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WO2002036239A1 - Filter sand washing method and its system - Google Patents

Filter sand washing method and its system Download PDF

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Publication number
WO2002036239A1
WO2002036239A1 PCT/JP2000/007764 JP0007764W WO0236239A1 WO 2002036239 A1 WO2002036239 A1 WO 2002036239A1 JP 0007764 W JP0007764 W JP 0007764W WO 0236239 A1 WO0236239 A1 WO 0236239A1
Authority
WO
WIPO (PCT)
Prior art keywords
sand
washing
filter
filtered
rapid filtration
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.)
Ceased
Application number
PCT/JP2000/007764
Other languages
French (fr)
Japanese (ja)
Inventor
Yasuhiro Saito
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.)
Nihon Genryo Co Ltd
Original Assignee
Nihon Genryo 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 Nihon Genryo Co Ltd filed Critical Nihon Genryo Co Ltd
Priority to CNB00820117XA priority Critical patent/CN1270803C/en
Priority to PCT/JP2000/007764 priority patent/WO2002036239A1/en
Priority to KR1020037006174A priority patent/KR100543150B1/en
Priority to JP2001138429A priority patent/JP3807542B2/en
Publication of WO2002036239A1 publication Critical patent/WO2002036239A1/en
Anticipated expiration legal-status Critical
Priority to US11/600,786 priority patent/US20070113870A1/en
Priority to US12/401,360 priority patent/US20090166277A1/en
Ceased legal-status Critical Current

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Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D24/00Filters comprising loose filtering material, i.e. filtering material without any binder between the individual particles or fibres thereof
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D41/00Regeneration of the filtering material or filter elements outside the filter for liquid or gaseous fluids
    • B01D41/02Regeneration of the filtering material or filter elements outside the filter for liquid or gaseous fluids of loose filtering material

Definitions

  • the present invention relates to a method and a system for cleaning filter sand in a filtration pond for purifying water, and more particularly, to a cleaning method and a system for removing a part of the filter sand in a rapid filtration pond for cleaning.
  • Non-land which is a phenomenon that the gravel layer that should have been partially thickening or thinning, occurs.
  • the sand layer becomes thinner in the thicker part of the gravel layer, and the filtration becomes insufficient in that part, and the filtration function that is originally performed is reduced, and the filter pond does not work properly and the water supply is safe. Can no longer be done.
  • new sand may be used for the filter sand that is laid again during rehabilitation work, but only about 10 to 20% of the collected sand is actually recognized as filter sand, and strict standards are imposed on filter materials. It is enacted, and if new sand is used, the cost will increase. Therefore, filtered sand is regenerated by washing.
  • the present inventors have already proposed a sand washing apparatus that can regenerate sand to a state close to fresh sand with a washing turbidity of 30 degrees or less by an innovative method called a kneading washing method (Japanese Patent Laid-Open No. -109051, JP-A-57526). With this device, it is possible to achieve the same purification function as a filtration pond using fresh sand without using fresh sand for the filtration sand that is laid on the filtration pond during rehabilitation work.
  • the maintenance of the filtration sand performed in the filtration basin includes the measurement of thornlessness and particle size survey. This is done to determine the timing of rehabilitation work.Maintenance to maintain the function of the sand that has regained its original purification function by rehabilitation work includes regular filtration by surface cleaning and backwashing. It is limited to the sand cleaning process only.
  • the water treatment plant should meet the above guidelines to maintain the turbidity at the outlet of the filtration pond below 0.1 degrees.
  • the frequency of washing and backwashing is increased, but during that time purification is not possible because the water cannot be purified and the amount of water that can be obtained is reduced.
  • the present invention has been made in view of the above circumstances, and the sand purifying function is regenerated by a method other than the usual cleaning method of surface cleaning and backflow cleaning without stopping the operation of the filtration pond, so that the filtration pond can be used. It is an object of the present invention to provide a method for cleaning filtered sand and a device for the same, which enable the cycle of rehabilitation work to be drastically extended.
  • the filter sand washing method of the present invention is characterized in that a predetermined amount of filter sand is sucked from the rapid filter pond during backflow washing of the rapid filter pond for purifying water with the filter sand, and the sucked filter sand is sent to a sand washing device. Feeding, removing dirt from the filter sand by the sand washing device, returning the filter sand from which the dirt has been removed to the rapid filtration tank at the time of backwashing of the rapid filtration tank, sucking, washing, and returning the filtered sand. The process is repeated to wash the filter sand in the rapid filtration tank.
  • the filter sand washing system of the present invention comprises: a rapid filter pond; a means for sucking filter sand from the quick filter pond; a sand washing device for washing the sucked filter sand; It is characterized by a means for returning the sand from which dirt has been removed to the pond.
  • the filter sand washing system may be one that continuously performs the steps of sucking, washing, and returning the filter sand, or may be one that performs a batch process.
  • ⁇ Suction of filtered sand '' is performed during backwashing of the rapid filtration pond because the filtered sand is in a state where water is filtered in a normal state. This is because there is a possibility that a portion having a small layer thickness is formed and turbidity leaks. Suction of the filtered sand can be performed even when the surface cleaning is performed simultaneously with the backwashing. Also, the ⁇ return of filtered sand '' is performed during backwashing of the rapid filtration pond. During backwashing, the purified water is pressed into the filtration pond from the lower pressure chamber and the sand is floating.
  • the filter sand can form a flat layer when the backwashing is completed.
  • the filtration sand can be returned even when backwashing and surface cleaning are performed at the same time as suction of filtration sand.
  • Predetermined amount means the amount of filtration that does not affect the purification of water in the filtration pond.
  • suction of filtered sand means that the surface of the gravel layer of the rapid filtration pond has unevenness. It is preferable that the suction be performed with a suction force of a size not to be formed.
  • the filter sand layer of the rapid filtration pond is about 60 cm, but if the filter sand is sucked with too strong suction force or if it is sucked near the boundary with the gravel layer, the gravel layer supporting the filter sand will It is preferable to absorb the filtered sand with a suction force that does not cause unevenness on the surface of the gravel layer because the sand becomes partially thin or thick.
  • the suction of the filter sand depends on the composition of the filter layer and the suction power of the suction, but is preferably 15 to 70%, more preferably 40 to 60% of the filter sand layer from the surface of the filter sand layer.
  • the filtered sand from which the dirt has been removed may be stored in a storage tank until returning to the rapid filtration pond, or the filtered sand from which the dirt has been removed may be stored in the storage tank. Without storing, the filtered sand from which the dirt has been removed may be returned before the backwashing at the time of the backwashing in which the filtered sand has been sucked is completed.
  • the steps of sucking, washing, and returning the filtered sand may be performed continuously during the backwashing.
  • a storage tank it is preferable to add water or water containing an oxidizing agent so that the stored filtered sand does not come into contact with air.
  • an oxidizing agent for example, chlorine is preferable.
  • the manganese layer of the filter sand which has the ability to remove manganese in raw water, is maintained by filling the storage tank with water or water containing an oxidizing agent so that the filter sand does not dry. can do.
  • the storage tank may be large enough to store at least one predetermined amount of filtered sand sucked from the filter pond in water so as not to come into contact with air.
  • the filter sand cleaning method and system of the present invention can also be applied to the filtration of filter sand from a plurality of quick filter ponds, which are connected to four to six quick filter ponds called green leaves. That is, in the method for washing filtered sand of the present invention, a predetermined amount of filtered sand is sucked from the rapid filtering pond at the time of backflow washing of the quick filtering pond for purifying water with the filtered sand, and the sucked filtered sand is sent to the sand washing device.
  • the method is characterized in that the filter sand is returned to the rapid filtration tank during backwashing of the rapid filtration tank, and the filtration sand in the plurality of rapid filtration ponds is washed by repeating the steps of sucking, washing, storing, and returning the filtered sand.
  • a filtration basin with heavy filtration sand there may be a filtration basin with heavy filtration sand and a filtration basin with relatively little filtration sand.
  • Filter sand that has been sucked from a filter pond that has very bad filter sand is returned to the filter pond that has relatively little filter sand, and filter sand that has been sucked from the filter pond that has relatively little filter sand is filtered. It is more preferable to return the filter to a filter tank with heavy dirt from the viewpoint of leveling the filter sand in a plurality of filters.
  • sequence control it is preferable that the repetition of each of these steps is automatically performed by sequence control.
  • backwashing of a rapid filtration pond can be controlled with pressure loss and time as factors, and the sequence control can be used to suck, wash, and return filtered sand, or to suck, wash, store, and return filtered sand.
  • a series of steps can be performed automatically.
  • the filter sand that has already been removed is not mixed with the filter sand that has been removed to increase the cleaning efficiency. . Therefore, it is preferable to return the filtered sand from which dirt has been removed to a position away from the position where the sand is sucked in the rapid filtration tank. That is, it is preferable that the means for sucking the filtered sand from the rapid filtration pond and the means for returning the filtered sand from which dirt has been removed are provided separately.
  • the position where the filter sand is sucked should be moved each time the filter sand is sucked, and the position where the filter sand after removing the dirt is returned should also be moved each time the filter sand is returned.
  • at least one of the means for sucking the filtered sand from the rapid filtration pond and the means for returning the soil-removed sand to the rapid filtration pond is movably provided.
  • the "sand cleaning device” includes a device as disclosed in Japanese Patent Application Laid-Open No. 10-109051, that is, a cleaning tank for storing cleaning water together with sand, and a screw rotating around a substantially vertical axis in the cleaning tank.
  • the screw conveyor is rotated by rotating the screw conveyor at a lower portion of the screw conveyor below the surface of the washing water to raise the sand and the washing water and interpose the washing water.
  • the dirt of the sand is removed by the contact of the sand, and the sand is flowed on the screw conveyor at the upper part of the screw conveyor on the surface of the washing water, so that the water containing the sludge is slightly contained.
  • filter sand cleaning which relied solely on surface cleaning and backwashing, has been replaced by a filter sand washing method according to the present invention.
  • the dirt from the filtered sand is removed by the sand washer, and the filtered sand from which the dirt has been removed is returned to the rapid filtration pond during backwashing, and the filtered sand is repeatedly sucked, washed and returned. Since the filter sand in the filter pond is to be cleaned, the filter sand can be washed effectively without stopping the operation of the filter pond, and the cycle of filter rehabilitation work can be drastically extended. .
  • the water purification function of the filtration tank can be regenerated. It becomes possible.
  • dirt from the filter sand is removed, it is possible to reduce the filtration resistance.Therefore, it is only necessary to carry out backwashing at the designed pressure.Therefore, it is possible to reduce the outflow of filter sand and the outflow of exfoliated sludge. Therefore, the period of rehabilitation works for filter ponds can be dramatically extended from this point.
  • a predetermined amount of filter sand is sucked from the rapid filtration pond, and the sucked filter sand is supplied to the sand washer, and the sand is removed by the sand washer, and the filtered sand is removed and stored.
  • the time is almost the same as the time required to wash all the filtered sand in a single filtration pond. This makes it possible to wash the filtered sand from multiple filtration ponds.
  • the filter sand sucked from the filter pond where the filter sand is very dirty is returned to the filter pond where the filter sand is relatively less contaminated, and the filter sand is collected from the filter pond where the filter sand is less contaminated. If the filtered sand is returned to the filter pond where the filter sand is very dirty, the filter sand in the filter pond can be leveled. '
  • the sand cleaning method of the present invention and the sand cleaning apparatus of the system together with the sand, A washing tank that stores washing water, a screw conveyor that rotates around a substantially vertical axis in the washing tank, and a screw conveyor that is disposed below the screw conveyor below the surface of the washing water.
  • the rotation of the U-conveyor raises the sand and the washing water, and removes dirt from the sand by contact between the sands with the washing water interposed therebetween.
  • FIG. 1 is a process diagram showing an embodiment of the filtered sand washing method of the present invention
  • FIG. 2 is a schematic diagram showing a first embodiment of the filtered sand washing system of the present invention
  • FIG. FIG. 4 is a schematic diagram showing a second embodiment of the filter sand washing system of the present invention
  • FIG. 4 is a process diagram showing another embodiment of the filter sand washing method of the present invention
  • FIG. 6 is a process diagram showing still another embodiment of the filter sand washing method
  • FIG. 6 is a sectional view taken along line A--A of the rapid filtration pond shown in FIG. 2
  • FIG. 8 is a diagram showing a flow of the filtration sand
  • FIG. 8 is a diagram showing an example of the movement of the filtration sand between the filtration ponds.
  • the filter sand washing system of the present invention cleans the filter sand with dirt adhering from the rapid filtration pond 1, the rapid filtration pond 1, and the filter sand 5 with dirt adhering thereto.
  • Stock the sand washer 3 and the filtered sand 6 washed by the sand washer 3. It is provided with a washing sand stock tank 4 to be stored, and a path 7 for returning dirt-removed sand from the washing sand stock tank 4 to the rapid filtration pond 1. (Details of the processing steps of this filter sand washing system will be described later with reference to examples.)
  • the filter sand washing system of the present invention cleans a quick filter pond 1, a pump 2 for sucking filter sand with dirt from the quick filter pond 1, and a filter sand 5 with dirt. It may be provided with a sand washing device 3 to be cleaned and a path 7 for returning the sand from which dirt has been removed from the sand washing device 3 to the rapid filtration pond 1, that is, a device without a washing sand stock tank.
  • a filtration sand washing system without a washing sand stock tank it is possible to save the cost of the washing stock tank, and also to install a washing sand stock tank around the rapid filtration pond. This is a more preferable mode when there is no room.
  • the surface cleaning and backwashing of the filtration pond 1 are performed within the time (eg, 15 to 25 minutes).
  • the 1 m 3 of contaminated filtration sand by suction from the filtration reservoir 1 by the pump 2 sends the filtration sand sucked by the pump 2 to the sand washing device 3, washing in a short time, the sand washing device 3 (about 10 minutes)
  • the filtered sand (clean sand) after the washing can be returned to the filtration pond 1.
  • the suction of the sand and the return of the clean sand during the time when one surface cleaning and backwashing are being performed, it becomes possible to wash the sand in a short time.
  • contaminated filtered sand is continuously pumped from filter pond 1 using pump 2.
  • the filtered sand sucked by the pump 2 is continuously sent to the sand washing device 3 and continuously washed by the sand washing device 3, and the purified sand is filtered before the surface washing and backwashing of the filtration pond 1 are completed.
  • the treatment can also be performed by a process of continuously returning to pond 1. If the treatment is performed continuously during the time during which the surface cleaning and the backwashing are performed, it is possible to wash a larger amount of soil in a short time.
  • the rapid filtration pond 1 has a filtration sand layer 12 as a filtration layer, and 13 to 16 gravel layers supporting the filtration sand layer 12.
  • the filter sand layer 12 is made of sand having an effective diameter of 0.6 mm and a uniformity coefficient of 1.5 or less.
  • the gravel layer consists of four layers with different particle sizes, and the filter sand is used as a support layer. Is prevented from entering the water collection device (not shown, but the device for collecting the purified water is provided further below the rapid filtration pond 1).
  • the gravel layers 13 to 16 are selected to be nearly spherical, hard, clean, and homogeneous in order to perform backwashing evenly.
  • the effective diameter is 2.0 to 3.511111, the gravel layer 14 is 3.5 to 7.0 difficult, the gravel layer 15 is 7.0 to 13.Omm, and the gravel layer 16 is 13.0 to 20.Omm. Coarse grains are spread in the lower layer so that there is no irregularity.
  • water that has been pretreated by flocculating and precipitating the turbidity of the raw water with a flocculant is introduced.
  • An exhaust trough 21 is provided.
  • the filtration for water purification is stopped, and washing water is injected from the lower pressure chamber of the rapid filtration pond to lift the filter sand, and the sand is removed. Washing is performed by mixing with sand.
  • the surface washing is performed by spraying washing water from the front washing tube 22 onto the surface of the filter sand 12 at the time of backwashing or at a certain time during the backwash cycle. Washing drainage 11 after surface washing and backwashing is discharged from trough 21. When the washing is completed, the pretreated raw water is sent again and the filtration is resumed.
  • the process of water purification and washing is usually automated, and the timing of surface washing and backwashing is set in advance depending on the condition of the raw water at the water treatment plant where the water is treated by the rapid filtration method, or the head loss is fixed. It is set so that surface cleaning and backwashing are automatically performed when the above occurs.
  • the selection standard for filtered sand JWWA A 103-1988 is that the washing turbidity is 30 degrees or less, the hydrochloric acid solubility is 3.5% or less, the effective diameter is 0.45 to 0.70, and the uniformity coefficient is 1.7 It is stipulated below. Regularly perform general surface cleaning and backwashing as described above. Even after renovation every 10 years, the turbidity of washing was 1480 degrees, the solubility of hydrochloric acid was 9.7%, and the effective diameter was 0.533. With an equality coefficient of 1.485, turbidity adheres to the filtered sand and becomes considerably dirty.
  • the following is an example of a filter sand washing system in which a part of the filter sand is washed with a sand washing device, and the soil-removed sand is returned to the filter tank again, in addition to the normal washing process described above. .
  • the sand washing device 3 includes a washing tank disclosed in Japanese Patent Application Laid-Open No. 10-109051 for storing washing water together with sand, a screw conveyor rotating around a substantially vertical axis in the washing tank, and a screw conveyor. At the lower part of the screw conveyor below the surface of the washing water, the sand and the washing water are raised by the rotation of the screw conveyor, and the sand is contacted by the sand with the washing water interposed therebetween. The dirt is removed, and the sand is flowed on the screw conveyor at the upper part of the screw conveyor on the surface of the washing water, and the sand containing the sludge-containing water is slightly contacted with the sand.
  • a device capable of realizing a kneading-washing method comprising circulating means for lowering the raised sand to the lower portion of the screw conveyor and again raising the sand on the screw conveyor.
  • lm 3 of dirty filter sand is removed at the corner of filter basin 1.
  • (La) was pumped by pump 2.
  • the suction of the filtered sand was performed at a depth of about 10 cm from the upper part of the gravel layer 13 (the thickness of the filtered sand layer was 60 cm).
  • the filtered sand (5) sucked by the pump 2 was sent to the sand washing device 3 and washed by the sand washing device 3 for about 1 hour.
  • the washing turbidity of the suctioned filter sand (5) was reduced from 1480 ° C to 11 ° C, the hydrochloric acid solubility was changed from 9.7% to 2.8%, and the coefficient of uniformity was increased by washing for about 1 hour. From 1.485, it can be seen that washing is performed to the same level as that of fresh sand.
  • the filtered sand (6a) after washing was stored in a washing sand stock tank filled with water. Approximately 48 hours after the filtration performed in the rapid filtration tank 1, the filtration was stopped, and surface cleaning and backwashing were started again. At this time, the corner (lb) opposite to the corner (la) ) was returned to the filtration pond 1. By repeating this cycle, almost all the sand of 60 m 3 in the filter pond 1 was washed in about 120 days.
  • Example 1 Filtered sand cleaning was performed in the same manner as in Example 1 except that the specific sand cleaning device used in Example 1 was changed to a conventional sand cleaning device using a jet stream. As shown in Table 4, there was a slight significant difference compared to the one using the specific sand washing device of Example 1, but the sand was remarkably washed. However, in the case of Example 1, there was almost no change in the particle size of the sand, but the effective diameter was reduced and the uniformity coefficient was increased after long-time cleaning. With conventional sand washing equipment using jet water, sand is washed during washing. It can be seen that the sand crushed due to collision with the pipe wall or the like.
  • FIG. 7 is a diagram showing the flow of the filter sand corresponding to a plurality of filter ponds
  • FIG. 8 is a diagram showing an example of the movement of the filter sand between the filter ponds.
  • a filter sand system combining six quick filter ponds A to F as shown in Fig. 7 and one sand washing device and one storage tank is described. The principle is exactly the same whether the number is larger or smaller.
  • Filtration ponds AF are filtration ponds where backwashing is performed every 48 hours. As shown in Fig. 7, the interval between backwashing of each filtration pond is 8 hours.
  • a predetermined amount of filter sand is sucked from filter pond A.
  • the sucked filter sand is washed for 1 hour with a sand washing device.
  • the filtered sand from which the dirt has been removed is stored in a storage tank filled with water or water containing an oxidizing agent.
  • the stored filter sand after washing is returned to Filter Pond B where backwashing starts after 8 hours from backwashing of Filter Pond A.
  • washed filter sand is returned and dirty filter sand is absorbed.
  • the filtered sand sucked in the filtration basin B is washed for 1 hour with a sand washing device, and the washed filtered sand is stored in a storage tank filled with water or water containing an oxidizing agent.
  • the stored filter sand after washing is returned to Filter Pond C where backwashing starts after 8 hours from backwashing of Filter Pond B.
  • the washed filter sand is returned and dirty filter sand is absorbed. In this way, after 48 hours, a predetermined amount of the filter sand is absorbed in all of the filter ponds A to F, and a predetermined amount of the filter sand after the washing is released. .
  • This process can be repeated to wash all the filtered sand in the filtration ponds AF.
  • multiple filtration ponds By matching the timing of backwashing, it is possible to wash the filter sand in multiple filtration ponds in a time that is almost the same as the time required to wash the filtration sand in a single filtration pond.
  • filter sand after washing of filter A is filtered to filter E as shown in Fig. 8, and then filtered.
  • Filter sand after washing of Pond E was returned to Filter Pond C, filtered sand after washing of Filter Pond C to Filter Pond D, and filtered sand after washing of Filter Pond D to Filter Pond A.
  • ⁇ F can be leveled.
  • a step of sucking filter sand from the rapid filtration pond a step of washing the filter sand with a sand washing device, and a step of returning the filtered sand from which dirt has been removed to the rapid filter pond, or filtering from the rapid filter pond.
  • Sequence control automatically performs four steps: sucking sand, washing the filtered sand with a sand washing device, storing the washed filtered sand in a storage tank, and returning the filtered sand from which dirt has been removed to the rapid filtration pond.

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  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Filtration Of Liquid (AREA)
  • Separation Of Solids By Using Liquids Or Pneumatic Power (AREA)

Abstract

When backwashing a rapid filter (1) where water is washed with filter sand, a preset amount of filter sand (5) is sucked from the rapid filter (1) by a pump (2). The sucked filter sand (5) is fed to a sand washing device (3) where the contaminants on the filter sand are removed. Contaminants-removed filter sand (6) is kept in a washed-sand stock tank (4), and stored filter sand (7) is returned to the rapid filter (1) when the rapid filter is backwashed. An automatic washing of filter sand in the rapid filter is possible by repeating the steps of sucking, washing and returning filter sand, whereby a sand washing function is regenerated by a washing method other than surface washing and backwashing to thereby drastically prolong a regenerating cycle of a filter pond.

Description

明 細 書 濾過石少洗、净方、法とそのシステム 技術分里予  Memorandum Book Filtering stone washing, method, law and its system

本発明は、水の浄化を行う濾過池の濾過砂を洗浄する方法及びシステムに関し、 詳しくは急速濾過池の濾過砂の一部を取り出して洗浄を行う洗浄方法及びシステ ムに関するものである。  The present invention relates to a method and a system for cleaning filter sand in a filtration pond for purifying water, and more particularly, to a cleaning method and a system for removing a part of the filter sand in a rapid filtration pond for cleaning.

背景技術 Background art

浄水場における浄水処理は、 河川、 湖沼から引き込んだ原水に薬品を注入して 原水中の浮遊物を沈殿しやすい大きさの塊にして沈殿させ、 上澄みを濾過池に送 り、 ここでさらに微細な浮遊物を砂 (濾過砂) の層を通して取り除き、 濾過した 水を塩素で消毒することにより行われている。 急速濾過池では、 一般に 24~72時 間おきに定期的に濾過材の洗浄が行われる。 洗浄には、 ノズルから噴射される砂 層表面を叩くように洗浄する表面洗浄と、 下部圧力室から浄水を濾過池内に圧入 して砂を浮上させ、 砂と砂とをもみ合わせて汚れを落とす逆流洗诤がある。  In water treatment at a water treatment plant, chemicals are injected into raw water drawn from rivers and lakes to precipitate suspended solids in the raw water into chunks that are easy to sediment, and the supernatant is sent to a filtration pond, where it is further refined. This is done by removing unusual suspended matter through a layer of sand (filtered sand) and disinfecting the filtered water with chlorine. In rapid filtration basins, filtration media is generally cleaned regularly every 24 to 72 hours. For cleaning, the surface of the sand layer sprayed from the nozzle is washed by tapping, and the clean water is pressed into the filter pond from the lower pressure chamber to float the sand, and the sand is mixed with the sand to remove dirt. There is backwashing.

この浄水処理に使用される濾過砂は、 このような表面洗浄、 逆流洗浄を定期的 に行っていても、 長年繰り返し使用していると表面に汚れ (汚泥等の濁質) が付 着してくる。 濁質の付着により濾過砂の粒径肥大が進むと、 濾過砂間の空隙が減 少したり、 濾過砂の吸着物質の剥離による目詰まり現象や汚泥そのものの剥離に よるリークなどが起きるようになる。 逆流洗浄の回数を増やすなどしてこれに対 応しているが、 逆流洗浄を長年繰り返しているとその水圧により濾過砂を支持し ている砂利層にも影響が出て、 本来水平に敷き詰められているはずの砂利層が部 分的に厚くなつたり薄くなつたりしてしまう現象である不陸が生じたりする。 こ の不陸ができると砂利層の厚い部分では砂層が薄くなり、 その部分では濾過が不 十分になり、 本来発揮される濾過機能が低下して濾過池が正常に働かず安全な水 の供給ができなくなってくる。  Even if the filter sand used for this water purification process is used for such surface cleaning and backwashing regularly, if it is used repeatedly for many years, dirt (turbidity such as sludge) adheres to the surface. come. As the particle size of the filter sand increases due to the adhesion of turbidity, voids between the filter sands decrease, clogging due to separation of the adsorbed substance of the filter sand, and leakage due to separation of the sludge itself will occur. . This has been addressed by increasing the number of backwashing steps, but if backwashing is repeated for many years, the water pressure will also affect the gravel layer that supports the filtered sand, and it will be spread horizontally. Non-land, which is a phenomenon that the gravel layer that should have been partially thickening or thinning, occurs. When this unevenness occurs, the sand layer becomes thinner in the thicker part of the gravel layer, and the filtration becomes insufficient in that part, and the filtration function that is originally performed is reduced, and the filter pond does not work properly and the water supply is safe. Can no longer be done.

正常な濾過機能を復帰させるためには、 濾過池の運転を一端停止して濾過材を 搬出し、 搬出した濾過材を洗浄,篩い分けし、 濾過池内部を点検修理した後、 洗 浄した濾過材を再び濾過池へ敷き直すという更生工事を行う必要がある。 しかし この更生工事には莫大なコストを要し、 また工事の期間は濾過池の運転を停止す る必要があり、更生工事にかかる期間はそのまま浄水効率の低下につながるため、 更生工事の周期はなるべく長くしたいという浄水場側の要望がある。 In order to restore the normal filtration function, the operation of the filter pond is stopped once, the filter medium is removed, the removed filter medium is washed and sieved, and the inside of the filter pond is inspected and repaired. It is necessary to carry out rehabilitation work to re-install the cleaned filter media in the filtration pond. However, this rehabilitation work requires enormous costs, and it is necessary to stop the operation of the filtration pond during the construction period.The period of the rehabilitation work directly lowers the water purification efficiency. There is a request from the water treatment plant to make it as long as possible.

一方、 更生工事で敷き直す濾過砂には、 新しい砂が用いられる場合もあるが、 採取した砂のうち濾過砂として現実に認められるのはわずか 1〜 2割程度と濾過 材には厳しい基準が制定されており、 また新しい砂を使用する場合にはコストの 増大にもつながるため、 濾過砂は洗浄などによって再生されている。 本発明者ら はすでに、 揉み洗い工法という画期的な方法で、 洗浄濁度 30度以下という新砂に 近い状態にまで砂の再生を可能とする砂洗浄装置を提案している (特開平 10- 109051号,特開平 Π-57526号)。 この装置により、 更生工事の際に濾過池へ敷き直 す濾過砂に新砂を用いなくても、 新砂を用いた濾過池と同様の浄ィ匕機能を実現す ることが可能となっている。  On the other hand, new sand may be used for the filter sand that is laid again during rehabilitation work, but only about 10 to 20% of the collected sand is actually recognized as filter sand, and strict standards are imposed on filter materials. It is enacted, and if new sand is used, the cost will increase. Therefore, filtered sand is regenerated by washing. The present inventors have already proposed a sand washing apparatus that can regenerate sand to a state close to fresh sand with a washing turbidity of 30 degrees or less by an innovative method called a kneading washing method (Japanese Patent Laid-Open No. -109051, JP-A-57526). With this device, it is possible to achieve the same purification function as a filtration pond using fresh sand without using fresh sand for the filtration sand that is laid on the filtration pond during rehabilitation work.

しかし、 近年の都市排水、 工業排水、 農業排水等による河川、 湖、 海の水質汚 染、 あるいは大気汚染物質の窒素酸化物や硫黄酸化物が溶け込んで降る酸性雨等 により水道用原水は急速に悪化している。 このような原水の悪化により、 濾過砂 の状態は表 1に示すように汚濁が進み、 かっては通常の運転において 7〜:0年の 長期間にわたり使用可能であった濾過池も、 更生工事のペースを早めなければな らなくなっている。  However, raw water for water supply has been rapidly increasing due to the recent pollution of rivers, lakes, and oceans due to urban, industrial, and agricultural wastewater, and acid rain that has been caused by the dissolution of nitrogen oxides and sulfur oxides as air pollutants. Is getting worse. Due to such deterioration of raw water, the condition of the filter sand is becoming more polluted as shown in Table 1, and filter ponds that were able to be used for a long period of time of 7 to 0 years in normal operation, The pace has to be accelerated.

【表 1】  【table 1】

Figure imgf000004_0001
Figure imgf000004_0001

-方、 濾過池で行われる濾過砂のメンテナンスはもつばら不陸測定や粒径調査な どの更生工事の時期を判断するために行われるものであり、 更生工事によって本 来の浄ィ匕機能を取り戻した砂の機能を維持するためのメンテナンスは、表面洗浄、 逆流洗浄による定期的な濾過砂の洗浄工程のみに限られている。 On the other hand, the maintenance of the filtration sand performed in the filtration basin includes the measurement of thornlessness and particle size survey. This is done to determine the timing of rehabilitation work.Maintenance to maintain the function of the sand that has regained its original purification function by rehabilitation work includes regular filtration by surface cleaning and backwashing. It is limited to the sand cleaning process only.

また、 1996年に制定されたクリプトスポリジゥム暫定対策を受けて濾過池出口 の濁度を 0. 1 度以下に維持するという厚生省の指針に対応するため、 浄水場では 上記のような表面洗浄、 逆流洗浄の頻度を上げて対応しているが、 その間は浄水 ができず取得できる水量は減るため浄化効率は悪くなつている。 また洗浄のたび に細砂が流出し、 さらに逆流洗浄の頻度が増えると不陸の形成を早めることにも なり、 結果として更生工事の時期を早める結果となる場合もあり、 従来の表面洗 浄、 逆流洗浄という洗浄工程のみで対応するには限界があると考えられる。  In addition, following the provisional measures against cryptosporidium enacted in 1996, the water treatment plant should meet the above guidelines to maintain the turbidity at the outlet of the filtration pond below 0.1 degrees. The frequency of washing and backwashing is increased, but during that time purification is not possible because the water cannot be purified and the amount of water that can be obtained is reduced. In addition, fine sand flows out each time washing is performed, and if the frequency of backwashing increases, the formation of unevenness will be accelerated, which may result in earlier rehabilitation work. However, it is considered that there is a limit in responding only by the washing process of backwashing.

本発明は上記事情に鑑みなされたものであり、 濾過池の運転を休止することな く、 砂の浄化機能を表面洗浄、 逆流洗浄という通常の洗浄方法以外の方法で再生 させて、 濾過池の更生工事の周期を飛躍的に延長することを可能とする濾過砂洗 浄方法及びそのための装置を提供することを目的とするものである。  The present invention has been made in view of the above circumstances, and the sand purifying function is regenerated by a method other than the usual cleaning method of surface cleaning and backflow cleaning without stopping the operation of the filtration pond, so that the filtration pond can be used. It is an object of the present invention to provide a method for cleaning filtered sand and a device for the same, which enable the cycle of rehabilitation work to be drastically extended.

発明の開示 Disclosure of the invention

本発明の濾過砂洗浄方法は、 濾過砂により水の浄化を行う急速濾過池の逆流洗 浄時に該急速濾過池から所定量の濾過砂を吸い取り、 該吸い取つた濾過砂を砂洗 浄装置に供給し、 該砂洗浄装置によって前記濾過砂の汚れを除去し、 汚れを除去 した前記濾過砂を前記急速濾過池の逆流洗浄時に該急速濾過池に戻し、 前記濾過 砂の吸い取り、 洗浄、 戻しの工程を繰り返して前記急速濾過池内の濾過砂を洗浄 することを特徴とするものである。  The filter sand washing method of the present invention is characterized in that a predetermined amount of filter sand is sucked from the rapid filter pond during backflow washing of the rapid filter pond for purifying water with the filter sand, and the sucked filter sand is sent to a sand washing device. Feeding, removing dirt from the filter sand by the sand washing device, returning the filter sand from which the dirt has been removed to the rapid filtration tank at the time of backwashing of the rapid filtration tank, sucking, washing, and returning the filtered sand. The process is repeated to wash the filter sand in the rapid filtration tank.

また、 本発明の濾過砂洗浄システムは、 急速濾過池と、 該急速濾過池から濾過 砂を吸い取る手段と、 吸い取った該濾過砂を洗浄する砂洗浄装置と、 該砂洗浄装 置から前記急速濾過池へ汚れを除去した砂を戻す手段とからなることを特徴とす るものである。 該濾過砂洗浄システムは濾過砂の吸取り、 洗浄、 戻しの工程を連 続処理するものであってもよいし、 バッチ処理により行うものであってもよい。  Further, the filter sand washing system of the present invention comprises: a rapid filter pond; a means for sucking filter sand from the quick filter pond; a sand washing device for washing the sucked filter sand; It is characterized by a means for returning the sand from which dirt has been removed to the pond. The filter sand washing system may be one that continuously performs the steps of sucking, washing, and returning the filter sand, or may be one that performs a batch process.

「濾過砂の吸取り」 を急速濾過池の逆流洗浄時に行うのは、 濾過砂は通常の状 態では水を濾過している状態であり、 この状態で濾過砂の吸取りを行うと濾過砂 の層に層厚の薄い部分ができてしまい濁質がリークする可能性があるためである。 濾過砂の吸取りは逆流洗浄と同時に表面洗浄が行われている時であっても差し支 えない。 また、 「濾過砂の戻し」 も急速濾過池の逆流洗浄時に行うのは、 逆流洗 浄時は、 下部圧力室から浄水を濾過池内に圧入して砂が浮上している状態である ので、 この状態で濾過砂を戻せば、 逆流洗浄が終わったときには濾過砂が平らな 層を形成することができるからである。 なお、 濾過砂の戻しも、 濾過砂の吸取り と同様に逆流洗浄と同時に表面洗浄が行われている時であっても差し支えない。 「所定量」 とは、 濾過池の水の浄化に影響を与えない程度の濾過 ¾>の量を意味す また、 「濾過砂の吸取り」 は、 急速濾過池の砂利層の表面に不陸を形成しない 大きさの吸引力で行わせることが好ましい。 急速濾過池の濾過砂層は 60cm前後で あるが、 あまりに強い吸引力で濾過砂を吸い取ったり、 あるいは砂利層との境界 近くで濾過砂を吸い取る場合には、 濾過砂を支持している砂利層が部分的に薄く なったり厚くなつたりするので、 砂利層の表面に不陸を形成しない程度の吸引力 で濾過砂を吸い取ることが好ましい。 濾過砂の吸取りは、 濾過層構成やその吸取 りの吸引力にもよるが濾過砂層の表面から濾過砂の層の 15 ~70 %の深さ、 さらに は 40〜60 %の深さが好ましい。また、不陸防止ネットが使用されている場合には、 100 %の深さ、 すなわち砂利層のすぐ上からの吸引であっても差し支えない。 砂洗浄装置によって濾過砂の汚れを除去した後、 汚れを除去した濾過砂は急速 濾過池に戻すまでの間、 貯留槽に貯留してもよいし、 汚れを除去した濾過砂を貯 留槽に貯留することなく、 汚れを除去した前記濾過砂を、 該濾過砂を吸い取った 前記逆流洗浄時における逆流洗浄が終了する前に戻してもよい。 貯留槽を設けな い場合には、 前記濾過砂の吸取り、 洗浄、 戻しの工程を前記逆流洗浄時に連続し て行ってもよい。 `` Suction of filtered sand '' is performed during backwashing of the rapid filtration pond because the filtered sand is in a state where water is filtered in a normal state. This is because there is a possibility that a portion having a small layer thickness is formed and turbidity leaks. Suction of the filtered sand can be performed even when the surface cleaning is performed simultaneously with the backwashing. Also, the `` return of filtered sand '' is performed during backwashing of the rapid filtration pond. During backwashing, the purified water is pressed into the filtration pond from the lower pressure chamber and the sand is floating. If the filter sand is returned in this state, the filter sand can form a flat layer when the backwashing is completed. The filtration sand can be returned even when backwashing and surface cleaning are performed at the same time as suction of filtration sand. "Predetermined amount" means the amount of filtration that does not affect the purification of water in the filtration pond. "Suction of filtered sand" means that the surface of the gravel layer of the rapid filtration pond has unevenness. It is preferable that the suction be performed with a suction force of a size not to be formed. The filter sand layer of the rapid filtration pond is about 60 cm, but if the filter sand is sucked with too strong suction force or if it is sucked near the boundary with the gravel layer, the gravel layer supporting the filter sand will It is preferable to absorb the filtered sand with a suction force that does not cause unevenness on the surface of the gravel layer because the sand becomes partially thin or thick. The suction of the filter sand depends on the composition of the filter layer and the suction power of the suction, but is preferably 15 to 70%, more preferably 40 to 60% of the filter sand layer from the surface of the filter sand layer. If a non-landing net is used, it can be suctioned from 100% depth, that is, just above the gravel layer. After removing the dirt from the filtered sand by the sand washing device, the filtered sand from which the dirt has been removed may be stored in a storage tank until returning to the rapid filtration pond, or the filtered sand from which the dirt has been removed may be stored in the storage tank. Without storing, the filtered sand from which the dirt has been removed may be returned before the backwashing at the time of the backwashing in which the filtered sand has been sucked is completed. When a storage tank is not provided, the steps of sucking, washing, and returning the filtered sand may be performed continuously during the backwashing.

貯留槽を設ける場合には、 貯留された濾過砂が空気と触れないように水あるい は酸化剤を含んだ水を入れておくことが好ましい。 酸化剤としては、 たとえば塩 素などが好ましい。 砂洗浄装置から洗浄後の濾過砂を貯留槽に移すことにより、 空いた 洗浄装置を、 他の急速濾過池の砂洗浄に使うことが可能となる。 またそ の貯留槽に濾過砂が乾燥しないように水あるいは酸化剤を含んだ水を張っておく ことにより、 原水のマンガン除去能力を有する濾過砂のマンガン層の活性を維持 することができる。 貯留槽の大きさは、 少なくとも濾過池から吸い取った 1回分 の所定量の濾過砂を空気に触れないように水に入れて貯留できる大きさであれば よい。 When a storage tank is provided, it is preferable to add water or water containing an oxidizing agent so that the stored filtered sand does not come into contact with air. As the oxidizing agent, for example, chlorine is preferable. By transferring the filtered sand after washing from the sand washing device to the storage tank, it becomes possible to use the empty washing device for sand washing of other rapid filtration ponds. The manganese layer of the filter sand, which has the ability to remove manganese in raw water, is maintained by filling the storage tank with water or water containing an oxidizing agent so that the filter sand does not dry. can do. The storage tank may be large enough to store at least one predetermined amount of filtered sand sucked from the filter pond in water so as not to come into contact with air.

本発明の濾過砂洗浄方法およびシステムは、 グリーンリーフと呼ばれる 4〜 6 の急速濾過池がつながつているような複数の急速濾過池の濾過砂の洗浄にも適用 することができる。 すなわち、 本発明の濾過砂洗浄方法は濾過砂により水の浄ィ匕 を行う急速濾過池の逆流洗浄時に該急速濾過池から所定量の濾過砂を吸い取り、 該吸い取った濾過砂を砂洗浄装置に供給し、 該砂洗浄装置によつて前記濾過砂の 汚れを除去し、 該汚れを除去した濾過砂を貯留槽に貯留し、 該貯留しておいた濾 過砂を前記急速濾過池とは異なる急速濾過池の逆流洗浄時に該急速濾過池に戻し、 前記濾過砂の吸取り、 洗浄、 貯留、 戻しの工程を繰り返して複数の急速濾過池内 の濾過砂を洗浄することを特徴とするものである。  The filter sand cleaning method and system of the present invention can also be applied to the filtration of filter sand from a plurality of quick filter ponds, which are connected to four to six quick filter ponds called green leaves. That is, in the method for washing filtered sand of the present invention, a predetermined amount of filtered sand is sucked from the rapid filtering pond at the time of backflow washing of the quick filtering pond for purifying water with the filtered sand, and the sucked filtered sand is sent to the sand washing device. Feeding, removing dirt from the filtered sand by the sand washing device, storing the filtered sand from which the dirt has been removed in a storage tank, and separating the stored filtered sand from the rapid filtration pond. The method is characterized in that the filter sand is returned to the rapid filtration tank during backwashing of the rapid filtration tank, and the filtration sand in the plurality of rapid filtration ponds is washed by repeating the steps of sucking, washing, storing, and returning the filtered sand.

貯留しておいた濾過砂を濾過砂を吸い取った濾過池とは異なる濾過池に戻すこ ととしたのは、 同じ濾過池に戻すと、 その濾過池の次の逆流洗浄時まで洗浄した 濾過砂を戻すことができないため、 実質的には濾過池を 1つずつ濾過砂洗浄する のと同じだけの時間が必要となるからである。 貯留槽を複数設ければ同じ濾過池 に戻しても単一の濾過池の濾過砂を洗浄するのと時間的には差がないが、 この場 合にはかなりの設備費用と土地が必要となり経済的ではない。 また、 かなり大き な貯留槽を設ければ、 複数の濾過池から吸い取り洗浄した濾過砂を貯留すること が可能となるが、 この場合にもかなりの設備投資が必要となってくる。 しかし、 通常、 複数の急速濾過池がつながっているような浄水場では、 各急速濾過池の逆 流洗浄は処理能力の観点から同時には行われず、 タイミングをずらして行うよう になっている。 従って、 たとえばこのずれたタイミングを利用すれば、 急速濾過 池が複数に増えた場合にも、 1つの濾過池の濾過砂を全て洗浄する時間と殆ど変 わらない時間で全ての濾過池の濾過砂の洗浄を行うことができ、 しかも貯留槽は 単一の濾過池の濾過砂を洗浄する場合と同様の規模の貯留槽 1つで足りるので設 備費用の観点からも好ましい。  The reason that the stored filter sand was returned to a filter pond different from the filter pond that absorbed the filter sand was that when the filter pond was returned to the same filter pond, the filter sand that had been washed until the next backwashing of the filter pond was performed. Because it is not possible to return the filter, it takes substantially as much time to wash the filter basin one by one with filter sand. If multiple storage tanks are provided, there is no difference in the time required to wash the filter sand from a single filtration pond even if it is returned to the same filtration pond, but this requires considerable equipment costs and land. Not economic. Also, if a very large storage tank is provided, it is possible to store the filtered sand that has been sucked and washed from multiple filtration ponds, but this also requires considerable capital investment. However, in a water treatment plant where multiple rapid filtration ponds are connected, backwashing of each rapid filtration basin is not performed at the same time from the viewpoint of processing capacity, and the timing is shifted. Therefore, for example, by using this deviated timing, even if the number of the rapid filtration ponds increases, the filtration sands of all the filtration ponds can be almost the same as the time for washing all the filtration sand in one filtration basin. Cleaning can be performed, and the storage tank needs only one storage tank of the same size as that for washing the filter sand of a single filtration pond, which is preferable from the viewpoint of installation costs.

また、 複数の急速濾過池を有する浄水場では、 濾過砂の汚れがひどい濾過池と 濾過砂の汚れが比較的少ない濾過池が存在する場合がある。このような場合には、 濾過砂の汚れがひどい濾過池から吸い取つた濾過砂は、 濾過砂の汚れが比較的少 ない濾過池に戻し、濾過砂の汚れが比較的少ない濾過池から吸い取った濾過砂は、 濾過砂の汚れがひどい濾過池に戻すことが複数の濾過池め濾過砂の平準化の観点 からより好ましい。 In addition, in a water treatment plant with multiple rapid filtration ponds, there may be a filtration basin with heavy filtration sand and a filtration basin with relatively little filtration sand. In such a case, Filter sand that has been sucked from a filter pond that has very bad filter sand is returned to the filter pond that has relatively little filter sand, and filter sand that has been sucked from the filter pond that has relatively little filter sand is filtered. It is more preferable to return the filter to a filter tank with heavy dirt from the viewpoint of leveling the filter sand in a plurality of filters.

これらの各工程の繰り返しはシーケンス制御により自動的に行うことが好まし い。 すなわち、 急速濾過池の逆流洗浄は圧力損失や時間をファクタ一として制御 することができるので、 シーケンス制御により、 濾過砂の吸取り、 洗浄、 戻しの 工程あるいは、 濾過砂の吸取り、 洗浄、 貯留、 戻しの工程の一連の流れを自動的 に行うことができる。  It is preferable that the repetition of each of these steps is automatically performed by sequence control. In other words, backwashing of a rapid filtration pond can be controlled with pressure loss and time as factors, and the sequence control can be used to suck, wash, and return filtered sand, or to suck, wash, store, and return filtered sand. A series of steps can be performed automatically.

濾過砂の吸取りと戻しはともに濾過砂が浮遊している逆流洗浄中に行われるた め、 吸い取られる濾過砂にすでに汚れを除去された濾過砂が混ざらないことが洗 浄効率を上げるために好ましい。 従って急速濾過池内の濾過砂を吸い取る位置か ら離れた位置に汚れを除去した濾過砂を戻すことが好ましい。 すなわち、 急速濾 過池から濾過砂を吸い取る手段と汚れを除去した濾過砂を戻す手段は離して設け ることが好ましい。 また、 濾過砂の洗浄効率の観点から、 濾過砂を吸い取る位置 は、 濾過砂を吸い取る毎に移動させることが、 汚れを除去した濾過砂を戻す位置 もまた、 濾過砂を戻す毎に移動させることが好ましい。 すなわち、 急速濾過池か ら濾過砂を吸い取る手段と、 前記急速濾過池へ汚れを除去した砂を戻す手段の少 なくとも一方が移動可能に設けられていることが好ましい。  Since both suction and return of the filter sand are performed during backwashing where the filter sand is floating, it is preferable that the filter sand that has already been removed is not mixed with the filter sand that has been removed to increase the cleaning efficiency. . Therefore, it is preferable to return the filtered sand from which dirt has been removed to a position away from the position where the sand is sucked in the rapid filtration tank. That is, it is preferable that the means for sucking the filtered sand from the rapid filtration pond and the means for returning the filtered sand from which dirt has been removed are provided separately. In addition, from the viewpoint of washing efficiency of the filter sand, the position where the filter sand is sucked should be moved each time the filter sand is sucked, and the position where the filter sand after removing the dirt is returned should also be moved each time the filter sand is returned. Is preferred. That is, it is preferable that at least one of the means for sucking the filtered sand from the rapid filtration pond and the means for returning the soil-removed sand to the rapid filtration pond is movably provided.

「砂洗浄装置」 としては、 特開平 10- 109051 号に開示されているような装置、 すなわち砂とともに洗浄水を貯留する洗浄槽と、 該洗浄槽 でほぼ鉛直な軸の回 りに回転するスクリユーコンベアと、 該スクリューコンペァを、 前記洗浄水の水 面下にある前記スクリユーコンベアの下部において該スクリユーコンベアの回転 により前記砂と前記洗浄水を上昇させるとともに該洗浄水を介在させた前記砂同 士の接触により該砂の汚れを除去し、 前記洗浄水の水面上にある前記スクリュー コンベアの上部において前記砂を前記スクリューコンベア上で流動させて、 汚泥 を含む水をわずかに含む前記砂同士の接触によって該砂の汚れを除去するような 速度で回転させる手段と、 上昇させた該砂を前記スクリューコンベアの下部まで 下降させ、 再び該スクリューコンベアで上昇させる循璟手段とからなる装置を使 用することが好ましい。 The "sand cleaning device" includes a device as disclosed in Japanese Patent Application Laid-Open No. 10-109051, that is, a cleaning tank for storing cleaning water together with sand, and a screw rotating around a substantially vertical axis in the cleaning tank. The screw conveyor is rotated by rotating the screw conveyor at a lower portion of the screw conveyor below the surface of the washing water to raise the sand and the washing water and interpose the washing water. The dirt of the sand is removed by the contact of the sand, and the sand is flowed on the screw conveyor at the upper part of the screw conveyor on the surface of the washing water, so that the water containing the sludge is slightly contained. Means for rotating the sand at such a speed as to remove dirt from the sand by contact between the sands, and lowering the raised sand to a lower portion of the screw conveyor, and And a circulating means for ascending with the screw conveyor. It is preferred to use

従来表面洗浄、 逆流洗浄という洗浄方法のみに頼っていた濾過砂の洗浄を、 本 発明の濾過砂洗浄方法は、 逆流洗浄時に急速濾過池から所定量の濾過砂を吸い取 り、 吸い取った濾過砂を砂洗浄装置に供給し、 砂洗浄装置によって濾過砂の汚れ を除去し、 汚れを除去した濾過砂を逆流洗浄時に急速濾過池に戻し、 この濾過砂 の吸い取り、 洗浄、 戻しを繰り返すことによって急速濾過池内の濾過砂を洗浄す ることとしたので、 濾過池の運転を休止することなく効果的に濾過砂の洗浄がで き、 濾過池の更生工事の周期を飛躍的に延長することができる。  Conventionally, filter sand cleaning, which relied solely on surface cleaning and backwashing, has been replaced by a filter sand washing method according to the present invention. Is supplied to the sand washer, the dirt from the filtered sand is removed by the sand washer, and the filtered sand from which the dirt has been removed is returned to the rapid filtration pond during backwashing, and the filtered sand is repeatedly sucked, washed and returned. Since the filter sand in the filter pond is to be cleaned, the filter sand can be washed effectively without stopping the operation of the filter pond, and the cycle of filter rehabilitation work can be drastically extended. .

より具体的には、 たとえば濾過砂の吸取り、 洗浄、 戻しを繰り返すことによつ て急速濾過池内のほぼ全濾過砂を自動的に洗浄すれば、 濾過池の水浄化機能を再 生させることが可能となる。 また、 濾過砂の汚れが除去されていれば濾過抵抗を 減らすことが可能となるので設計通りの圧力で逆流洗浄を行えばよく、 従って濾 過砂の流出を減らすこと、 及び剥離する汚泥の流出を大幅に減らすことが可能と なり、 また不陸の形成を遅らせることが可能となるので、 この点からも濾過池の 更生工事の周期を飛躍的に延長することができる。  More specifically, if almost all of the sand in the rapid filtration tank is automatically washed, for example, by repeatedly sucking, washing and returning the sand, the water purification function of the filtration tank can be regenerated. It becomes possible. In addition, if dirt from the filter sand is removed, it is possible to reduce the filtration resistance.Therefore, it is only necessary to carry out backwashing at the designed pressure.Therefore, it is possible to reduce the outflow of filter sand and the outflow of exfoliated sludge. Therefore, the period of rehabilitation works for filter ponds can be dramatically extended from this point.

なお、 逆流洗浄時に急速濾過池から所定量の濾過砂を吸い取り、 吸い取った濾 過砂を砂洗浄装置に供給し、 砂洗浄装置によって濾過砂の汚れを除去し、 汚れを 除去した濾過砂を貯留槽に貯留し、 貯留しておいた濾過砂を濾過砂を吸い取った 急速濾過池とは異なる急速濾過池の逆流洗浄時に戻し、 濾過砂の吸取り、 洗浄、 貯留、 戻しの工程を繰り返すことにより、 濾過池の運転を休止することなく複数 の濾過池の濾過砂を効率的に洗浄することができる。 また、 貯留しておいた濾過 砂を、 濾過砂を吸い取った急速濾過池とは異なる急速濾過池に戻すので、 単一の 濾過池の濾過砂を全て洗浄するのにかかる時間と殆ど変わらない時間で複数の濾 過池の濾過砂の洗浄が可能となる。 さらに、 濾過砂を戻す際に、 濾過砂の汚れが ひどい濾過池から吸い取った濾過砂は、 濾過砂の汚れが比較的少ない濾過池に戻 し、 濾過砂の汚れが比較的少ない濾過池から吸い取った濾過砂は、 濾過砂の汚れ がひどい濾過池に戻すこととすれば、 濾過池の濾過砂の平準化を図ることができ る。 '  In addition, at the time of backwashing, a predetermined amount of filter sand is sucked from the rapid filtration pond, and the sucked filter sand is supplied to the sand washer, and the sand is removed by the sand washer, and the filtered sand is removed and stored. By storing the filtered sand in the tank and returning the stored filtered sand during backwashing of the rapid filtration pond, which is different from the rapid filtration pond that absorbed the filtered sand, and repeating the process of sucking, washing, storing, and returning the filtered sand, It is possible to efficiently wash the filter sand from a plurality of filtration ponds without stopping the operation of the filtration ponds. In addition, since the stored filtered sand is returned to the rapid filtration pond different from the rapid filtration pond that sucked the filtered sand, the time is almost the same as the time required to wash all the filtered sand in a single filtration pond. This makes it possible to wash the filtered sand from multiple filtration ponds. In addition, when returning the filter sand, the filter sand sucked from the filter pond where the filter sand is very dirty is returned to the filter pond where the filter sand is relatively less contaminated, and the filter sand is collected from the filter pond where the filter sand is less contaminated. If the filtered sand is returned to the filter pond where the filter sand is very dirty, the filter sand in the filter pond can be leveled. '

また、 本発明の濾過砂洗浄方法及びそのシステムの砂洗浄装置に、 砂とともに 洗浄水を貯留する洗浄槽と、 該洗浄槽内でほぼ鉛直な軸の回りに回転するスクリ ユーコンベアと、 該スクリューコンベアを、 前記洗浄水の水面下にある前記スク リユーコンベアの下部において該スクリユーコンベアの回転により前記砂と前記 洗浄水を上昇させるとともに該洗浄水を介在させた前記砂同士の接触により該砂 の汚れを除去し、 前記洗浄水の水面上にある前記スクリューコンベアの上部にお いて前記砂を前記スクリューコンベア上で流動させて、 汚泥を含む水をわずかに 含む前記砂同士の接触によって該砂の汚れを除去するような速度で回転させる手 段と、 上昇させた該砂を前記スクリユーコンベアの下部まで下降させ、 再び該ス クリューコンベアで上昇させる循環手段とからなる装置を使用すれば、 砂を砕く ことなく砂同士が揉み合って汚れを落とすことが可能となるので、 濾過砂の水浄 化機能を新砂に近い状態に再生することができ、 濾過池の更生工事の周期をさら に飛躍的に延長することができる。 In addition, the sand cleaning method of the present invention and the sand cleaning apparatus of the system, together with the sand, A washing tank that stores washing water, a screw conveyor that rotates around a substantially vertical axis in the washing tank, and a screw conveyor that is disposed below the screw conveyor below the surface of the washing water. The rotation of the U-conveyor raises the sand and the washing water, and removes dirt from the sand by contact between the sands with the washing water interposed therebetween. Means for causing the sand to flow on the screw conveyor and rotating the sand at such a speed as to remove dirt from the sand by contact between the sands containing a small amount of water containing sludge; and If a device consisting of circulating means for lowering the screw conveyor to the lower part of the screw conveyor and raising it again by the screw conveyor is used, the sand is not crushed. Sand can be rubbed against each other to remove dirt, so that the water purification function of filtered sand can be regenerated to a state similar to fresh sand, further extending the cycle of filter tank rehabilitation work. be able to.

また、 浄水場ではクリプトスポリジゥム対策として、 従来表面洗浄や逆流洗浄 の頻度を上げて対応してきていたが、 通常の頻度で表面洗浄、 逆流洗浄を行えば 濾過池出口の濁度を 0.1 度以下に維持することが可能となるので、 クリプトスポ リジゥム対策の一助となり、 かつ浄化効率が下がることなく浄水場を稼動させる ことができる。  In the water treatment plant, as a countermeasure against cryptosporidium, the frequency of surface washing and backwashing has been increased in the past. It is possible to maintain the temperature below this level, which helps to prevent cryptosporium and allows the water treatment plant to operate without any reduction in purification efficiency.

図面の簡単な説明  BRIEF DESCRIPTION OF THE FIGURES

第 1図は、 本発明の濾過砂洗浄方法の実施の形態を示す工程図、 第 2図は、 本 発明の濾過砂洗浄システムの第一の実施の形態を示す概略図、 第 3図は、 本発明 の濾過砂洗浄システムの第二の実施の形態を示す概略図、 第 4図は、 本発明の濾 過砂洗浄方法の他の実施の形態を示す工程図、 第 5図は、 本発明の濾過砂洗浄方 法のさらに他の実施の形態を示す工程図、 第 6図は、 図 2に示す急速濾過池の A —A線断面図、 第 7図は、 複数の濾過池に対応した濾過砂の流れを示す図、 第 8 図は、 濾過池間の濾過砂の移動の一例を示す図である。  FIG. 1 is a process diagram showing an embodiment of the filtered sand washing method of the present invention, FIG. 2 is a schematic diagram showing a first embodiment of the filtered sand washing system of the present invention, FIG. FIG. 4 is a schematic diagram showing a second embodiment of the filter sand washing system of the present invention, FIG. 4 is a process diagram showing another embodiment of the filter sand washing method of the present invention, and FIG. 6 is a process diagram showing still another embodiment of the filter sand washing method, FIG. 6 is a sectional view taken along line A--A of the rapid filtration pond shown in FIG. 2, and FIG. FIG. 8 is a diagram showing a flow of the filtration sand, and FIG. 8 is a diagram showing an example of the movement of the filtration sand between the filtration ponds.

発明を実施するための最良の开 態 BEST MODE FOR CARRYING OUT THE INVENTION

本発明の濾過砂洗浄システムは、 図 2に示すように、 急速濾過池 1と、 急速濾 過池 1から汚れが付着した濾過砂を吸い取るポンプ 2と、 汚れが付着した濾過砂 5を洗浄する砂洗浄装置 3と、 砂洗浄装置 3で洗浄された濾過砂 6をストックし ておく洗浄砂ストツク槽 4と、 洗浄砂ストツク槽 4から急速濾過池 1へ汚れを除 去した砂を戻す経路 7を備えてなるものである。 (この濾過砂洗浄システムの処 理工程の詳細は実施例により後述する。 ) As shown in FIG. 2, the filter sand washing system of the present invention, as shown in FIG. 2, cleans the filter sand with dirt adhering from the rapid filtration pond 1, the rapid filtration pond 1, and the filter sand 5 with dirt adhering thereto. Stock the sand washer 3 and the filtered sand 6 washed by the sand washer 3. It is provided with a washing sand stock tank 4 to be stored, and a path 7 for returning dirt-removed sand from the washing sand stock tank 4 to the rapid filtration pond 1. (Details of the processing steps of this filter sand washing system will be described later with reference to examples.)

また、 本発明の濾過砂洗浄システムは、 図 3に示すように、 急速濾過池 1と、 急速濾過池 1から汚れが付着した濾過砂を吸い取るポンプ 2と、 汚れが付着した 濾過砂 5を洗浄する砂洗浄装置 3と、 砂洗浄装置 3から急速濾過池 1へ汚れを除 去した砂を戻す経路 7とを備えてなるもの、 すなわち洗浄砂ストック槽を備えて いないものであってもよい。 洗浄砂ストック槽を備えていない濾過砂洗浄システ ムの場合には、 洗浄 ストック槽にかかる費用を節約することが可能となり、 ま た、 急速濾過池の周囲に洗浄砂ストツク槽を設置する土地の余裕がない場合など にはより好ましい態様である。  Further, as shown in FIG. 3, the filter sand washing system of the present invention, as shown in FIG. 3, cleans a quick filter pond 1, a pump 2 for sucking filter sand with dirt from the quick filter pond 1, and a filter sand 5 with dirt. It may be provided with a sand washing device 3 to be cleaned and a path 7 for returning the sand from which dirt has been removed from the sand washing device 3 to the rapid filtration pond 1, that is, a device without a washing sand stock tank. In the case of a filtration sand washing system without a washing sand stock tank, it is possible to save the cost of the washing stock tank, and also to install a washing sand stock tank around the rapid filtration pond. This is a more preferable mode when there is no room.

図 3に示す濾過砂洗浄システムの処理の例としては、例えば図 4に示すように、 濾過池 1の表面洗浄、 逆流洗浄が行われている時間 (例: 15分〜 25分) 内に約 1 m3 の汚れた濾過砂を濾過池 1からポンプ 2で吸引し、 ポンプ 2で吸引した濾過 砂を砂洗浄装置 3に送り、 砂洗浄装置 3で短い時間 (約 10分程度) 内の洗浄を行 い、 濾過池 1の表面洗浄、 逆流洗浄が終了する前に洗浄後の濾過砂 (浄砂) を濾 過池 1に戻すという工程により行うことができる。 このように一つの表面洗浄、 逆流洗浄が行われている時間内に、汚砂の吸取りと浄砂の戻しを行うことにより、 短時間で汚砂の洗浄を行うことが可能となる。 As an example of the treatment of the filter sand cleaning system shown in Fig. 3, as shown in Fig. 4, for example, the surface cleaning and backwashing of the filtration pond 1 are performed within the time (eg, 15 to 25 minutes). the 1 m 3 of contaminated filtration sand by suction from the filtration reservoir 1 by the pump 2, sends the filtration sand sucked by the pump 2 to the sand washing device 3, washing in a short time, the sand washing device 3 (about 10 minutes) Before the surface cleaning and backwashing of the filtration pond 1 is completed, the filtered sand (clean sand) after the washing can be returned to the filtration pond 1. In this way, by performing the suction of the sand and the return of the clean sand during the time when one surface cleaning and backwashing are being performed, it becomes possible to wash the sand in a short time.

あるいは、 図 5に示すように、 濾過池 1の表面洗浄、 逆流洗浄が行われている 時間 (例: 7分〜 10分) 内に汚れた濾過砂を濾過池 1からポンプ 2で連続して吸 引し、 ポンプ 2で吸引した濾過砂を砂洗浄装置 3に連続して送り、 砂洗浄装置 3 で連続洗浄を行い、 濾過池 1の表面洗浄、 逆流洗浄が終了する前に浄砂を濾過池 1に連続して戻すという工程により処理を行うこともできる。 このように表面洗 浄、 逆流洗浄が行われている時間内に連続して処理を行えば、 短時間でより多く の汚砂の洗浄を行うことができる。  Alternatively, as shown in Fig. 5, during the time during which surface cleaning and backwashing of filter pond 1 are performed (eg, 7 to 10 minutes), contaminated filtered sand is continuously pumped from filter pond 1 using pump 2. The filtered sand sucked by the pump 2 is continuously sent to the sand washing device 3 and continuously washed by the sand washing device 3, and the purified sand is filtered before the surface washing and backwashing of the filtration pond 1 are completed. The treatment can also be performed by a process of continuously returning to pond 1. If the treatment is performed continuously during the time during which the surface cleaning and the backwashing are performed, it is possible to wash a larger amount of soil in a short time.

急速濾過池 1は、 第 6図に示すように濾過層として濾過砂層 12と、 濾過砂層 12 を支える 13〜; 16の砂利層を備えている。濾過砂層 12は、有効径 0.6mm、均等係数 1.5 以下の砂からなる。 砂利層は粒径の異なる 4層からなり、 支持層として濾過砂 12 が集水装置 (図示していないが、 浄化された水が集水される装置が急速濾過池 1 のさらに下部に設けられている) に入ることを防いでいる。 砂利層 13〜16は、 逆 流洗浄を均等に行うため、 球形に近く硬質で清浄、 均質なものが選定され、 その 粒径としては一般的に用いられるもの、すなゎち砂利層13には有効径2.0 〜3. 5111111、 砂利層 14には 3.5〜7.0難、砂利層 15には 7. 0〜13. Omm、砂利層 16には 13. 0〜20. Omm と、 細粒を上層に粗粒を下層に順次不陸のないように敷き詰められている。 濾過 砂層 12の上には原水の濁質を凝集剤によって凝集、 沈殿させて前処理された水が 導入されている。 また濾過砂層 12の上方には、 表面洗浄の際に濾過砂層を表面か ら叩くように洗浄する表洗水をノズルから噴射する表洗管 22と、 表面洗浄、 逆流 洗浄の際の洗浄排水を排出するトラフ 21が設けられている。 As shown in FIG. 6, the rapid filtration pond 1 has a filtration sand layer 12 as a filtration layer, and 13 to 16 gravel layers supporting the filtration sand layer 12. The filter sand layer 12 is made of sand having an effective diameter of 0.6 mm and a uniformity coefficient of 1.5 or less. The gravel layer consists of four layers with different particle sizes, and the filter sand is used as a support layer. Is prevented from entering the water collection device (not shown, but the device for collecting the purified water is provided further below the rapid filtration pond 1). The gravel layers 13 to 16 are selected to be nearly spherical, hard, clean, and homogeneous in order to perform backwashing evenly. The effective diameter is 2.0 to 3.511111, the gravel layer 14 is 3.5 to 7.0 difficult, the gravel layer 15 is 7.0 to 13.Omm, and the gravel layer 16 is 13.0 to 20.Omm. Coarse grains are spread in the lower layer so that there is no irregularity. On the filtration sand layer 12, water that has been pretreated by flocculating and precipitating the turbidity of the raw water with a flocculant is introduced. Above the filter sand layer 12, a washing pipe 22 for spraying washing water for washing the filter sand layer from the surface so that the filter sand layer is hit from the surface during washing, and washing drainage for washing the surface and backwashing. An exhaust trough 21 is provided.

次に原水の一般的な浄化処理工程を簡単に説明する。 河川、 湖などから凝集沈 殿池に引き込まれた原水の濁質をポリ塩化アルミニウムなどの凝集剤によって凝 集、 沈殿させた後、 上澄みは急速濾過池 1の濾過砂層 12の上に送水される。 この 濾過砂層 12によって凝集沈殿池では除去できなかった微細な浮遊物が取り除かれ る。 濾過した水は急速濾過池 1の下部に設けられている集水装置に集水される。 集水された水は塩素で消毒されて配水池に貯水される。 濾過速度は通常 120〜150 m/日である。 一般にはこの濾過速度で定時的にあるいは損失水頭が 1.5mに達す ると、 浄水のための濾過は中止され急速濾過池の下部圧力室から洗浄水を圧入し て濾過砂を浮上させ、 砂と砂とをもみ合わせて洗浄が行われる。 表面洗浄は逆流 洗浄時または逆洗サイクルのある時間に合わせて、 濾過砂 12の表面に表洗管 22か ら洗浄水を噴射させて行われる。 表面洗浄、 逆流洗浄後の洗浄排水 11はトラフ 21 から排出される。 洗浄が終了すると再び、 前処理された原水が送水されて濾過が 再開される。 この浄水、 洗浄の工程は通常自動化されており、 急速濾過法で浄水 処理を行う浄水場の原水の状態により、 表面洗浄、 逆流洗浄を行うタイミングが あらかじめ設定されていたり、 あるいは損失水頭が一定値以上になると自動的に 表面洗浄、 逆流洗浄が行われるように設定されている。  Next, a general purification process of raw water will be briefly described. After the turbidity of raw water drawn from rivers and lakes into the coagulation sedimentation ponds is condensed and precipitated by a coagulant such as polyaluminum chloride, the supernatant is sent to the filtration sand layer 12 of the rapid filtration pond 1 . This filtration sand layer 12 removes fine suspended matter that could not be removed by the coagulation sedimentation basin. The filtered water is collected in a water collecting device provided at the lower part of the rapid filtration pond 1. The collected water is disinfected with chlorine and stored in a reservoir. The filtration speed is usually between 120 and 150 m / day. In general, at this filtration speed, when the head loss reaches 1.5 m at regular intervals, the filtration for water purification is stopped, and washing water is injected from the lower pressure chamber of the rapid filtration pond to lift the filter sand, and the sand is removed. Washing is performed by mixing with sand. The surface washing is performed by spraying washing water from the front washing tube 22 onto the surface of the filter sand 12 at the time of backwashing or at a certain time during the backwash cycle. Washing drainage 11 after surface washing and backwashing is discharged from trough 21. When the washing is completed, the pretreated raw water is sent again and the filtration is resumed. The process of water purification and washing is usually automated, and the timing of surface washing and backwashing is set in advance depending on the condition of the raw water at the water treatment plant where the water is treated by the rapid filtration method, or the head loss is fixed. It is set so that surface cleaning and backwashing are automatically performed when the above occurs.

表 2に示すように濾過砂の選定標準 (日本水道協会規格 JWWA A 103-1988 ) は、 洗浄濁度は 30度以下、塩酸可溶率は 3.5%以下、有効径 0.45〜0.70顧、均等係数 1.7 以下と定められている。 上記のような一般的な表面洗浄、 逆流洗浄を定期的に行 つていても、 新砂から 10年もたつと、 7年おきに更生工事を行っても表 2の原汚 砂に示すように洗浄濁度 1480度、塩酸可溶率 9.7%、有効径 0.533画、均等係数 1.485 と濾過砂に濁質が付着し、 相当に汚れてくる。 As shown in Table 2, the selection standard for filtered sand (JWWA A 103-1988) is that the washing turbidity is 30 degrees or less, the hydrochloric acid solubility is 3.5% or less, the effective diameter is 0.45 to 0.70, and the uniformity coefficient is 1.7 It is stipulated below. Regularly perform general surface cleaning and backwashing as described above. Even after renovation every 10 years, the turbidity of washing was 1480 degrees, the solubility of hydrochloric acid was 9.7%, and the effective diameter was 0.533. With an equality coefficient of 1.485, turbidity adheres to the filtered sand and becomes considerably dirty.

【表 2】  [Table 2]

Figure imgf000013_0001
このように、 濁質が付着した濾過砂を使用し続けると濁質による目詰まり現象が 起こり、 急激な損失水頭の上昇により逆流洗浄の回数が増加し、 その逆流洗浄の 水圧により砂利層にも影響が出て不陸の形成を早める。 不陸の形成により砂利層 が厚い部分では砂層が薄くなり、 その部分での濾過が不十分となり、 また汚泥物 質や濾過砂から剥離した吸着物質により、 ブレークスルーが起こって濾過水に悪 影響を及ぼすようになる。 このような状態になると、 更生工事が必要となってく る。
Figure imgf000013_0001
As described above, if filter sand with turbidity is continued to be used, clogging by the turbidity occurs, and the number of backwashing increases due to a sudden rise in head loss, and the gravel layer is also formed by the water pressure of the backwashing. Influence hastens the formation of unevenness. Due to the formation of unevenness, the sand layer becomes thinner in the part where the gravel layer is thicker, and the filtration in that part becomes insufficient, and the sludge substances and the adsorbed substances separated from the filter sand cause breakthrough, which adversely affects the filtered water. Will be exerted. In such a situation, rehabilitation work will be required.

以下に、 上記の通常の洗浄工程に、 さらに濾過砂の一部を取って砂洗浄装置で 洗浄し、 汚れを除去した砂を再び濾過池に戻す工程を行う濾過砂洗浄システムの 実施例を示す。  The following is an example of a filter sand washing system in which a part of the filter sand is washed with a sand washing device, and the soil-removed sand is returned to the filter tank again, in addition to the normal washing process described above. .

(実施例 1 )  (Example 1)

砂洗浄装置 3には、 特開平 10-109051 号に開示されている、 砂とともに洗浄水 を貯留する洗浄槽と、 該洗浄槽内でほぼ鉛直な軸の回りに回転するスクリユーコ ンベアと、 該スクリユーコンベアを、 前記洗浄水の水面下にある前記スクリュー コンベアの下部において該スクリューコンベアの回転により前記砂と前記洗浄水 を上昇させるとともに該洗浄水を介在させた前記砂同士の接触により該砂の汚れ を除去し、 前記洗浄水の水面上にある前記スクリューコンベアの上部において前 記砂を前記スクリューコンベア上で流動させて、 汚泥を含む水をわずかに含む前 記砂同士の接触によって該砂の汚れを除去するような速度で回転させる手段と、 上昇させた該砂を前記スクリューコンベアの下部まで下降させ、 再び該スクリュ ーコンベアで上昇させる循環手段とからなる、 揉み洗い工法を実現できる装置を 用いた。 第 1図、 第 2図に示すように、 濾過池 1の表面洗浄、 逆流洗浄が行われ ている時間 (7分〜 10分) 内に l m3 の汚れた濾過砂を濾過池 1の角部 (la) か らポンプ 2で吸引した。 濾過砂の吸引は、 砂利層 13の上部から約 10cm程度の深さ で行った (濾過砂層厚は 60cm) 。 ポンプ 2で吸引した濾過砂 (5 ) を、 砂洗浄装 置 3に送り、 砂洗浄装置 3で約 1時間洗浄を行った。 表 3に示すように、 約 1時 間の洗浄により、 吸引された濾過砂 ( 5 ) の洗净濁度は 1480度から 11度へ、 塩酸 可溶率は 9.7%から 2.8%へ、 均等係数は 1.485から】.280と洗浄が新砂と同様の水 準にまで行われていることがわかる。 The sand washing device 3 includes a washing tank disclosed in Japanese Patent Application Laid-Open No. 10-109051 for storing washing water together with sand, a screw conveyor rotating around a substantially vertical axis in the washing tank, and a screw conveyor. At the lower part of the screw conveyor below the surface of the washing water, the sand and the washing water are raised by the rotation of the screw conveyor, and the sand is contacted by the sand with the washing water interposed therebetween. The dirt is removed, and the sand is flowed on the screw conveyor at the upper part of the screw conveyor on the surface of the washing water, and the sand containing the sludge-containing water is slightly contacted with the sand. Means for rotating at such a speed as to remove dirt, A device capable of realizing a kneading-washing method was used, comprising circulating means for lowering the raised sand to the lower portion of the screw conveyor and again raising the sand on the screw conveyor. As shown in Fig. 1 and Fig. 2, during the time (7 to 10 minutes) during which the surface cleaning and backwashing of filter basin 1 are performed, lm 3 of dirty filter sand is removed at the corner of filter basin 1. (La) was pumped by pump 2. The suction of the filtered sand was performed at a depth of about 10 cm from the upper part of the gravel layer 13 (the thickness of the filtered sand layer was 60 cm). The filtered sand (5) sucked by the pump 2 was sent to the sand washing device 3 and washed by the sand washing device 3 for about 1 hour. As shown in Table 3, the washing turbidity of the suctioned filter sand (5) was reduced from 1480 ° C to 11 ° C, the hydrochloric acid solubility was changed from 9.7% to 2.8%, and the coefficient of uniformity was increased by washing for about 1 hour. From 1.485, it can be seen that washing is performed to the same level as that of fresh sand.

【表 3】  [Table 3]

Figure imgf000014_0001
Figure imgf000014_0001

洗浄後の濾過砂 (6a) は水が張られた洗浄砂ストック槽で保管した。 急速濾過池 1で再び行われていた濾過から約 48時間経過後、濾過は中止され、再び表面洗浄、 逆流洗浄が開始され、 この際に、 角部 (la) とは相対する角部 (lb) から洗浄し た砂を濾過池 1へ戻した。 このサイクルを繰り返すことにより、 濾過池 1の濾過 砂 60m3のほぼ全量の砂を約 120 日で洗浄した。 The filtered sand (6a) after washing was stored in a washing sand stock tank filled with water. Approximately 48 hours after the filtration performed in the rapid filtration tank 1, the filtration was stopped, and surface cleaning and backwashing were started again. At this time, the corner (lb) opposite to the corner (la) ) Was returned to the filtration pond 1. By repeating this cycle, almost all the sand of 60 m 3 in the filter pond 1 was washed in about 120 days.

(実施例 2 )  (Example 2)

上記実施例 1で用いた特定の砂洗浄装置を、 従来のジエツト水流による砂洗浄 装置に変えて行うこと以外は実施例 1と同様に濾過砂洗浄を行った。 表 4に示す ように実施例 1の特定の砂洗浄装置を用いたものに比較して、 若干の有意差はあ るが原汚砂からは格段に洗浄された。 但し、 実施例 1の場合には砂の粒径にほと んど変化はみられなかったが、 長時間洗浄を行ううちに有効径は下がり、 均等係 数は大きくなつた。 ジェット水流を用いた従来の砂洗浄装置では、 洗浄中に砂が 管壁等に衝突して砂の破砕が生じていることがわかる。 Filtered sand cleaning was performed in the same manner as in Example 1 except that the specific sand cleaning device used in Example 1 was changed to a conventional sand cleaning device using a jet stream. As shown in Table 4, there was a slight significant difference compared to the one using the specific sand washing device of Example 1, but the sand was remarkably washed. However, in the case of Example 1, there was almost no change in the particle size of the sand, but the effective diameter was reduced and the uniformity coefficient was increased after long-time cleaning. With conventional sand washing equipment using jet water, sand is washed during washing. It can be seen that the sand crushed due to collision with the pipe wall or the like.

【表 4】  [Table 4]

Figure imgf000015_0001
Figure imgf000015_0001

次に、急速濾過池が複数の場合の濾過砂の洗浄方法とシステムについて第 7図、 第 8図を用いて説明する。 第 7図は複数の濾過池に対応した濾過砂の流れを示す 図、 第 8図は濾過池間の濾過砂の移動の一例を示す図である。 ここでは第 7図に 示すように急速濾過池 A〜Fの 6つの急速濾過池と、 1台の砂洗浄装置と 1槽の 貯留槽とを組み合わせた濾過砂システムを例にとって説明するが濾過池の数はこ れ以上であってもまた、 これ以下であっても原理は全く同じである。  Next, a method and a system for filtering sand in the case of a plurality of rapid filtration ponds will be described with reference to FIGS. FIG. 7 is a diagram showing the flow of the filter sand corresponding to a plurality of filter ponds, and FIG. 8 is a diagram showing an example of the movement of the filter sand between the filter ponds. Here, as an example, a filter sand system combining six quick filter ponds A to F as shown in Fig. 7 and one sand washing device and one storage tank is described. The principle is exactly the same whether the number is larger or smaller.

濾過池 A〜 Fはそれそれ 48時間おきに逆流洗浄が行われる濾過池である。 第 7 図に示すように各濾過池の逆流洗浄が行われる時間の間隔は 8時間である。まず、 濾過池 Aから所定量の濾過砂が吸い取られる。 吸い取られた濾過砂は砂洗浄装置 で 1時間洗浄される。 汚れを除去された濾過砂は水あるいは酸化剤を含んだ水が 張られた貯留槽に貯留される。 貯留された洗浄後の濾過砂は、 濾過池 Aの逆流洗 浄から 8時間経過した後に逆流洗浄が始まる濾過池 Bに戻される。 濾過池 Bの逆 流洗浄時には洗浄された濾過砂が戻されるとともに、 汚れた濾過砂が吸い取られ る。 濾過池 Bで吸い取られた濾過砂は砂洗浄装置で 1時間洗浄され、 洗浄された 濾過砂は水あるいは酸化剤を含んだ水が張られた貯留槽に貯留される。 貯留され た洗浄後の濾過砂は、 濾過池 Bの逆流洗浄から 8時間経過した後に逆流洗浄が始 まる濾過池 Cに戻される。 濾過池 Cの逆流洗浄時には洗浄された濾過砂が戻され るとともに、 汚れた濾過砂が吸い取られる。 このようにして、 48時間が経過する と濾過池 A〜Fの全ての濾過池において、 所定量の濾過砂が吸い取られるととも に、 所定量の洗浄後の濾過砂が戾されることになる。 この工程を繰り返して、 濾 過池 A〜 Fの全ての濾過砂を洗浄することができる。 このように複数の濾過池の 逆流洗浄のタイミングに合わせることにより、 単一の濾過池の濾過砂の洗浄にか かる時間とほとんど変わらない時間で複数の濾過池の濾過砂洗浄を行うことがで きる Filtration ponds AF are filtration ponds where backwashing is performed every 48 hours. As shown in Fig. 7, the interval between backwashing of each filtration pond is 8 hours. First, a predetermined amount of filter sand is sucked from filter pond A. The sucked filter sand is washed for 1 hour with a sand washing device. The filtered sand from which the dirt has been removed is stored in a storage tank filled with water or water containing an oxidizing agent. The stored filter sand after washing is returned to Filter Pond B where backwashing starts after 8 hours from backwashing of Filter Pond A. During backwashing of filtration basin B, washed filter sand is returned and dirty filter sand is absorbed. The filtered sand sucked in the filtration basin B is washed for 1 hour with a sand washing device, and the washed filtered sand is stored in a storage tank filled with water or water containing an oxidizing agent. The stored filter sand after washing is returned to Filter Pond C where backwashing starts after 8 hours from backwashing of Filter Pond B. During backwashing of filter pond C, the washed filter sand is returned and dirty filter sand is absorbed. In this way, after 48 hours, a predetermined amount of the filter sand is absorbed in all of the filter ponds A to F, and a predetermined amount of the filter sand after the washing is released. . This process can be repeated to wash all the filtered sand in the filtration ponds AF. In this way, multiple filtration ponds By matching the timing of backwashing, it is possible to wash the filter sand in multiple filtration ponds in a time that is almost the same as the time required to wash the filtration sand in a single filtration pond.

また、 仮に濾過池の濾過砂が、 濾過池 A Fの順で汚れがひどくなつている場 合には、 第 8図に示すように濾過池 Aの洗浄後の濾過砂を濾過池 Eに、 濾過池 E の洗浄後の濾過砂を濾過池 Cに、 濾過池 Cの洗浄後の濾過砂を濾過池 Dに、 濾過 池 Dの洗浄後の濾過砂を濾過池 Aに戻すことにより、 濾過池 A〜Fの濾過砂の平 準化を図ることができる。  If the filter sand from the filter pond is heavily soiled in the order of filter AF, filter sand after washing of filter A is filtered to filter E as shown in Fig. 8, and then filtered. Filter sand after washing of Pond E was returned to Filter Pond C, filtered sand after washing of Filter Pond C to Filter Pond D, and filtered sand after washing of Filter Pond D to Filter Pond A. ~ F can be leveled.

また、 少なくとも、 急速濾過池から濾過砂を吸い取る工程と砂洗浄装置で濾過 砂を洗浄する工程と急速濾過池へ汚れを除去した濾過砂を戻す工程の 3工程、 ま たは急速濾過池から濾過砂を吸い取る工程と砂洗浄装置で濾過砂を洗浄する工程 と洗浄した濾過砂を貯留槽で貯留する工程と急速濾過池へ汚れを除去した濾過砂 を戻す工程の 4工程をシーケンス制御により自動的に行うことにより、 濾過砂を 新砂同様の状態に長期間保つことが可能となり、 更生工事の周期を飛躍的に延長 することが可能となる。  In addition, at least three steps: a step of sucking filter sand from the rapid filtration pond, a step of washing the filter sand with a sand washing device, and a step of returning the filtered sand from which dirt has been removed to the rapid filter pond, or filtering from the rapid filter pond. Sequence control automatically performs four steps: sucking sand, washing the filtered sand with a sand washing device, storing the washed filtered sand in a storage tank, and returning the filtered sand from which dirt has been removed to the rapid filtration pond. By doing so, it is possible to maintain the filtered sand in the same state as fresh sand for a long period of time, and the cycle of rehabilitation work can be drastically extended.

Claims

請求の範囲 The scope of the claims ( 1 ) 濾過砂により水の浄化を行う急速濾過池の逆流洗浄時に該急速濾過池から 所定量の濾過砂を吸い取り、 該吸い取った濾過砂を砂洗浄装置に供給し、 該砂洗 浄装置によつて前記濾過砂の汚れを除去し、 汚れを除去した前記濾過砂を前記急 速濾過池の逆流洗浄時に該急速濾過池に戻し、 前記濾過砂の吸取り、 洗浄、 戻し の工程を繰り返して前記急速濾過池内の濾過砂を洗浄することを特徴とする濾過 砂洗浄方法。  (1) At the time of backwashing of a rapid filtration pond for purifying water with filter sand, a predetermined amount of filter sand is sucked from the rapid filtration pond, the sucked filter sand is supplied to a sand washing device, and the sand is washed by the sand washing device. Therefore, the filter sand is removed from the filter sand, and the filter sand from which the filter sand is removed is returned to the rapid filtration tank during backwashing of the rapid filtration tank, and the steps of sucking, washing, and returning the filter sand are repeated. A method for washing filtered sand, comprising washing filtered sand in a rapid filtration tank. ( 2 ) 前記砂洗浄装置として、 砂とともに洗浄水を貯留する洗浄槽と、 該洗浄槽 内でほぼ鉛直な軸の回りに回転するスクリューコンベアと、 該スクリューコンペ ァを、 前記洗浄水の水面下にある前記スクリュ一コンベアの下部において該スク リユーコンベアの回転により前記砂と前記洗浄水を上昇させるとともに該洗浄水 を介在させた前記砂同士の接触により該砂の汚れを除去し、 前記洗浄水の水面上 にある前記スクリユーコンペアの上部において前記砂を前記スクリユーコンベア 上で流動させて、 汚泥を含む水をわずかに含む前記砂同士の接触によって該砂の 汚れを除去するような速度で回転させる手段と、 上昇させた該砂を前記スクリュ —コンペァの下部まで下降させ、 再び該スクリユーコンベアで上昇させる循環手 段とからなる装置を使用することを特徴とする請求の範囲第 1項記載の濾過砂洗 浄方法。  (2) As the sand washing device, a washing tank that stores washing water together with sand; a screw conveyor that rotates around a substantially vertical axis in the washing tank; and a screw conveyor that is below the surface of the washing water. The lower part of the screw conveyor, the rotation of the screw conveyor raises the sand and the washing water, and removes dirt from the sand by contact between the sands with the washing water interposed therebetween; The sand is made to flow on the screw conveyor at the upper part of the screw conveyer on the water surface at a speed such that the sand containing a small amount of water containing sludge contacts the sand to remove dirt from the sand. A rotating means, and a circulating means for lowering the raised sand to the lower part of the screw-conveyor and raising the sand again by the screw conveyor. Filtration sand washing process ranging first claim of claim, characterized in that the use of that device. ( 3 ) 前記砂洗浄装置によって濾過砂の汚れを除去した後、 該汚れを除去した濾 過砂を前記急速濾過池に戻すまで貯留槽に貯留することを特徴とする請求の範囲 第 1項または第 2項記載の濾過砂洗浄方法。  (3) After removing dirt from the filtered sand by the sand washing device, the filtered sand from which the dirt has been removed is stored in a storage tank until returned to the rapid filtration tank. Item 3. The method for washing filtered sand according to Item 2. ( 4 ) 汚れを除去した前記濾過砂を、 該濾過砂を吸い取った前記逆流洗浄時にお ける逆流洗浄が終了する前に戻すことを特徴とする請求の範囲第 1項または第 2 項記載の濾過砂洗浄方法。  (4) The filtration according to claim 1 or 2, wherein the filtered sand from which the dirt has been removed is returned before the backwashing in the backwashing in which the filtered sand is sucked is completed. Sand washing method. ( 5 ) 前記濾過砂の吸取り、 洗浄、 戻しの工程が前記逆流洗浄時に連続して行わ れることを特徴とする請求の範囲第 4項記載の濾過砂洗浄方法。  (5) The method according to claim 4, wherein the steps of sucking, washing, and returning the filtered sand are performed continuously during the backwashing. ( 6 ) 前記貯留槽に、 貯留された濾過砂が空気と触れないように水あるいは酸化 剤を含んだ水を入れておくことを特徴とする請求の範囲第 3項記載の濾過砂洗浄 方法。 (6) The method according to claim 3, wherein the storage tank is filled with water or water containing an oxidizing agent so that the stored filter sand does not come into contact with air. ( 7 ) 濾過砂により水の浄化を行う急速濾過池の逆流洗浄時に該急速濾過池から 所定量の濾過石少を吸い取り、 該吸い取った濾過砂を砂洗浄装置に供給し、 該砂洗 浄装置によつて前記濾過砂の汚れを除去し、 該汚れを除去した濾過砂を貯留槽に 貯留し、 該貯留しておいた濾過砂を前記急速濾過池とは異なる急速濾過池の逆流 洗浄時に該急速濾過池に戻し、 前記濾過砂の吸取り、 洗浄、 貯留、 戻しの工程を 繰り返して複数の急速濾過池内の濾過砂を洗浄することを特徴とする濾過砂洗浄 方法。 (7) A predetermined amount of filter stones is sucked from the rapid filtration pond at the time of backwashing of the rapid filtration pond for purifying water with the filter sand, and the sucked filter sand is supplied to a sand washing device, and the sand washing device is provided. Thus, the filter sand is removed from the filter sand, and the filter sand from which the filter sand is removed is stored in a storage tank. A method for cleaning filtered sand, comprising returning to a rapid filtration tank and repeating the steps of sucking, washing, storing, and returning the filtered sand to filter sand in a plurality of rapid filtration ponds. ( 8 )前記各工程の繰り返しをシーケンス制御により自動的に行うことを特徴と する請求の範囲第 1項から第 7項いずれか 1項記載の濾過砂洗浄方法。  (8) The filtered sand cleaning method according to any one of claims 1 to 7, wherein the repetition of each step is automatically performed by sequence control. ( 9 ) 前記急速濾過池内の前記濾過砂を吸い取る位置から離れた位置に前記汚れ を除去した濾過砂を戻すことを特徴とする請求の範囲第 1項から第 8項のいずれ か 1項記載の濾過砂洗浄方法。  (9) The filter sand according to any one of claims 1 to 8, wherein the filter sand from which the dirt has been removed is returned to a position in the rapid filtration tank that is away from a position where the filter sand is sucked. Filter sand washing method. ( 1 0 ) 前記濾過砂を吸い取る位置を、 濾過砂を吸い取る毎に移動させることを 特徴とする請求の範囲第 1項から第 9項いずれか 1項記載の濾過砂洗浄方法。 (10) The filtered sand cleaning method according to any one of claims 1 to 9, wherein a position where the filtered sand is sucked is moved every time the filtered sand is sucked. ( 1 1 ) 前記汚れを除去した濾過砂を戻す位置を、 濾過砂を戻す毎に移動させる ことを特徴とする請求の範囲第 1項から第 1 0項いずれか 1項記載の濾過砂洗浄 方法。 (11) The filtered sand cleaning method according to any one of claims 1 to 10, wherein a position to return the filtered sand from which the dirt has been removed is moved every time the filtered sand is returned. . ( 1 2 ) 前記濾過砂の吸取りを、 前記急速濾過池の砂利層の表面に不睦を形成し ない大きさの吸引力で行うことを特徴とする請求の範囲第 1項から第 1 1項いず れか 1項記載の濾過砂洗浄方法。  (12) The suction of the filtered sand is performed with a suction force having a magnitude that does not cause discomfort on the surface of the gravel layer of the rapid filtration tank. The method for washing filtered sand according to any one of the preceding claims. ( 1 3 ) 急速濾過池と、 該急速濾過池から濾過砂を吸い取る手段と、 吸い取った 該濾過砂を洗浄する砂洗浄装置と、 該砂洗浄装置から前記急速濾過池へ汚れを除 去した濾過砂を戻す手段とを備えてなることを特徴とする濾過砂洗浄システム。 (13) A quick filtration pond, means for sucking filtered sand from the quick filtration pond, a sand washing device for washing the sucked filtered sand, and filtration for removing dirt from the sand washing device to the quick filtration pond. And a means for returning the sand. ( 1 4 ) 前記砂洗浄装置で汚れを除去した濾過砂を前記急速濾過池へ戻す前に貯 留する貯留槽をさらに備えたものであることを特徴とする請求の範囲第 1 3項記 載の濾過砂洗浄システム。 (14) The storage device according to claim 13, further comprising a storage tank for storing the filtered sand from which dirt has been removed by the sand washing device before returning the filtered sand to the rapid filtration tank. Filter sand washing system. ( 1 5 ) 前記貯留槽が、 該貯留槽内の濾過砂が空気と触れないように該貯留槽内 に水を供給する手段を備えたものであることを特徴とする請求の範囲第 1 4項記 載に濾過砂洗浄システム。 ( 1 6 )前記急速濾過池を複数備えていることを特徴とする請求の範囲第 1 3項、 第 1 4項または第 1 5填記載の濾過砂洗浄システム。 (15) The storage tank according to claim 14, wherein the storage tank is provided with a unit for supplying water into the storage tank so that filtered sand in the storage tank does not come into contact with air. Filter sand washing system as described. (16) The filter sand washing system according to any one of claims 13 to 14, wherein the rapid filtration pond is provided in plurality. ( 1 7 ) 前記濾過砂洗浄システムが、 前記急速濾過池から濾過砂を吸い取る工程 と前記砂洗浄装置で濾過砂を洗浄する工程と前記急速濾過池へ汚れを除去した濾 過砂を戻す工程の少なくとも 3工程、 または前記急速濾過池から濾過砂を吸い取 る工程と前記砂洗浄装置で濾過砂を洗浄する工程と洗浄した濾過砂を貯留槽で貯 留する工程と前記急速濾過池へ汚れを除去した濾過砂を戻す工程の少なくとも 4 工程をシーケンス制御により自動的に行う制御手段を備えたものであることを特 徴とする請求の範囲第 1 3項から第 1 6項いずれか 1項記載の濾過砂洗浄システ ム。 .  (17) The filter sand washing system includes a step of sucking filter sand from the rapid filtration tank, a step of washing the filter sand with the sand washing device, and a step of returning the filtered sand from which dirt has been removed to the rapid filtration tank. At least three steps, a step of sucking filter sand from the rapid filtration tank, a step of washing the filter sand with the sand washing device, a step of storing the washed filter sand in a storage tank, and a step of removing dirt to the rapid filtration tank. The method according to any one of claims 13 to 16, further comprising control means for automatically performing at least four steps of returning the removed filtered sand by sequence control. Filter sand washing system. . ( 1 8 ) 前記急速濾過池から濾過砂を吸い取る手段と、 前記急速濾過池へ汚れを 除去した砂を戻す手段が、 前記急速濾過池の互いに離れた位置に設けられている ことを特徴とする請求の範囲第 1 3項から第 1 7項いずれか 1項記載の濾過砂洗 浄システム。  (18) The means for sucking the filtered sand from the rapid filtration pond and the means for returning the sand from which dirt has been removed to the rapid filtration pond are provided at positions separated from each other in the rapid filtration pond. The filtration sand cleaning system according to any one of claims 13 to 17. ( 1 9 ) 前記急速濾過池から濾過砂を吸い取る手段と、 前記急速濾過池へ汚れを 除去した砂を戻す手段の少なくとも一方が移動可能に設けられていることを特徴 とする請求の範囲第 1 3項から第 1 8項いずれか 1項記載の濾過 洗浄システム。 (19) At least one of a means for sucking filtered sand from the rapid filtration pond and a means for returning sand from which dirt has been removed to the rapid filtration pond is movably provided. Item 19. The filtration and washing system according to any one of Items 3 to 18. ( 2 0 ) 前記砂洗浄装置が、 砂とともに洗浄水を貯留する洗浄槽と、 該洗浄槽内 でほぼ鉛直な軸の回りに回転するスクリューコンペァと、 該スクリューコンベア を、 前記洗浄水の水面下にある前記スクリューコンペァの下部において該スクリ ユーコンペアの回転により前記砂と前記洗浄水を上昇させるとともに該洗浄水を 介在させた前記砂同士の接触により該砂の汚れを除去し、 前記洗浄水の水面上に ある前記スクリューコンベアの上部において前記砂を前記スクリューコンベア上 で流動させて、 汚泥を含む水をわずかに含む前記砂同士の接触によって該砂の汚 れを除去するような速度で回転させる手段と、 上昇させた該砂を前記スクリュー コンペアの下部まで下降させ、 再び該スクリユーコンペアで上昇させる循環手段 とからなるものであることを特徴とする請求の範囲第 1 3項から第 1 9項いずれ か 1項記載の濾過砂洗浄システム。 (20) The sand washing device comprises: a washing tank for storing washing water together with sand; a screw conveyor rotating around a substantially vertical axis in the washing tank; The lower part of the screw conveyer raises the sand and the washing water by rotating the screw compare, and removes dirt from the sand by contact between the sands with the washing water interposed therebetween. The sand is made to flow on the screw conveyor at the upper part of the screw conveyor on the surface of the water, at such a speed that the sand is removed by contact between the sands containing a small amount of water containing sludge. Means for rotating, and circulating means for lowering the raised sand to the lower part of the screw compare and raising the sand again with the screw compare. The filtered sand washing system according to any one of claims 13 to 19, characterized in that the filtered sand washing system is characterized in that:
PCT/JP2000/007764 2000-11-06 2000-11-06 Filter sand washing method and its system Ceased WO2002036239A1 (en)

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KR1020037006174A KR100543150B1 (en) 2000-11-06 2000-11-06 Filtration sand cleaning method and system
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US11/600,786 US20070113870A1 (en) 2000-11-06 2006-11-17 Method of cleansing filtration media and system therefor
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CN102921231A (en) * 2012-11-13 2013-02-13 江苏科技大学 Fully-automatic back-flushing type self-cleaning filter

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JPS5678684A (en) * 1979-11-30 1981-06-27 Ebara Infilco Co Ltd Organismic treatment for sewage
JPS62186911A (en) * 1986-02-10 1987-08-15 Katsuo Nakayama Sand filter
US5401397A (en) * 1993-04-15 1995-03-28 Automatic Control Filter system for a liquid stream with automatic rapid back flush capability
JP2000229205A (en) * 1999-02-05 2000-08-22 Japan Organo Co Ltd Upflow type continuous filter

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Publication number Priority date Publication date Assignee Title
JPS5678684A (en) * 1979-11-30 1981-06-27 Ebara Infilco Co Ltd Organismic treatment for sewage
JPS62186911A (en) * 1986-02-10 1987-08-15 Katsuo Nakayama Sand filter
US5401397A (en) * 1993-04-15 1995-03-28 Automatic Control Filter system for a liquid stream with automatic rapid back flush capability
JP2000229205A (en) * 1999-02-05 2000-08-22 Japan Organo Co Ltd Upflow type continuous filter

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CN102921231A (en) * 2012-11-13 2013-02-13 江苏科技大学 Fully-automatic back-flushing type self-cleaning filter

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