JPS6369518A - Pressurized electric permeation dehydrator - Google Patents

Pressurized electric permeation dehydrator

Info

Publication number
JPS6369518A
JPS6369518A JP61214503A JP21450386A JPS6369518A JP S6369518 A JPS6369518 A JP S6369518A JP 61214503 A JP61214503 A JP 61214503A JP 21450386 A JP21450386 A JP 21450386A JP S6369518 A JPS6369518 A JP S6369518A
Authority
JP
Japan
Prior art keywords
slurry
plate
filter plate
pressurizing
receiving vessel
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
JP61214503A
Other languages
Japanese (ja)
Inventor
Hideyuki Oohanamori
英幸 大花森
Hiroshi Hoshikawa
星川 寛
Masataka Yoshida
吉田 正孝
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.)
Fuji Electric Co Ltd
Original Assignee
Fuji Electric Co Ltd
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 Fuji Electric Co Ltd filed Critical Fuji Electric Co Ltd
Priority to JP61214503A priority Critical patent/JPS6369518A/en
Publication of JPS6369518A publication Critical patent/JPS6369518A/en
Pending legal-status Critical Current

Links

Landscapes

  • Separation Using Semi-Permeable Membranes (AREA)
  • Treatment Of Sludge (AREA)

Abstract

PURPOSE:To obtain high dehydrating rate, by carrying out electric permeation to slurry supplied in a slurry receiving vessel between a filter plate and a pressurizing plate. CONSTITUTION:The slurry to be dehydrated is introduced to the slurry receiving vessel 1 through a supply pipe 51 opened to the side surface of the slurry receiving vessel 1. When a specified amount of slurry is introduced in the slurry receiving vessel 1, a vacuum pump 32 is started to decompress the inside of a vacuum chamber 3. Then, the pressurizing plate 7 is moved downward by pressurizing cylinders 71 to mechanically press the slurry to the filter plate 2, and a direct current voltage is impressed between electrode plates 81 and 82. Dehydration of the slurry is carried out by the vacuum suction force, mechanical pressure and electric permeating action.

Description

【発明の詳細な説明】[Detailed description of the invention] 【発明の属する技術分野】[Technical field to which the invention pertains]

この発明は下水、し尿処理により発生する汚泥等を被脱
水処理物として脱水操作により汚泥をケーキ化する加圧
型電気浸透脱水装置に関する。
The present invention relates to a pressurized electroosmotic dewatering apparatus that uses sludge or the like generated from sewage or human waste treatment as a material to be dehydrated, and converts the sludge into a cake through a dewatering operation.

【従来技術とその問題点】[Prior art and its problems]

頭記した汚泥の脱水処理装置として第2図に示す如き真
空脱水装置が公知である。すなわち第2図において、1
はスラリ受槽、2は濾過板、3は真空室、4はベルト式
濾布であり、スラリ受槽1゜真空室3は濾過板2を挟ん
でその上下に配備されている。また前記のスラリ受槽1
は濾過板2に対して昇降シリンダ11により昇降操作さ
れる底面開放の容器であり、その上方にはスラリ供給ホ
ッパ5が配置しである。また真空室3には真空槽31を
介して真空ポンプ32が接続され、かつ真空槽31の底
部に弁33を介して濾液排出ライン34が引き出し配管
されている。一方、濾布4はプーリ間に張架されたエン
ドレスの濾布であり、駆動モータ41により濾過4Ii
、1の上面側を移動操作される。なお42G! 濾布4
1に対向する脱水ケーキのスクレーバ、43は濾布洗浄
ノズルである。 かかる構成でスラリ受槽lに泥弱を投入し、この状態で
真空ポンプ32を始動して真空室3内を減圧することに
より泥脩中の含有水が濾過板2を透過して真空室3内に
吸引排出され、濾布の上面側には脱水された泥概が残る
。続いてスラリ受槽1を上昇操作して濾布4がら切り離
し、駆動モータ41により濾布4を移動させることによ
り、脱水物はスクレーパ42で濾布4より掻き取られて
脱水ケ−キロとして回収される。一方、濾過板2を透過
して真空室3内に排出された濾液は真空槽31の底部に
溜り、ここから弁33の開放により濾液排出ライン34
を通じて系外に排水される。 ところで上記した従来の真空脱水装置では真空室3内の
減圧が周囲の大気圧によって制約を受け、しかも脱水の
進行に伴って濾布4の目詰まりが生じ、かつ脱水ケーキ
の成長とともに濾液の通過する濾過抵抗が増大して脱水
効果が急速に低下する。 このために従来では汚泥等に高分子凝集剤を添加する等
して脱水性の改善を図っているが、それでも脱水率には
限界があって脱水ケーキを焼却処分できる程度の低含水
率まで脱水させることが困難であり、その改善策が望ま
れている。
As the sludge dewatering apparatus mentioned above, a vacuum dehydrating apparatus as shown in FIG. 2 is known. That is, in Figure 2, 1
1 is a slurry receiving tank, 2 is a filter plate, 3 is a vacuum chamber, and 4 is a belt type filter cloth. In addition, the slurry receiving tank 1
is a container with an open bottom that is raised and lowered by a lifting cylinder 11 relative to a filter plate 2, and a slurry supply hopper 5 is disposed above the container. A vacuum pump 32 is connected to the vacuum chamber 3 via a vacuum tank 31, and a filtrate discharge line 34 is connected to the bottom of the vacuum tank 31 via a valve 33. On the other hand, the filter cloth 4 is an endless filter cloth stretched between pulleys.
, 1 is moved on the upper surface side. In addition, 42G! Filter cloth 4
1 is a dewatered cake scraper, and 43 is a filter cloth cleaning nozzle. With this configuration, mud is poured into the slurry receiving tank l, and in this state, the vacuum pump 32 is started to reduce the pressure inside the vacuum chamber 3, so that the water contained in the slurry passes through the filter plate 2 and flows into the vacuum chamber 3. The dehydrated slurry remains on the upper surface of the filter cloth. Subsequently, the slurry receiving tank 1 is lifted to separate it from the filter cloth 4, and the filter cloth 4 is moved by the drive motor 41, so that the dehydrated material is scraped off from the filter cloth 4 by the scraper 42 and recovered as a dehydrated cake kilo. Ru. On the other hand, the filtrate that has passed through the filter plate 2 and is discharged into the vacuum chamber 3 accumulates at the bottom of the vacuum chamber 31, and from there, when the valve 33 is opened, the filtrate is discharged into the filtrate discharge line 34.
is drained out of the system through the By the way, in the above-mentioned conventional vacuum dehydration apparatus, the reduced pressure in the vacuum chamber 3 is restricted by the surrounding atmospheric pressure, and as the dehydration progresses, the filter cloth 4 becomes clogged, and as the dehydrated cake grows, the filtrate passes through. The filtration resistance increases and the dehydration effect rapidly decreases. To this end, conventional efforts have been made to improve dewatering properties by adding polymer flocculants to sludge, etc., but there is still a limit to the dewatering rate, and the dewatering cake can be dehydrated to a low enough water content that it can be disposed of by incineration. It is difficult to do so, and improvement measures are desired.

【発明の目的】 この発明は上記の点にかんがみなされたものであり、従
来の脱水装置に電気浸透および加圧脱水方式を組み入れ
ることにより高い脱水率が得られるようにした加圧型電
気浸透脱水装置を提供することを目的とする。
[Object of the Invention] The present invention has been made in view of the above points, and is a pressurized electroosmotic dehydration device that can obtain a high dehydration rate by incorporating electroosmosis and pressure dehydration methods into a conventional dehydration device. The purpose is to provide

【発明の要点】[Key points of the invention]

上記目的を達成するために、この発明は 濾過板と、該
濾過板を挟んでその上下に配備したスラリ受槽および真
空室と、スラリ受槽内に供給した泥漿を濾過板側へ加圧
する加圧板およびその加圧操作手段と、前記濾過板とこ
れに対向する加圧板との間で電気浸透操作を行う直流電
圧印加手段とを具備することにより、泥漿に対して真空
による減圧に加え、機械的な加圧、および電気浸透を作
用させて高い脱水率が得られるようにしたものである。
In order to achieve the above object, the present invention includes a filter plate, a slurry receiving tank and a vacuum chamber arranged above and below the filter plate, and a pressure plate that pressurizes the slurry supplied into the slurry receiving tank toward the filter plate. and a pressurizing operation means for the same, and a direct current voltage applying means for performing an electroosmosis operation between the filter plate and the pressure plate facing the filter plate, so that in addition to reducing the pressure by vacuum, mechanical A high dehydration rate can be obtained by applying high pressure and electroosmosis.

【発明の実施例】[Embodiments of the invention]

第1図はこの発明の実施例による加圧型電気浸透脱水装
置の構成を示すものであり、第2図と同一部材には同じ
符号が付しである。すなわちこの発明により、スラリ受
槽1の内部には槽内面域を覆って油圧ないし空気圧式の
加圧シリンダ71で駆動操作される加圧板7が配備され
ている。なお72は加圧板7の周縁に設けたシール材で
ある。さらに加えて前記加圧板7の内面側およびこれに
対向する濾過板2の裏面側に電極板81.82を配し、
この電極板81と82の間に直流電源83を接続して電
気浸透用の電圧印加手段8が装備されている。なお電極
板82は穴あき電極板として成る。 次に上記構成による泥漿の脱水動作に付いて説明する。 まず被脱水物である泥漿はスラリ受槽1の側面に開口す
る供給管51を通じてスラリ受槽内に導入される。この
際に加圧板7は上昇位置に待機している。ここでスラリ
受槽l内に所定量の泥漿が導入されると、次に真空ポン
プ32を始動して真空室3内を減圧するとともに、加圧
シリンダ71の操作により加圧板7を下降移動して泥漿
を濾過板2に向けて機械的に加圧し、さらに電極板81
と82との間に直流電圧を印加する。 これにより泥漿中に含まれている水分は真空吸引力1機
械的加圧力による真空、加圧脱水作用に加え、電気浸透
作用により陰極側、つまりiIi過板側の電極板82の
方に移動して泥漿中より濾布4および濾過板2を透過し
、真空室3内へ濾過、排出されるようになる。しかもこ
の脱水操作の進行に伴って泥漿が減容すると、電極板8
1と82の間の間隔が次第に狭って電極板間の電界強度
が強まって電気浸透作用がより一層高まるようになり、
かくして脱水の困難な汚泥等も充分な低含水率まで直接
脱水できるようになる。なお泥漿から脱水分離された濾
液の排出、並びに脱水ケーキの回収は第2図に述べたと
同様に行われる。
FIG. 1 shows the configuration of a pressurized electroosmotic dehydrator according to an embodiment of the present invention, and the same members as in FIG. 2 are given the same reference numerals. That is, according to the present invention, inside the slurry receiving tank 1, a pressure plate 7 is provided which covers the inner surface area of the tank and is driven and operated by a hydraulic or pneumatic pressure cylinder 71. Note that 72 is a sealing material provided around the periphery of the pressure plate 7. Furthermore, electrode plates 81 and 82 are arranged on the inner surface side of the pressure plate 7 and the back side of the filter plate 2 opposite thereto,
A DC power supply 83 is connected between the electrode plates 81 and 82 to provide voltage application means 8 for electroosmosis. Note that the electrode plate 82 is formed as a perforated electrode plate. Next, the dewatering operation of the slurry with the above configuration will be explained. First, slurry, which is a material to be dehydrated, is introduced into the slurry receiving tank 1 through a supply pipe 51 that opens on the side surface of the slurry receiving tank 1 . At this time, the pressure plate 7 is waiting at the raised position. When a predetermined amount of slurry is introduced into the slurry receiving tank l, the vacuum pump 32 is then started to reduce the pressure in the vacuum chamber 3, and the pressure plate 7 is moved downward by operating the pressure cylinder 71. The slurry is mechanically pressurized toward the filter plate 2, and then the electrode plate 81
A DC voltage is applied between and 82. As a result, the water contained in the slurry moves toward the cathode side, that is, the electrode plate 82 on the iii overplate side, due to the vacuum suction force 1, the vacuum and pressure dehydration effect due to the mechanical pressure force, and the electroosmosis effect. The slurry passes through the filter cloth 4 and the filter plate 2, and is filtered and discharged into the vacuum chamber 3. Moreover, as the volume of the slurry decreases with the progress of this dehydration operation, the electrode plate 8
As the distance between 1 and 82 gradually narrows, the electric field strength between the electrode plates increases, and the electroosmotic effect further increases.
In this way, sludge and the like that are difficult to dewater can be directly dehydrated to a sufficiently low water content. Note that the discharge of the filtrate dehydrated and separated from the slurry and the collection of the dehydrated cake are performed in the same manner as described in FIG.

【発明の効果】【Effect of the invention】

以上述べたようにこの発明によれば、 濾過板と、該濾
過板を挟んでその上下に配備したスラリ受槽および真空
室と、スラリ受槽内に供給した泥漿を濾過板側へ加圧す
る加圧板およびその加圧操作手段と、前記濾過板とこれ
に対向する加圧板との間で電気浸透操作を行う直流電圧
印加手段とを具備して構成したことにより、従来の脱水
装置では直接脱水が困難であった汚泥等も充分に低含水
率まで脱水させることが可能な性能の優れた脱水装置を
提供することができる。
As described above, according to the present invention, there are provided a filter plate, a slurry receiving tank and a vacuum chamber disposed above and below the filter plate, and a pressure plate that pressurizes the slurry supplied into the slurry receiving tank toward the filter plate. Since it is configured to include a pressurizing operation means and a DC voltage applying means for performing electroosmotic operation between the filter plate and the opposing pressure plate, direct dehydration is difficult with conventional dehydrating equipment. It is possible to provide a dewatering device with excellent performance that can dehydrate even sludge and the like to a sufficiently low water content.

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

第1図はこの発明の実施例による加圧型電気浸透脱水装
置の構成配置図、第2図は従来における真空脱水装置の
構成配置図である。各図において、1ニスラリ受槽、2
:濾過板、3:真空室、7:加圧板、71:加圧シリン
ダ、8:直流電圧印加手段、81.82=電極板、83
:直流電源。 第1図
FIG. 1 is a structural layout diagram of a pressurized electroosmotic dehydrator according to an embodiment of the present invention, and FIG. 2 is a structural layout diagram of a conventional vacuum dehydrator. In each figure, 1 Nislari receiver, 2
: filter plate, 3: vacuum chamber, 7: pressure plate, 71: pressure cylinder, 8: DC voltage application means, 81.82 = electrode plate, 83
:DC power supply. Figure 1

Claims (1)

【特許請求の範囲】[Claims] 濾過板と、該濾過板を挟んでその上下に配備したスラリ
受槽および真空室と、スラリ受槽内に供給した泥漿を濾
過板側へ加圧する加圧板およびその加圧操作手段と、前
記濾過板とこれに対向する加圧板との間で電気浸透操作
を行う直流電圧印加手段とを具備して成ることを特徴と
する加圧型電気浸透脱水装置。
A filter plate, a slurry receiving tank and a vacuum chamber disposed above and below the filter plate, a pressurizing plate and its pressurizing operation means for pressurizing the slurry supplied into the slurry receiving tank toward the filter plate, and the filter plate. 1. A pressurized electroosmotic dehydration apparatus comprising: a DC voltage applying means for performing an electroosmotic operation between the pressurizing plate and the pressurizing plate facing the pressurizing plate.
JP61214503A 1986-09-11 1986-09-11 Pressurized electric permeation dehydrator Pending JPS6369518A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP61214503A JPS6369518A (en) 1986-09-11 1986-09-11 Pressurized electric permeation dehydrator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP61214503A JPS6369518A (en) 1986-09-11 1986-09-11 Pressurized electric permeation dehydrator

Publications (1)

Publication Number Publication Date
JPS6369518A true JPS6369518A (en) 1988-03-29

Family

ID=16656792

Family Applications (1)

Application Number Title Priority Date Filing Date
JP61214503A Pending JPS6369518A (en) 1986-09-11 1986-09-11 Pressurized electric permeation dehydrator

Country Status (1)

Country Link
JP (1) JPS6369518A (en)

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2002233874A (en) * 2001-02-09 2002-08-20 Nippon Chemicon Corp Electrosmosis apparatus
CN101472669A (en) * 2006-06-14 2009-07-01 艾尔科泰克技术公司 Processes and apparatuses for treating and/or increasing dryness of a substance
JP2011072863A (en) * 2009-09-29 2011-04-14 Kurita Water Ind Ltd Electroosmotic dewatering apparatus
CN104801094A (en) * 2015-04-29 2015-07-29 济南圣泉集团股份有限公司 Solid-liquid separator
CN105923977A (en) * 2016-06-21 2016-09-07 饶宾期 Electroosmosis and pressure filtration coupled sewage sludge dehydrating device
CN105923968A (en) * 2016-06-21 2016-09-07 饶宾期 Sewage sludge dewatering device based on cooperation of oxidization, electroosmosis and mechanical filter pressing
CN105967485A (en) * 2016-05-26 2016-09-28 饶宾期 Sewage sludge oxidation electroosmosis mechanical filter pressing cooperated dehydration method
CN106396303A (en) * 2016-06-21 2017-02-15 饶宾期 A sewage and sludge dehydrating device coupling electroosmosis and mechanical pressure filtration

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS515862A (en) * 1974-07-01 1976-01-19 Seiken Reiki Kk Odeino datsusuihoho

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS515862A (en) * 1974-07-01 1976-01-19 Seiken Reiki Kk Odeino datsusuihoho

Cited By (15)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2002233874A (en) * 2001-02-09 2002-08-20 Nippon Chemicon Corp Electrosmosis apparatus
JP4638615B2 (en) * 2001-02-09 2011-02-23 日本ケミコン株式会社 Electroosmosis equipment
CN101472669A (en) * 2006-06-14 2009-07-01 艾尔科泰克技术公司 Processes and apparatuses for treating and/or increasing dryness of a substance
JP2009539587A (en) * 2006-06-14 2009-11-19 レ テクノロジーズ エルコテック インコーポレイテッド Process and apparatus for treating a substance and / or increasing its dryness
US8454814B2 (en) 2006-06-14 2013-06-04 GL&V Canada Processes and apparatuses for treating and/or increasing dryness of a substance
JP2011072863A (en) * 2009-09-29 2011-04-14 Kurita Water Ind Ltd Electroosmotic dewatering apparatus
CN104801094A (en) * 2015-04-29 2015-07-29 济南圣泉集团股份有限公司 Solid-liquid separator
CN105967485A (en) * 2016-05-26 2016-09-28 饶宾期 Sewage sludge oxidation electroosmosis mechanical filter pressing cooperated dehydration method
CN105967485B (en) * 2016-05-26 2019-01-29 中国计量大学 Sewage sludge aoxidizes electro-osmosis mechanism filter-pressing and cooperates with dewatering
CN105923977A (en) * 2016-06-21 2016-09-07 饶宾期 Electroosmosis and pressure filtration coupled sewage sludge dehydrating device
CN105923968A (en) * 2016-06-21 2016-09-07 饶宾期 Sewage sludge dewatering device based on cooperation of oxidization, electroosmosis and mechanical filter pressing
CN106396303A (en) * 2016-06-21 2017-02-15 饶宾期 A sewage and sludge dehydrating device coupling electroosmosis and mechanical pressure filtration
CN105923968B (en) * 2016-06-21 2019-03-26 中国计量大学 Sewage sludge dehydration device based on oxidation electro-osmosis mechanism filter-pressing collaboration
CN106396303B (en) * 2016-06-21 2019-03-26 中国计量大学 The sewage sludge dehydration device that electro-osmosis is coupled with mechanism filter-pressing
CN105923977B (en) * 2016-06-21 2019-03-26 中国计量大学 The sewage sludge dehydration device of electro-osmosis filters pressing coupling

Similar Documents

Publication Publication Date Title
JPS621426A (en) Electroosmotic dehydration apparatus
JPS6369518A (en) Pressurized electric permeation dehydrator
JP2018192431A (en) Solid-liquid separator, and solid-liquid separation method for solid-liquid mixture
CN109293219A (en) Sludge dehydration device
CN210560030U (en) Sludge deep dehydration equipment of quick consolidation
EP0367792A1 (en) Two-stage batch filter apparatus and filtration process
CN219239492U (en) Self-suction type filter pressing dehydration equipment and solid-liquid separator
CN205152036U (en) Sludge thickener and drier combination
KR101435308B1 (en) Solid-Liquid separation method
US3812971A (en) An apparatus for dehydrating a slurry
JPH0819897A (en) Solid-liquid separation device and squeeze dehydration device
CN204434447U (en) A kind of follow-on sludge vacuum dewatering unit
JPS58122085A (en) Dehydrating method
CN217600575U (en) Drying treatment device for printing and dyeing sludge
JP2988576B2 (en) Filtration and concentration of sludge
CN205549712U (en) High pressure combination squeezer
JPH0852307A (en) Filter press
CN219585963U (en) Mud dewatering device for sewage treatment
CN214735295U (en) Drying treatment system for printing and dyeing sludge
JPH02115012A (en) Sludge dehydration apparatus
JP3105216U (en) Dredging dewatering equipment
CN217628073U (en) Device for efficiently collecting percolate
JPH02258005A (en) Dehydration treatment
JPS6155407B2 (en)
JPS6253208B2 (en)