JPS58122085A - Dehydrating method - Google Patents

Dehydrating method

Info

Publication number
JPS58122085A
JPS58122085A JP57003613A JP361382A JPS58122085A JP S58122085 A JPS58122085 A JP S58122085A JP 57003613 A JP57003613 A JP 57003613A JP 361382 A JP361382 A JP 361382A JP S58122085 A JPS58122085 A JP S58122085A
Authority
JP
Japan
Prior art keywords
additives
dehydrated
additive
sludge
electric power
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
JP57003613A
Other languages
Japanese (ja)
Inventor
Susumu Nishikawa
進 西川
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.)
Mitsubishi Heavy Industries Ltd
Original Assignee
Mitsubishi Heavy Industries 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 Mitsubishi Heavy Industries Ltd filed Critical Mitsubishi Heavy Industries Ltd
Priority to JP57003613A priority Critical patent/JPS58122085A/en
Publication of JPS58122085A publication Critical patent/JPS58122085A/en
Pending legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D61/00Processes of separation using semi-permeable membranes, e.g. dialysis, osmosis or ultrafiltration; Apparatus, accessories or auxiliary operations specially adapted therefor
    • B01D61/42Electrodialysis; Electro-osmosis ; Electro-ultrafiltration; Membrane capacitive deionization
    • B01D61/56Electro-osmotic dewatering

Landscapes

  • Engineering & Computer Science (AREA)
  • Water Supply & Treatment (AREA)
  • Health & Medical Sciences (AREA)
  • Urology & Nephrology (AREA)
  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Treatment Of Sludge (AREA)

Abstract

PURPOSE:To reduce dehydration time and electric power consumption, by adding an additive having high hydrating power beforehand to a material to be dehydrated, dehydrating said material by an electrosmosis method, and, if necessary, by recovering said additive by using a reverse osmosis membrane. CONSTITUTION:An electrode 2 is provided to the second half of a dehyrator 1 such as a belt press, and electric power is applied thereto from an electric power source device 2. After sludge 6 is mixed with flocculating agents 7 and additives 8 having high hydrating power, the sludge is supplied to a dehydrator 1 and is thus dehydrated. Dehydrated cake 12 is discharged to the outside of the system and separated filtrate 9 is passed through a reverse osmosis membrane 4, whereby the above-described additives 10 are recovered and reused. If the filtrate 9 is pressurized by using the membrane 4, the additives are recovered as they are, and it is only necessary to make up the additives by as much as the additives contained in the cake 12 and discharged. The consumption of the additives is decreased considerably.

Description

【発明の詳細な説明】 来の電気浸透法を用いた脱水方法の改良に関する。[Detailed description of the invention] This paper relates to improvements in dehydration methods using conventional electroosmosis methods.

上水汚泥、産業廃水汚泥などの処理施設に於いて脱水ケ
ーキの含水率の低下は最終処分の焼却埋立での消エネル
ギ、低容量化の目的で必要なものである。
In treatment facilities for clean water sludge, industrial wastewater sludge, etc., lowering the moisture content of dehydrated cakes is necessary for the purpose of energy consumption and capacity reduction in final disposal by incineration and landfill.

従来用いられている電気浸透法による脱水処理法は、被
脱水物を加電し、液体中のイオ/が陰極に移動する間に
イオ/が水分子と共に移動することにより脱水する方法
である。
A conventionally used dehydration treatment method using electroosmosis is a method in which a substance to be dehydrated is electrically charged, and while io/ in the liquid moves to the cathode, the io/ moves together with water molecules, thereby dehydrating the object.

しかし電気浸透法に限らず、フィルタプレス等の機械的
加圧力による脱水機でも含水率に限界が有り、また特に
電気浸透法では電力消費量が大きく、脱水時間が長いと
いう欠点があり、これを改善するにはかなりの加圧力が
必要となる。
However, not only the electroosmosis method, but also dehydration machines that use mechanical pressure such as filter presses have a limit to the water content, and the electroosmosis method in particular has the drawbacks of high power consumption and long dehydration time. Considerable pressure is required to improve this.

本発明は、このような電気浸透法の欠点を改善し、また
従来のものより性能(含水率など)面でも優れた脱水方
法を提案するもので、電気浸透法による脱水方法におい
て、被脱水物中にイオン化した時に水利力が強く、電場
における移動度の大きい電解質の添加剤、例えば塩化ア
ルミ、塩化カルシウム、臭化マグネシウムなどを加える
ことにより、脱水時の時間の短縮、消費電力の削減をね
らったものであり、さらにこの添加剤は大半が脱水時に
分離液中に含まれるため、この添加剤の消費量を減すた
めに逆浸透圧を利用した膜を使って回収し、再利用する
ことを特徴とする。
The present invention aims to improve the drawbacks of the electroosmosis method and to propose a dehydration method that is superior in terms of performance (water content, etc.) than conventional methods. By adding electrolyte additives, such as aluminum chloride, calcium chloride, and magnesium bromide, which have a strong water use capacity when ionized and have high mobility in an electric field, we aim to shorten the dehydration time and reduce power consumption. Moreover, most of this additive is contained in the separated liquid during dehydration, so in order to reduce the consumption of this additive, it is possible to recover it using a membrane that uses reverse osmosis and reuse it. It is characterized by

次に本発明方法の一実施例を図面に基いて説明する。第
1図は本実施例の装置を示し、図中、脱水機1は従来か
ら有るベルトプレス等の脱水機で、本脱水機後半に電極
2を設け、電源装置3により加電する。汚泥6は凝集剤
7および水利力が強い添加剤8と共に混和槽5で混合さ
れて脱水機1に供給脱水され、脱水ケーキ12として排
出される。脱水機1で分離されたF液9は浸透膜4で前
記添加剤10を回収し、再利用する。
Next, an embodiment of the method of the present invention will be explained based on the drawings. FIG. 1 shows the apparatus of this embodiment. In the figure, a dehydrator 1 is a conventional dehydrator such as a belt press, an electrode 2 is provided in the latter half of the dehydrator, and electricity is applied by a power supply 3. The sludge 6 is mixed in a mixing tank 5 with a flocculant 7 and an additive 8 having a strong water utilization power, supplied to a dehydrator 1, dehydrated, and discharged as a dewatered cake 12. The F liquid 9 separated in the dehydrator 1 collects the additive 10 in the permeable membrane 4 and reuses it.

なお図中、11は処理水、13は混和槽5に設けられた
かく拌器である。
In addition, in the figure, 11 is treated water, and 13 is a stirrer provided in the mixing tank 5.

本装置では、電極2はF布の上下もしくはF布そのもの
が電極となり、−次脱水後の汚泥に電場を与える。浸透
膜4は加えた添加剤8の浸透圧以上に加圧される。電極
2により加電された汚泥中の水分は更に水分中の添加剤
の水利力が加わってより短い時間で濾過され、従ってこ
の間の電力消費量も少く、脱水ケーキ中の水分も低下す
る。
In this device, the electrodes 2 are the upper and lower portions of the F cloth or the F cloth itself, and apply an electric field to the sludge after secondary dewatering. The permeable membrane 4 is pressurized to a level higher than the osmotic pressure of the additive 8 added. The water in the sludge electrified by the electrode 2 is further filtered in a shorter time due to the water utilization power of the additives in the water, so the power consumption during this time is also reduced and the water content in the dewatered cake is also reduced.

F液9中に含′まれる添加剤は通常は処理水として排出
されるが、泥液を浸透膜を利用して加圧することによシ
添加剤はそのまま回収され、脱水ケーキ中に含まれて排
出されるものだけ、メークアンプすれば良く、添加剤の
消費量もほんのわずかで済む。
The additives contained in the F liquid 9 are normally discharged as treated water, but by pressurizing the slurry using a permeable membrane, the additives are recovered as they are and are contained in the dehydrated cake. It is only necessary to make up the substances that are emitted during the process, and the amount of additives consumed is very small.

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

第1図は本発明方法の一実施例を示すフローチャートで
るる。 1・・・脱水機、2・・・電極、3・・・電源装置、4
・・・浸透膜、5・・・混和槽、6・・・汚泥、7・・
・凝集剤、8・・・添加剤。
FIG. 1 is a flowchart showing one embodiment of the method of the present invention. 1... Dehydrator, 2... Electrode, 3... Power supply device, 4
... Permeation membrane, 5... Mixing tank, 6... Sludge, 7...
・Flocculant, 8...Additive.

Claims (2)

【特許請求の範囲】[Claims] (1)  電気浸透法による脱水方法において、被脱水
物に予じめ水利力の強い添加剤を加えることを特徴とす
る脱水方法。
(1) A dehydration method using electroosmosis, characterized in that an additive with strong water utilization is added to the material to be dehydrated in advance.
(2)  電気浸透法による脱水方法において、被脱水
物に予じめ水利力の強い添加剤を加え、脱水処理後分離
水に含まれている前記添加剤を逆浸透圧を利用した膜を
使って回収し再利用することを特徴とする脱水方法。
(2) In a dehydration method using electroosmosis, an additive with strong water utilization is added to the material to be dehydrated in advance, and after the dehydration treatment, the additive contained in the separated water is removed using a membrane using reverse osmosis pressure. A dehydration method characterized by recovering and reusing waste water.
JP57003613A 1982-01-13 1982-01-13 Dehydrating method Pending JPS58122085A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP57003613A JPS58122085A (en) 1982-01-13 1982-01-13 Dehydrating method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP57003613A JPS58122085A (en) 1982-01-13 1982-01-13 Dehydrating method

Publications (1)

Publication Number Publication Date
JPS58122085A true JPS58122085A (en) 1983-07-20

Family

ID=11562336

Family Applications (1)

Application Number Title Priority Date Filing Date
JP57003613A Pending JPS58122085A (en) 1982-01-13 1982-01-13 Dehydrating method

Country Status (1)

Country Link
JP (1) JPS58122085A (en)

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS61216799A (en) * 1985-03-22 1986-09-26 Ishigaki Kiko Kk Filtering dehydration of purified sludge
EP0520698A2 (en) * 1991-06-26 1992-12-30 Shinko Pantec Co., Ltd. Method of electroosmotically dehydrating sludge
WO1996011051A3 (en) * 1994-10-06 1996-06-20 Scapa Group Plc Dewatering process
WO2010113846A1 (en) * 2009-03-30 2010-10-07 栗田工業株式会社 Method for dewatering sludge and method and device for electroosmotic dewatering
JP2010234188A (en) * 2009-03-30 2010-10-21 Kurita Water Ind Ltd Sludge dewatering method
CN102603151A (en) * 2012-02-21 2012-07-25 天津生态城环保有限公司 Method for sludge dewatering by reinforcement Geotech-bag
CN105152515A (en) * 2015-10-14 2015-12-16 无锡百灵传感技术有限公司 Sludge dehydration equipment based on vacuum electroosmosis

Cited By (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS61216799A (en) * 1985-03-22 1986-09-26 Ishigaki Kiko Kk Filtering dehydration of purified sludge
EP0520698A2 (en) * 1991-06-26 1992-12-30 Shinko Pantec Co., Ltd. Method of electroosmotically dehydrating sludge
JPH054100A (en) * 1991-06-26 1993-01-14 Shinko Pantec Co Ltd Electroosmosis dehydrating method for sludge
US5279718A (en) * 1991-06-26 1994-01-18 Shinko Pantec Co., Ltd. Method of electroosmotically dehydrating sludge
WO1996011051A3 (en) * 1994-10-06 1996-06-20 Scapa Group Plc Dewatering process
WO2010113846A1 (en) * 2009-03-30 2010-10-07 栗田工業株式会社 Method for dewatering sludge and method and device for electroosmotic dewatering
JP2010234188A (en) * 2009-03-30 2010-10-21 Kurita Water Ind Ltd Sludge dewatering method
CN102361829A (en) * 2009-03-30 2012-02-22 栗田工业株式会社 Method for dewatering sludge and method and device for electroosmotic dewatering
CN102603151A (en) * 2012-02-21 2012-07-25 天津生态城环保有限公司 Method for sludge dewatering by reinforcement Geotech-bag
CN105152515A (en) * 2015-10-14 2015-12-16 无锡百灵传感技术有限公司 Sludge dehydration equipment based on vacuum electroosmosis

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