JPS58122085A - Dehydrating method - Google Patents
Dehydrating methodInfo
- 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
Links
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D61/00—Processes of separation using semi-permeable membranes, e.g. dialysis, osmosis or ultrafiltration; Apparatus, accessories or auxiliary operations specially adapted therefor
- B01D61/42—Electrodialysis; Electro-osmosis ; Electro-ultrafiltration; Membrane capacitive deionization
- B01D61/56—Electro-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
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.
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)
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.
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.
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)
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 |
-
1982
- 1982-01-13 JP JP57003613A patent/JPS58122085A/en active Pending
Cited By (10)
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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