圧力にポンプ1の有効圧を加えた値
となり、従来のポンプのみ、加圧タンクのみの汚
泥供給に比べ、供給圧力を高くできて高い脱水効
率を得ることができる。ポンプ1のみの汚泥供給
から加圧タンク2を加味した汚泥供給への切換時
の汚泥供給圧力、すなわち前記供給圧力の所望値
は適宜に設定すればよく、例えば3〜8Kg/cm2と
する。 During this operation, the sludge supply pressure to the dehydrator 6 is the pressure in the pressurized tank 2 plus the effective pressure of the pump 1, which lowers the supply pressure compared to the conventional sludge supply using only a pump or only a pressurized tank. It is possible to obtain high dewatering efficiency. The sludge supply pressure at the time of switching from the sludge supply using only the pump 1 to the sludge supply including the pressurized tank 2, that is, the desired value of the supply pressure, may be set appropriately, for example, from 3 to 8 Kg/ cm2 .
なお、実施例においては、当初ポンプ1のみで
汚泥供給を行つたが、必ずしもそうする必要はな
く、供給当初から加圧タンク2の加圧された汚泥
をポンプ1により加圧脱水機6に供給するように
してもよく、また、第1図鎖線で示すようにポン
プ1の前後に開閉弁を設けるとともに、バイパス
管を設け、供給当初は加圧タンク2の加圧された
汚泥をポンプ1を通さず直接加圧脱水機6に供給
し、供給圧力又は供給時間が所望の値になつた後
はポンプ1を通して、加圧された汚泥をポンプ1
により加圧脱水機6に供給するようにしてもよ
い。 In the embodiment, the sludge was initially supplied using only the pump 1, but it is not necessary to do so, and the pressurized sludge in the pressurized tank 2 can be supplied to the pressure dehydrator 6 using the pump 1 from the beginning of supply. In addition, as shown by the chain line in Figure 1, on-off valves may be provided before and after the pump 1, and a bypass pipe may be provided so that the pressurized sludge in the pressurized tank 2 is transferred to the pump 1 at the beginning of supply. The pressurized sludge is directly supplied to the pressure dehydrator 6 without passing through the pump 1, and after the supply pressure or supply time reaches the desired value, the pressurized sludge is passed through the pump 1.
Alternatively, the water may be supplied to the pressurized dehydrator 6.
さらに、この考案は、圧搾機構を有しない加圧
脱水機或は圧搾機構を有する加圧脱水機いずれに
も採用し得ることは勿論である。 Furthermore, it goes without saying that this invention can be applied to either a pressurized dehydrator without a squeezing mechanism or a pressurized dehydrator that has a squeezing mechanism.
第1図はこの考案の加圧脱水機の汚泥供給装置
の一実施例の概略配管図、第2図は第1図の作用
説明用の経過時間と汚泥供給圧力との関係図であ
る。
1……汚泥供給ポンプ、2……加圧タンク、5
……コンプレツサ、6……加圧脱水機。
FIG. 1 is a schematic piping diagram of an embodiment of the sludge supply device for a pressurized dewatering machine of this invention, and FIG. 2 is a diagram showing the relationship between elapsed time and sludge supply pressure for explaining the operation of FIG. 1. 1... Sludge supply pump, 2... Pressurized tank, 5
... Compressor, 6 ... Pressure dehydrator.
Claims (1)
の配管に加圧タンク2を介設して、その加圧タン
ク2内の汚泥を前記ポンプ1に供給可能とした加
圧脱水機の汚泥供給装置。 Sludge of a pressurized dehydrator in which a pressurized tank 2 is interposed in the piping from the sludge tank to the sludge supply pump 1 of the pressurized dehydrator 6, and the sludge in the pressurized tank 2 can be supplied to the pump 1. Feeding device.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP59883U JPS59106510U (en) | 1983-01-06 | 1983-01-06 | Sludge supply device for pressure dehydrator |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP59883U JPS59106510U (en) | 1983-01-06 | 1983-01-06 | Sludge supply device for pressure dehydrator |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS59106510U JPS59106510U (en) | 1984-07-18 |
JPH0334261Y2 true JPH0334261Y2 (en) | 1991-07-19 |
Family
ID=30132349
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP59883U Granted JPS59106510U (en) | 1983-01-06 | 1983-01-06 | Sludge supply device for pressure dehydrator |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS59106510U (en) |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP4749365B2 (en) * | 2007-03-19 | 2011-08-17 | 新明和工業株式会社 | Sludge concentrator and sludge concentrator |
Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS52135465A (en) * | 1976-04-05 | 1977-11-12 | Organo Kk | Crude liquid pressure feeder for pressure filtrating machines |
JPS5716646A (en) * | 1980-07-04 | 1982-01-28 | Nisshin Flour Milling Co Ltd | Production of apricot chips |
-
1983
- 1983-01-06 JP JP59883U patent/JPS59106510U/en active Granted
Patent Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS52135465A (en) * | 1976-04-05 | 1977-11-12 | Organo Kk | Crude liquid pressure feeder for pressure filtrating machines |
JPS5716646A (en) * | 1980-07-04 | 1982-01-28 | Nisshin Flour Milling Co Ltd | Production of apricot chips |
Also Published As
Publication number | Publication date |
---|---|
JPS59106510U (en) | 1984-07-18 |
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