JPS6031879A - Pressure float concentration apparatus - Google Patents

Pressure float concentration apparatus

Info

Publication number
JPS6031879A
JPS6031879A JP14174083A JP14174083A JPS6031879A JP S6031879 A JPS6031879 A JP S6031879A JP 14174083 A JP14174083 A JP 14174083A JP 14174083 A JP14174083 A JP 14174083A JP S6031879 A JPS6031879 A JP S6031879A
Authority
JP
Japan
Prior art keywords
pressure
pump
tank
pressurized
amount
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
Application number
JP14174083A
Other languages
Japanese (ja)
Inventor
Masanosuke Yoneda
米田 理之助
Joji Yashiro
八代 譲治
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Kubota Corp
Original Assignee
Kubota Corp
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 by Kubota Corp filed Critical Kubota Corp
Priority to JP14174083A priority Critical patent/JPS6031879A/en
Publication of JPS6031879A publication Critical patent/JPS6031879A/en
Pending legal-status Critical Current

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Abstract

PURPOSE:To compensate a leak by balancing the inflow amount and the outflow amount to a pressure tank, by interlocking a booster pump and a vacuum pump through a variable reduction gear, and providing a pressure regulating valve to the vacuum pump side. CONSTITUTION:For example, when a leak is generated from the high pressure side to the low pressure side in a booster pump 18, the outflow amount from a pressure tank 7 by a vacuum pump 14 increases in quantity as compared with the inflow amount to the pressure tank 7 by the booster pump 8 and, as a result, the water level in the pressure tank 7 is gradually lowered. Because a leak amount comes to a nearly constant value by the characteristics of a pump system, a variable reduction gear 15 is preset manually corresponding to the lowering in the water level and the speed of the booster pump 8 is made faster than that of the vacuum pump 14 to supply pressurized water to the tank 7 in an amount corresponding to the lowering amount in the water level. In addition, the small variation of the water level in the pressure tank 7 is detected by a level meter 18 and the emitting amount from the vacuum pump 14 is adjusted by a pressure regulating valve 17.

Description

【発明の詳細な説明】 本発明は加圧浮上濃縮装置に関する。[Detailed description of the invention] The present invention relates to a pressurized flotation concentrator.

汚泥を濃縮させる場合に、この汚泥を加圧空気溶解水と
混合し、混合液を加圧浮上濃縮槽内の底部に放出し、こ
の混合液の上昇による水圧の低下にもとづいて前記加圧
溶解空気を気泡化させ、この気泡を前記汚泥に付着させ
て汚泥を浮上分離させ1分離水を下方に排出させて汚泥
を濃縮させる、いわゆる加圧浮上濃縮法がある。また、
加圧用水を昇圧させ、加圧タンク〔混気タンク)内にお
いて前記昇圧後の加圧水に圧縮空気を吹き込んで。
When concentrating sludge, this sludge is mixed with pressurized air-dissolved water, the mixed liquid is discharged to the bottom of the pressure flotation thickening tank, and the above-mentioned pressurized dissolution is performed based on the drop in water pressure caused by the rise of this mixed liquid. There is a so-called pressure flotation concentration method in which air is bubbled, the bubbles are attached to the sludge, the sludge is floated and separated, and the separated water is discharged downward to concentrate the sludge. Also,
The pressure of pressurized water is increased, and compressed air is blown into the pressurized water after the pressure increase in a pressurized tank (mixed air tank).

この空気を溶解させ、加圧空気溶解水を一旦減圧させて
これを汚泥に混合させる低圧混合法がある。
There is a low-pressure mixing method in which this air is dissolved and the pressurized air-dissolved water is once depressurized and mixed with sludge.

ところで、低圧混合法では、いったん昇圧させた加圧水
を空気溶解後再び減圧させる必要があるため、昇圧ポン
プと減圧ポンプとを互いに連動連結すれば、系内の圧力
は昇圧ポンプに対しては駆動時の抵抗となるが減圧ポン
プに対しては駆動力として作用することになるため、こ
れらは互いに打消す方向に働き、この分のエネルギ回収
を図ることができるという利点がある。前記昇圧ポンプ
および減圧ポンプとしては容積式ポンプを利用するのが
望ましいが、しかしこの容積式ポンプでは高圧側から低
圧側への加圧水のリークが避けられないという問題があ
る。すなわち、高圧側と低圧側の圧力差に応じて昇圧ポ
ンプでは流量が減じる方向に、減圧ポンプでは流量が増
加する方向に働き・加圧タンク内水位が低下するという
問題が生じる。
By the way, in the low-pressure mixing method, it is necessary to once increase the pressure of pressurized water and then reduce the pressure again after dissolving the air. Therefore, if the booster pump and the pressure-reducing pump are connected in conjunction with each other, the pressure in the system will be the same as that of the booster pump during operation. However, since it acts as a driving force on the decompression pump, these forces act in a direction that cancels each other out, and there is an advantage that this amount of energy can be recovered. It is desirable to use positive displacement pumps as the pressure boosting pump and the pressure reducing pump, but this positive displacement pump has a problem in that leakage of pressurized water from the high pressure side to the low pressure side is unavoidable. That is, depending on the pressure difference between the high-pressure side and the low-pressure side, a pressure-boosting pump works in a direction where the flow rate decreases, and a pressure-reducing pump works in a direction where the flow rate increases, causing a problem that the water level in the pressurized tank decreases.

そこで本発明は、昇圧ポンプと減圧ポンプとを互いに連
動連結した場合におけるリークを補償して、加圧タンク
への流入量と流出量をバランスさせることを目的とする
ものである。
SUMMARY OF THE INVENTION Therefore, an object of the present invention is to compensate for leakage when a booster pump and a pressure-reducing pump are connected in conjunction with each other, thereby balancing the amount of inflow and outflow to a pressurized tank.

この目的を達成するため本発明は、加圧浮上濃縮槽の分
離水を昇圧させる容積式昇圧ポンプの吐出側を、昇圧後
の加圧水に圧縮空気を送り込んで溶解させる加圧タンク
に臨ませ、前記客積式昇圧ポンプに連動してこの加圧タ
ンクからの加圧空気溶解水を減圧させる容積式減圧ポン
プを設け、減圧後の加圧空気溶解水を調圧した後汚泥と
の混合を行なう混合器へ導(調圧弁を設け、前記容積式
鯉圧ポンプと前記容積式減圧ポンプとを連動させる可変
速減速装置を設けたものである。
In order to achieve this object, the present invention makes the discharge side of a positive displacement booster pump that boosts the pressure of separated water in a pressurized flotation concentration tank face a pressurization tank that sends compressed air into the pressurized water to dissolve it. A positive displacement pressure reducing pump is provided to reduce the pressure of the pressurized air-dissolved water from the pressurized tank in conjunction with the passenger displacement booster pump, and the pressure of the reduced-pressure air-dissolved water is adjusted and then mixed with the sludge. A pressure regulating valve is provided, and a variable speed reduction device is provided to interlock the positive displacement carp pressure pump and the positive displacement pressure reducing pump.

したがって、昇圧ポンプにおけるリークによりこの昇圧
ポンプから所定量の加圧水が加圧タンク内に供給されな
くなっても、可変速減速機によって昇圧ポンプを減圧ポ
ンプよりも増速させることができるとともに、調圧弁に
よって減圧ポンプからの吐出量を絞ることができるため
、減圧ポンプによる加圧タンクからの流出量と昇圧ポン
プによる加圧タンクへの流入量とを均衡させて、前記リ
ークを補償することができ、加圧タンクの水位保持を図
って所定水量を確保することが可能となる。
Therefore, even if a predetermined amount of pressurized water is no longer supplied from the boost pump to the pressurized tank due to a leak in the boost pump, the variable speed reducer allows the boost pump to be faster than the pressure reducer pump, and the pressure regulating valve Since the discharge amount from the decompression pump can be reduced, the amount of outflow from the pressurized tank by the decompression pump and the amount of inflow into the pressurized tank by the booster pump can be balanced, and the leak can be compensated for. It becomes possible to maintain the water level in the pressure tank and secure a predetermined amount of water.

以下1本発明の一実施例を図面にもとづいて説明する。An embodiment of the present invention will be described below with reference to the drawings.

図面において(1)は汚泥貯槽であり、槽内の汚泥を混
合器(2)へ供給するための容積式給泥ポンプ(3)が
接続されている。(4)はモータである。−万(5)は
加圧浮上濃縮槽(6)における分離水を加圧用水として
貯留する分離水槽であり、槽内の分離水を昇圧して加圧
タンク(7)へ送るための容積式昇圧ポンプ(8)が接
続されている。加圧タンク(7)には。
In the drawing, (1) is a sludge storage tank, to which is connected a positive displacement sludge pump (3) for supplying sludge in the tank to a mixer (2). (4) is a motor. - 10,000 (5) is a separation water tank that stores the separated water in the pressurized flotation concentration tank (6) as pressurizing water, and is a volumetric type that increases the pressure of the separated water in the tank and sends it to the pressurizing tank (7). A boost pump (8) is connected. In the pressurized tank (7).

空気圧縮機(9)から、空気タンク(イ)、流量制御弁
αつおよび圧力調整弁(2)を介して圧縮空気が供給さ
れ、この圧縮空気が加圧水内に吹き込まれて溶解される
ようになっている。圧力調整弁■は、加圧タンク(7)
の圧力検出器斡からめ信号により開度調節されている。
Compressed air is supplied from the air compressor (9) through the air tank (a), the flow rate control valve α, and the pressure adjustment valve (2), and this compressed air is blown into the pressurized water and dissolved. It has become. Pressure adjustment valve ■ is pressurized tank (7)
The opening is adjusted by a signal from the pressure sensor.

(141は加圧タンク(7)からの加圧空気溶解水を減
圧させる容積式減圧ポンプであり、この減圧ポンプα上
と011記昇圧ポンプ(8)とは、可変速減速機(へ)
を介して互いに連動されている。qQは両ポンプ(8)
(ト)を駆動させるためのモータである。またa’tt
は減圧ポンプo4からの減圧流加圧空気溶解水を調圧し
た後混合器(2)へ導く調圧弁であり、加圧タンク(7
)のレベル計[相]からの信号により開度調節されるよ
うになっている。(ト)は減圧ポンプ9畳と調圧弁a′
I)との間における圧力指示計である。なお、混合器(
2)内では汚泥と減圧後の加圧空気溶解水とが低圧混合
され、混合液は加圧浮上濃縮槽(6)へ供給されるよう
になっている。
(141 is a positive displacement pressure reducing pump that reduces the pressure of pressurized air-dissolved water from the pressurized tank (7), and this pressure reducing pump α and 011 boost pump (8) are connected to the variable speed reducer (to)
are linked to each other via. qQ is both pumps (8)
This is a motor for driving (g). Also a'tt
is a pressure regulating valve that regulates the pressure of the reduced pressure flow pressurized air-dissolved water from the reduced pressure pump o4 and then guides it to the mixer (2).
) The opening is adjusted by the signal from the level meter [phase]. (g) is the pressure reducing pump 9 tatami and the pressure regulating valve a'
I) is a pressure indicator between the In addition, the mixer (
2), sludge and decompressed pressurized air-dissolved water are mixed under low pressure, and the mixed liquid is supplied to the pressurized flotation concentration tank (6).

このような構成によれば1分離水槽(5)内の加圧用水
は、容積式昇圧ポンプ(8)により昇圧された後加圧タ
ンク(7)に送られ、この加圧タンク(7)内で空気が
溶解され、容積式減圧ポンプσ→により一旦減圧され・
調圧弁Qηにて調圧すなわちさらに減圧された後に、混
合器(2)へ送られる。また汚泥貯槽(1)内の汚泥は
給泥ポンプ(3)により混合器(2)に送られ、混合器
(2)内で加圧空気溶解水と低圧混合される。
According to this configuration, the pressurized water in the one-separation water tank (5) is pressurized by the positive displacement booster pump (8) and then sent to the pressurizing tank (7). The air is dissolved and the pressure is reduced once by the positive displacement pump σ→.
After being pressure regulated, that is, further reduced in pressure, by the pressure regulating valve Qη, it is sent to the mixer (2). Further, the sludge in the sludge storage tank (1) is sent to the mixer (2) by the sludge pump (3), and mixed with pressurized air-dissolved water at low pressure in the mixer (2).

混合液は加圧浮上濃縮槽(6)内に放出されて汚泥が浮
上分離され1分離水は分離水槽(5)へ送られて系内を
循環される。浮上汚泥は加圧浮上濃縮槽(6)水面に設
けた汚泥排出装置により外部に排出される〔図示せず)
The mixed liquid is discharged into a pressurized flotation concentration tank (6), the sludge is floated and separated, and the separated water is sent to a separation water tank (5) and circulated within the system. The floated sludge is discharged to the outside by a sludge discharge device installed on the water surface of the pressurized flotation thickener tank (6) (not shown)
.

このとき、たとえば昇圧ポンプ(8)において高圧側か
ら低圧側へのリークが発生すれば、減圧ポンプα◆によ
る加圧タンク(7)からの流出量が、昇圧ポンプ(8)
による加圧タンク(7)への流入量よりも多くなり、こ
の結果加圧タンク(7)内の水位が徐々に低下すること
になる。リーク量はポンプ系の特性等によりほぼ一定の
値となるため、これに対応して可変速減速機(ト)を予
めマニアル設定し、減圧ポンプ(ロ)、Jlよりも昇圧
ポンプ(8)を増速させて、前記水位低下分に相当する
量の加圧水を加圧タンク(7)内に供給させる。また、
加圧タンク(7)内水位に日間変動等の小変動が生じた
場合には、レベル計(ロ)にてこれを検知し、調圧弁α
ηの開度を調節して減圧ポンプα◆からの吐出量を調整
する。すなわち、可変速減速機011においては粗調節
を行ない、かつ調圧弁αηにおいては微調節を行なうこ
とになって。
At this time, for example, if a leak occurs from the high pressure side to the low pressure side in the boost pump (8), the amount of flow from the pressurized tank (7) caused by the pressure reducing pump α◆ will be
As a result, the water level in the pressurized tank (7) gradually decreases. Since the amount of leakage is a nearly constant value depending on the characteristics of the pump system, etc., the variable speed reducer (G) is manually set in advance to accommodate this, and the boost pump (8) is used rather than the decompression pump (B) and JL. The speed is increased to supply pressurized water in an amount corresponding to the water level drop into the pressurized tank (7). Also,
If there are small fluctuations in the water level in the pressurized tank (7), such as daily fluctuations, this will be detected by the level meter (b) and the pressure regulating valve α will be activated.
Adjust the opening of η to adjust the discharge amount from the pressure reducing pump α◆. That is, the variable speed reduction gear 011 is to be roughly adjusted, and the pressure regulating valve αη is to be finely adjusted.

これらにより加圧タンク(7)内の水位が保持されるこ
とになる。
These will maintain the water level in the pressurized tank (7).

以上述べたように本発明によると、昇圧ポンプにおける
リークによりこの昇圧ポンプから所定量の加圧水が加圧
タンク内に供給されなくなっても、可変速減速機によっ
て昇圧ポンプを減圧ポンプよりも増速させることができ
るとともに、調圧弁によって減圧ポンプからの吐出量を
絞ることができるため、減圧ポンプによる加圧タンクか
らの流出量と昇圧ポンプによる加圧タンクへの流入量と
を均衡させて、 ffQ記リークを補償することができ
As described above, according to the present invention, even if a predetermined amount of pressurized water is not supplied from the boost pump into the pressurized tank due to a leak in the boost pump, the boost pump is sped up more than the pressure reducer pump by the variable speed reducer. At the same time, the discharge amount from the pressure reducing pump can be restricted by the pressure regulating valve, so the amount of outflow from the pressurized tank due to the pressure reducing pump and the amount of inflow into the pressurized tank due to the boosting pump are balanced, and the ffQ Can compensate for leaks.

加圧タンクの水位保持を図って所定水量を確保すること
が可能となる。
It becomes possible to maintain the water level in the pressurized tank and secure a predetermined amount of water.

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

図面は本発明の一実施例の概略構成を示す図である。 (2]−°゛混合器、(5)・・・分離水槽t (a)
 ”’加圧浮上濃縮槽、(7)・・・加圧タンク、(8
)・・・容積式昇圧ポンプ1a◆・・・容積式減圧ポン
プ、(ト)・・・可変速減速機、ση・・・調圧弁 代理人 森本義弘
The drawings are diagrams showing a schematic configuration of an embodiment of the present invention. (2) - ° Mixer, (5)...separation water tank t (a)
”' Pressurized flotation concentration tank, (7) ... Pressurized tank, (8
)...Positive displacement boosting pump 1a◆...Positive displacement pressure reducing pump, (G)...Variable speed reducer, ση...Pressure regulating valve agent Yoshihiro Morimoto

Claims (1)

【特許請求の範囲】[Claims] 1、 加圧浮上濃縮槽の分離水を昇圧させる容積式昇圧
ポンプの吐出側を、昇圧後の加圧水に圧縮空気を送り込
んで溶解させる加圧タンクに臨ませ、n記容積式昇圧ポ
ンプに連動してこの加圧タンクからの加圧空気溶解水を
減圧させる容積式減圧ポンプを設け、減圧後の加圧空気
溶解水を調圧した後汚泥との混合を行なう混合器へ導く
調圧弁を設け、前記容積式昇圧ポンプと前記容積式減圧
ポンプとを連動させる可変速減速装置を設けたことを特
徴とする加圧浮上濃縮装置。
1. The discharge side of the positive displacement boost pump that boosts the pressure of the separated water in the pressurized flotation concentration tank faces the pressure tank that sends compressed air into the pressurized water to dissolve it, and is linked to the positive displacement boost pump described in n. A positive displacement pressure reducing pump is provided to reduce the pressure of the pressurized air dissolved water from the pressurized tank, and a pressure regulating valve is provided to guide the reduced pressure air dissolved water to a mixer where it is mixed with sludge after regulating the pressure. A pressurized flotation concentrator characterized in that a variable speed reduction device is provided for interlocking the positive displacement boost pump and the positive displacement decompression pump.
JP14174083A 1983-08-01 1983-08-01 Pressure float concentration apparatus Pending JPS6031879A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP14174083A JPS6031879A (en) 1983-08-01 1983-08-01 Pressure float concentration apparatus

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP14174083A JPS6031879A (en) 1983-08-01 1983-08-01 Pressure float concentration apparatus

Publications (1)

Publication Number Publication Date
JPS6031879A true JPS6031879A (en) 1985-02-18

Family

ID=15299097

Family Applications (1)

Application Number Title Priority Date Filing Date
JP14174083A Pending JPS6031879A (en) 1983-08-01 1983-08-01 Pressure float concentration apparatus

Country Status (1)

Country Link
JP (1) JPS6031879A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5904763A (en) * 1995-03-24 1999-05-18 Blocken; Wilfried Insulating mortar

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5904763A (en) * 1995-03-24 1999-05-18 Blocken; Wilfried Insulating mortar

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