JPH05192512A - Water purifying plant - Google Patents
Water purifying plantInfo
- Publication number
- JPH05192512A JPH05192512A JP3012592A JP3012592A JPH05192512A JP H05192512 A JPH05192512 A JP H05192512A JP 3012592 A JP3012592 A JP 3012592A JP 3012592 A JP3012592 A JP 3012592A JP H05192512 A JPH05192512 A JP H05192512A
- Authority
- JP
- Japan
- Prior art keywords
- water
- tank
- cylinder
- sedimentation
- pumping
- 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
Landscapes
- Separation Of Suspended Particles By Flocculating Agents (AREA)
Abstract
Description
【0001】[0001]
【産業上の利用分野】この発明は河川などから取水し、
上水とする為の淨水を目的とした淨水装置に関する。[Industrial field of application] This invention takes water from rivers,
The present invention relates to a fresh water device intended for fresh water for use as clean water.
【0002】[0002]
【従来の技術】従来上水を得るには、取水を沈澱池に導
き凝集剤を注入し、水中ポンプ又はプロペラなどで撹拌
して固形物を沈澱させた後、濾過池で濾過し、ついで塩
素消毒した後配水している。2. Description of the Related Art Conventionally, in order to obtain clean water, the intake water is introduced into a settling tank, a coagulant is injected, the solid matter is precipitated by stirring with a submersible pump or a propeller, and then filtered in a filter tank, followed by chlorine. Water is distributed after disinfection.
【0003】[0003]
【発明により解決すべき課題】前記従来の技術によれ
ば、撹拌が不十分、かつ不均等になる為に、凝集剤その
他の添加物が不均等に混合され易く、必要量より多く添
加しなければならないのみならず沈澱(凝集)効率など
が悪くなるおそれもあった。また水中ポンプ又はプロペ
ラを利用した撹拌においては、水流が一定し、撹拌効率
も悪くなるおそれがあったので、複数の撹拌器を必要と
したり、機械撹拌の為に、腐蝕、発錆、摩耗などの諸欠
点を生じるおそれがあった。According to the above-mentioned prior art, since the agitation is insufficient and uneven, the coagulant and other additives are likely to be unevenly mixed, and more than the required amount must be added. Not only does this have to be done, but the precipitation (aggregation) efficiency may also deteriorate. In addition, in agitation using a submersible pump or propeller, the water flow was constant and there was a risk that the agitation efficiency would deteriorate, so multiple agitators were required, and mechanical agitation required corrosion, rusting, abrasion, etc. There was a possibility that various defects of
【0004】[0004]
【課題を解決する為の手段】然るにこの発明は、沈澱池
に間欠空気揚水筒を設置したので、水中モータ又はプロ
ペラなどを利用した場合と異なり、水を上下対流させて
全槽循環撹拌すると共に、前記揚水の為には機械部分と
か、シヤフトその他水中で回転する物が一切使用され
ず、その上空気を動力に用いるので、保修は不必要とな
り、かつ自浄作用により、揚水筒の清掃なども不必要に
なるなど、前記従来の問題点を悉く改善したのである。However, in the present invention, since the intermittent air pumping cylinder is installed in the settling basin, unlike the case where an underwater motor or propeller is used, water is vertically convected to circulate and stir the whole tank. However, for pumping water, no mechanical parts, shafts or other objects that rotate in water are used, and since air is used as power, maintenance is unnecessary, and due to the self-cleaning function, cleaning of the pump cylinder is also possible. The above problems of the prior art, such as unnecessaryness, have been alleviated.
【0005】即ちこの発明は、沈澱池中に間欠空気揚水
筒を設置したことを特徴とする淨水装置である。また沈
澱池は、一側を着水槽に連結し、他側を濾過槽に連結し
たものである。次に沈澱池は、PH調整槽、疑集剤混入
槽及び固形物分離槽を順次連結して構成したものであ
る。更にPH調整槽には、石灰溶解槽を付設すると共
に、該石灰溶解槽中に間欠空気揚水筒を設置したもので
ある。That is, the present invention is a fresh water system characterized in that an intermittent air pumping cylinder is installed in a sedimentation basin. The sedimentation basin has one side connected to a water tank and the other side connected to a filtration tank. Next, the sedimentation basin is constituted by sequentially connecting a pH adjusting tank, a collecting agent mixing tank, and a solid matter separating tank. Further, the pH adjusting tank is provided with a lime dissolving tank and an intermittent air pumping cylinder installed in the lime dissolving tank.
【0006】前記のように、この発明よれば、間欠空気
揚水筒を用いるので、槽内の揚水筒設置場所において上
昇流を生起し、ついで拡散流に方向変換される。このよ
うな水流が間欠的に生起される為に、各部水流は定常流
となるおそれなく、しかも水中へ気泡がでる都度撹拌す
るので、凝集剤その他の添加物を、揚水筒の筒部に与え
ることにより自動的に混合して拡散される。またこの発
明においては、石灰溶解槽を付設することによって、高
濃度石灰水を造り、その適量をPH調整槽に自動給送す
ることにより、PHを自動的に調整することができる。As described above, according to the present invention, since the intermittent air pumping cylinder is used, an ascending flow is generated at the location where the pumping cylinder is installed in the tank, and then the direction is changed to the diffusion flow. Since such a water flow is generated intermittently, there is no risk that the water flow in each part will become a steady flow, and since the water is agitated each time bubbles form in the water, a flocculant and other additives are applied to the cylinder part of the pumping cylinder. As a result, they are automatically mixed and diffused. Further, in the present invention, the pH can be automatically adjusted by providing a lime dissolving tank to make high-concentration lime water and automatically feeding an appropriate amount of the lime water to the PH adjusting tank.
【0007】前記において、揚水筒は、円筒形、又は逆
錐形であるが何れにしても内部を気泡と水とが、平均流
速1m/sec 前後で移動するので、円筒等の内側は常時
清掃状態を保ち異物(藻類、有機無機固形物、微生物)
が付着するおそれはない。従って原則的に清掃も不必要
である。更に揚水筒も、空気室も共に中空であって、機
械的回転体その他は一切用いられていないので、故障を
生じるおそれはない。また万一故障を生じた場合には、
揚水状態で目視により容易に発見できると共に、故障部
分の発見と、改善もきわめて容易であり、送水に支障を
生じるおそれはない。従って送水継続のまゝ修理その他
の改善作業を行うことができる。In the above description, the pumping cylinder has a cylindrical shape or an inverted pyramidal shape, but in any case, since bubbles and water move at an average flow velocity of about 1 m / sec, the inside of the cylinder or the like is always cleaned. Foreign substances (algae, organic-inorganic solids, microorganisms) that maintain the condition
There is no risk of adhesion. Therefore, in principle, cleaning is unnecessary. Furthermore, since both the pumping cylinder and the air chamber are hollow and no mechanical rotating body or the like is used, there is no possibility of causing a failure. In case of a failure,
It can be easily found by visual inspection in the pumped state, and it is also very easy to find and improve the faulty part, and there is no risk of impeding water supply. Therefore, it is possible to carry out repairs and other improvement work while continuing water supply.
【0008】[0008]
【作用】この発明によれば、沈澱槽に間欠空気揚水筒を
設置したので、沈澱槽内に上下循環水流を生起して全水
を拡販すると共に、添加剤などを均等に拡散させる。According to the present invention, since the intermittent air pumping cylinder is installed in the settling tank, the vertical circulating water flow is generated in the settling tank to expand the sales of all the water and evenly diffuse the additives.
【0009】また揚水筒は自淨作用によって常時同一能
力を保たれる。例えば揚水筒内の抵抗増加とか、断面積
減少など揚水能力を低下させるような原因を生じるおそ
れがない。Further, the pumping cylinder can always maintain the same ability by the self-sustaining action. For example, there is no fear that causes such as an increase in the resistance in the pumping cylinder or a decrease in the cross-sectional area will reduce the pumping capacity.
【0010】[0010]
【実施例1】この発明の実施例を図1、2、3、4につ
いて説明する。沈澱池1の一側に連通管2を介して着水
槽3を連結し、沈澱池1の他側に連通管2aを介して濾
過槽4を連結し、濾過槽4には、夫々連通管5、6を介
して塩素注入槽7と配水池8とを順次連結する(図
1)。前記沈澱池1は、仕切壁9、10、11、12、
13、14により、PH調整槽15、凝集槽16と沈澱
槽17a、17bにより構成されている。前記濾過槽4
には、砂層18a、18bが設けられ、沈澱池1からの
上澄水はこれらの層により濾過される。Embodiment 1 An embodiment of the present invention will be described with reference to FIGS. The landing tank 3 is connected to one side of the sedimentation tank 1 via the communication pipe 2, and the filtration tank 4 is connected to the other side of the sedimentation tank 1 via the communication pipe 2a. , 6 are used to sequentially connect the chlorine injection tank 7 and the distribution reservoir 8 (FIG. 1). The settling basin 1 includes partition walls 9, 10, 11, 12,
13 and 14, a pH adjusting tank 15, a flocculating tank 16 and settling tanks 17a and 17b. The filtration tank 4
Sand layers 18a, 18b are provided in the bed, and the supernatant water from the settling basin 1 is filtered by these layers.
【0011】またPH調整槽15と、凝集剤層16のほ
ゞ中央部には、間欠空気揚水装置19が設置されてお
り、各槽内の水を矢示20、21、22、23、24、
25のように上下対流させることによりPH調整剤(例
えば高濃度石灰水)及び高分子凝集剤を混合している。
前記に使用する間欠空気揚水装置19は、色々の構造が
あるが、一例として図3につき、その構造と動作を説明
する。Further, an intermittent air pumping device 19 is installed in the PH adjusting tank 15 and approximately at the center of the coagulant layer 16, and the water in each tank is indicated by arrows 20, 21, 22, 23, 24. ,
The pH adjuster (for example, high-concentration lime water) and the polymer coagulant are mixed by causing convection in the vertical direction like 25.
The intermittent air pumping device 19 used above has various structures, and the structure and operation will be described with reference to FIG. 3 as an example.
【0012】即ち揚水装置19は基筒26の外側に空気
室27を嵌装する。前記空気室27は、基筒26の外側
へ所定間隙を設けて、内筒28、仕切筒29及び外筒3
0を順次嵌装し、前記内筒28の上端を基筒26との間
を頂板32で閉鎖し、前記基筒壁と内筒28及び仕切筒
29の下端を底板33で閉鎖し、前記内筒壁と、仕切筒
29及び外筒30の上端を頂板34で閉鎖し、前記基筒
26の上部、内筒28、の下部及び仕切筒29の上部
へ、夫々連通孔35、36、37、を設けて構成してあ
る。また頂板32へ加圧空気の給送ホース38端を連結
する。前記基筒26の下端鍔39に索条40の一端を固
定し、索条40の他端に重錘41を連結して、重錘41
を沈澱池1の底上に設置すれば、揚水装置19を安定し
て設置することができる。前記基筒26の上端には、漏
斗状の外槽42の基端を連結し、前記外槽42内へ相似
外形の逆円錐状の中空体43を嵌合し、前記外槽42の
内壁と、前記中空体43との間へ、数本の仕切板44、
44を放射状、かつ等間隔に介装して固着し、外槽42
の内壁、中空体43の外壁及び二本の仕切板44、44
で揚水路45を形成している。前記揚水路45は、下部
から上部に向って漏斗状(側面)に拡がっているので、
外槽42の内壁と、中空体43の外壁との間隔を均一に
すれば、揚水路45は上方程断面積が大きなるが、前記
間隙の調整により断面積をほゞ一定にすることもでき
る。前記実施例において、給送ホース38から、矢示4
6のように加圧空気を圧送すると、加圧空気は、頂板3
2の内側から溜り、空気室27内の水位を矢示47のよ
うに押し下げる。前記水位34が連通孔36に達する
と、空気室27内の空気は、連通孔35、36、37を
矢示48、49、50のように通過し、気泡57となっ
て基筒1の上部へ放出され、ついで中空体43の下端頂
51で分けられて、各揚水路45、を矢示52のように
上昇し、その上端から斜上方へ、矢示53のように放出
され、矢示20、23の方向へ拡散する(図1、図2、
図3)。そこで図1中、矢示20、21、22、23、
24、25のように水を対流循環させる。That is, in the water pumping device 19, an air chamber 27 is fitted outside the base cylinder 26. The air chamber 27 is provided with a predetermined gap outside the base cylinder 26, and has an inner cylinder 28, a partition cylinder 29 and an outer cylinder 3.
0 is sequentially fitted, the upper end of the inner cylinder 28 is closed with a top plate 32 between the inner cylinder 28 and the base cylinder 26, and the lower ends of the base cylinder wall, the inner cylinder 28 and the partition cylinder 29 are closed with a bottom plate 33. The cylinder wall and the upper ends of the partition cylinder 29 and the outer cylinder 30 are closed by a top plate 34, and communication holes 35, 36, 37 are provided to the upper part of the base cylinder 26, the lower part of the inner cylinder 28, and the upper part of the partition cylinder 29, respectively. Is provided. Also, the end of the pressurized air feeding hose 38 is connected to the top plate 32. One end of the rope 40 is fixed to the lower end flange 39 of the base cylinder 26, and the weight 41 is connected to the other end of the rope 40.
If the pump is installed on the bottom of the settling basin 1, the pumping device 19 can be installed stably. The base end of the funnel-shaped outer tub 42 is connected to the upper end of the base cylinder 26, and the inverted conical hollow body 43 having a similar external shape is fitted into the outer tub 42 to form an inner wall of the outer tub 42. , A plurality of partition plates 44 between the hollow body 43,
The outer tubs 42 are fixed by arranging 44 radially and equidistantly.
Inner wall, the outer wall of the hollow body 43, and the two partition plates 44, 44
Forms a pumping channel 45. Since the pumping channel 45 extends from the lower part to the upper part in a funnel shape (side surface),
If the space between the inner wall of the outer tub 42 and the outer wall of the hollow body 43 is made uniform, the cross-sectional area of the pumping channel 45 becomes larger toward the upper side, but the cross-sectional area can be made almost constant by adjusting the gap. .. In the above-described embodiment, from the feeding hose 38, the arrow 4
When the pressurized air is sent under pressure as in 6, the pressurized air is
It collects from the inside of 2 and pushes down the water level in the air chamber 27 as shown by the arrow 47. When the water level 34 reaches the communication hole 36, the air in the air chamber 27 passes through the communication holes 35, 36 and 37 as indicated by arrows 48, 49 and 50, and becomes air bubbles 57 to form an upper portion of the base cylinder 1. And then divided by the lower end apex 51 of the hollow body 43 to rise in each pumping channel 45, as shown by the arrow 52, and obliquely upward from its upper end, as shown by the arrow 53, Diffuses in the directions of 20 and 23 (Fig. 1, Fig. 2,
(Figure 3). Therefore, in FIG. 1, arrows 20, 21, 22, 23,
The water is convectively circulated like 24 and 25.
【0013】前記実施装置において、河川などより着水
槽3に矢示54のように送り込まれた水は、調整槽15
において、例えば高濃度石灰水を揚水装置19の基筒2
6のホース31へ矢示56のように送り込み、揚水に混
入する。この揚水は、前記のように、矢示20、21、
22、23、24、25のように循環するので、短期
(容量により異なるが、例えば水量1000〜5000
トンでは1〜2日以内)に均一に混合できる。この水
は、PH7.0付近になって矢示58のように凝集槽1
6に入り、揚水装置19によって凝集剤を混合拡散する
ので、水に浮游した固形粒子は適度に団粒化し、矢示5
9、60、61、62、63のように沈澱槽17a、1
7bを流動通過すれば、固形物は屈曲流動の間に浮力が
なくなって沈澱し、その上澄水は、矢示64のように連
通管2aを介し、濾過槽4に入り、砂層18a、18b
で濾過された後、矢示65のように連通管5を経て塩素
注入槽7に入り、こゝで適量の塩素を注入された後、矢
示66のように連通管6を経て配水池8に入り、矢示6
7のように送水管68から送水される。このようにして
前記のように効率よく連続淨水されるのである。In the above-described apparatus, the water sent from the river or the like to the water landing tank 3 as shown by an arrow 54 is the adjusting tank 15
In, for example, high-concentration lime water
It is sent to the hose 31 of No. 6 as shown by the arrow 56 and mixed in the pumped water. This pumped water is, as described above, the arrow 20, 21,
Since it circulates like 22, 23, 24, 25, it is a short term (it depends on the capacity, but the water amount is, for example, 1000 to 5000).
Tons can be mixed uniformly within 1-2 days). This water is around pH 7.0, and as shown by arrow 58,
6, the coagulant is mixed and diffused by the pumping device 19, so that the solid particles suspended in the water are appropriately aggregated, and the arrow 5
Settling tanks 17a, 1 like 9, 60, 61, 62, 63
When flowing through 7b, the solid matter loses its buoyancy during the bending flow and precipitates, and the supernatant water enters the filtration tank 4 through the communication pipe 2a as indicated by the arrow 64, and the sand layers 18a, 18b.
After being filtered with, the chlorine injection tank 7 enters through the communication pipe 5 as shown by the arrow 65, and an appropriate amount of chlorine is injected therein, and then the distribution reservoir 8 passes through the communication pipe 6 as shown by the arrow 66. Enter, arrow 6
Water is supplied from the water supply pipe 68 as in 7. In this way, continuous continuous water supply is achieved as described above.
【0014】[0014]
【実施例2】前記実施例1における高濃度石灰水の製造
装置を図4、5、6に基づいて説明する。外槽55の内
側へ、所定間隔を保って内筒69を設置し、前記内筒6
9の底板70上へ間欠空気揚水装置71を設置する。ま
た内筒69の外側へ所定間隔をおいて多孔筒72を遊嵌
し、多孔筒72と内筒69との下部を塞板73で閉塞
し、内筒69と多孔筒72との間に消石灰74を収容す
る。前記多孔筒72は、パンチングメタル筒72aの外
側に網筒72bを嵌装してある。前記外槽55の一側外
部には循環槽75が設けられ、循環槽75の外壁には、
排水口76と、給送口77が上下に設けられ、前記外槽
55との間の壁には連通孔78、79が上下に設けら
れ、外槽55の他側上部には給水口80が設けられて石
灰水の製造装置84を構成する(図4)。図中81は給
気ホース、82、83は蓋板である。[Embodiment 2] An apparatus for producing high-concentration lime water in Embodiment 1 will be described with reference to FIGS. The inner cylinder 69 is installed inside the outer tank 55 at a predetermined interval, and the inner cylinder 6 is
An intermittent air pumping device 71 is installed on the bottom plate 70 of No. 9. The perforated cylinder 72 is loosely fitted to the outside of the inner cylinder 69 at a predetermined interval, the lower portions of the perforated cylinder 72 and the inner cylinder 69 are closed by a closing plate 73, and slaked lime is provided between the inner cylinder 69 and the perforated cylinder 72. 74 are accommodated. The perforated cylinder 72 has a mesh cylinder 72b fitted outside the punching metal cylinder 72a. A circulation tank 75 is provided outside one side of the outer tank 55, and an outer wall of the circulation tank 75 is
A drainage port 76 and a feed port 77 are provided above and below, a communication hole 78, 79 is provided above and below in a wall between the outer tub 55, and a water feed port 80 is provided on the other side upper part of the outer tub 55. It is provided and constitutes the lime water manufacturing apparatus 84 (FIG. 4). In the figure, 81 is an air supply hose, and 82 and 83 are cover plates.
【0015】次に記実施例について、その使用法を説明
する。前記製造装置84の内筒69と、多孔筒72の間
に適量の消石灰74を収容した後、給水口80から矢示
85のように給水する(通常PH改善すべき水を使用す
る)。ついで給気ホース81から矢示86のように加圧
空気を、揚水装置71の空気室87に送入する。前記空
気室87は、図6のように、揚水筒88の下部に所定間
隔を保って内筒89を遊嵌し、該内筒89の外側へ相当
の間隔を保って外筒90を遊嵌し、外筒90と、内筒8
9との間に仕切筒91を遊嵌し、外筒90、仕切筒91
と内筒89の外壁までの間を頂板92で閉塞し、揚水筒
88の外壁、内筒89の下端と、仕切筒91の下端とを
底板93で閉塞し、仕切筒91の上部、内筒89の下部
及び内筒89の上部と対向する揚水筒88の壁には連通
孔95、96、97が夫々穿設してある。前記における
内筒89の上端と、揚水筒88の外壁との間にも頂板9
4で閉塞され、空気室87が構成してある。Next, the usage of the embodiment will be described. After accommodating an appropriate amount of slaked lime 74 between the inner cylinder 69 of the manufacturing apparatus 84 and the perforated cylinder 72, water is supplied from the water supply port 80 as shown by an arrow 85 (usually, water for which PH should be improved is used). Then, pressurized air is supplied from the air supply hose 81 to the air chamber 87 of the water pumping device 71 as shown by an arrow 86. As shown in FIG. 6, in the air chamber 87, an inner cylinder 89 is loosely fitted to a lower portion of a pumping cylinder 88 at a predetermined interval, and an outer cylinder 90 is loosely fitted to the outside of the inner cylinder 89 at a considerable distance. Then, the outer cylinder 90 and the inner cylinder 8
A partition cylinder 91 is loosely fitted between the outer cylinder 90 and the partition cylinder 91.
And the outer wall of the inner cylinder 89 is closed by a top plate 92, the outer wall of the pumping cylinder 88, the lower end of the inner cylinder 89 and the lower end of the partition cylinder 91 are closed by a bottom plate 93, and the upper part of the partition cylinder 91, the inner cylinder. Communication holes 95, 96, 97 are formed in the wall of the pumping cylinder 88 facing the lower part of 89 and the upper part of the inner cylinder 89, respectively. The top plate 9 is also provided between the upper end of the inner cylinder 89 and the outer wall of the pumping cylinder 88.
4, and an air chamber 87 is formed.
【0016】前記において、空気室87内へ加圧空気が
送入されると、加圧空気の送入量に比例して空気室87
内の水位が下降する。水位が図6中鎖線の位置に達する
と、空気室87内の空気は、矢示98、99、100の
ように移動して揚水筒88内へ入り、大きな気泡101
となり、矢示102のように上昇する。In the above, when the pressurized air is fed into the air chamber 87, the air chamber 87 is proportional to the amount of the pressurized air fed.
The water level inside falls. When the water level reaches the position shown by the chain line in FIG. 6, the air in the air chamber 87 moves as indicated by arrows 98, 99, 100 into the pumping cylinder 88, and the large bubbles 101
And rise as shown by arrow 102.
【0017】前記のように気泡101が上昇すると、そ
の上昇につれて、揚水筒88の下部から矢示103のよ
うに水を吸い上げるので、水は揚水筒88内を上昇し、
矢示104、105、106、107、108、109
のように下降する。この際に消石灰に接触し、アルカリ
水(消石灰水)となる。また一部の水は循環槽55内を
矢示110、111、112のように下降する。そこで
給送口77にホース31を連結すれば、ホース31を介
して高アルカリ水(消石灰水)が矢示56のように基筒
26内へ供給される。When the bubble 101 rises as described above, as it rises, water is sucked up from the lower part of the pumping cylinder 88 as shown by the arrow 103, so that the water rises in the pumping cylinder 88,
Arrows 104, 105, 106, 107, 108, 109
To descend. At this time, it contacts slaked lime and becomes alkaline water (slaked lime water). Further, a part of the water descends in the circulation tank 55 as indicated by arrows 110, 111, 112. Therefore, if the hose 31 is connected to the feed port 77, the highly alkaline water (slaked lime water) is supplied into the base cylinder 26 through the hose 31 as shown by the arrow 56.
【0018】前記のように、揚水装置71で水を循環す
れば、水は不定常流となって消石灰に接触するので、効
率よく溶解し、高アルカリ水を容易に製造することがで
きる。As described above, when water is circulated in the pumping device 71, the water becomes an unsteady flow and comes into contact with slaked lime, so that it is efficiently dissolved and high alkaline water can be easily produced.
【0019】[0019]
【発明の効果】この発明は、沈殿池中に間欠空気揚水筒
を設置したので、沈澱池の水を上下循環対流し、PH調
整とか、凝集剤混入とかを効率よく行い得る効果があ
る。EFFECTS OF THE INVENTION Since the intermittent air pumping cylinder is installed in the sedimentation tank, the present invention has an effect that water in the sedimentation tank can be vertically circulated and convected to efficiently adjust the pH and mix the coagulant.
【図1】この発明の実施例の縦断正面図。FIG. 1 is a vertical sectional front view of an embodiment of the present invention.
【図2】同じく一部平面図。FIG. 2 is a partial plan view of the same.
【図3】同じく揚水装置の縦断拡大正面図。FIG. 3 is also an enlarged vertical sectional front view of the water pumping device.
【図4】同じく消石灰溶解槽の縦断正面図。FIG. 4 is a vertical sectional front view of the slaked lime dissolution tank.
【図5】同じく平面図。FIG. 5 is a plan view of the same.
【図6】同じく図4に用いた揚水装置の縦断面図。FIG. 6 is a vertical cross-sectional view of the water pumping device also used in FIG.
1 沈殿池 2、2a、5、6 連通管 3 着水槽 4 濾過槽 7 塩素注入槽 8 配水池 15 PH調整槽 16 凝集槽 17a、17b 沈殿槽 18 砂層 19 揚水装置 26 基筒 27 空気室 28 内筒 29 仕切筒 30 外筒 38 給送ホース 42 外槽 43 中空体 44 仕切板 57 気泡 68 送水管 69 内筒 71 揚水装置 72 多孔筒 74 消石灰 75 循環槽 81 給気ホース 84 消石灰水の製造装置 87 空気室 88 揚水筒 101 気泡 1 settling basin 2, 2a, 5, 6 communication pipe 3 landing tank 4 filtration tank 7 chlorine injection tank 8 distribution tank 15 PH adjusting tank 16 coagulation tank 17a, 17b sedimentation tank 18 sand layer 19 pumping device 26 base cylinder 27 air chamber 28 inside Cylinder 29 Partition Cylinder 30 Outer Cylinder 38 Feed Hose 42 Outer Tank 43 Hollow Body 44 Partition Plate 57 Bubble 68 Water Pipe 69 Inner Cylinder 71 Pumping Device 72 Perforated Cylinder 74 Slaked Lime 75 Circulation Tank 81 Air Supply Hose 84 Slaked Lime Water Manufacturing Device 87 Air chamber 88 Pumping pipe 101 Air bubbles
Claims (5)
とを特徴とする淨水装置。1. A fresh water system comprising an intermittent air pumping cylinder installed in a sedimentation basin.
を濾過槽に連結した請求項1記載の淨水装置。2. The water purifier according to claim 1, wherein one side of the settling basin is connected to the water receiving tank and the other side is connected to the filtration tank.
び固形物分離槽を順次連結して構成した請求項1記載の
淨水装置。3. The water purifier according to claim 1, wherein the settling basin comprises a pH adjusting tank, a collecting agent mixing tank, and a solids separating tank, which are sequentially connected.
と共に、該石灰溶解槽内に間欠空気揚水筒を設置した請
求項3記載の淨水装置4. The water purifier according to claim 3, wherein the pH adjusting tank is provided with a lime dissolving tank, and an intermittent air pumping cylinder is installed in the lime dissolving tank.
間欠的に放出する空気室を付設し、筒体の上部を円筒形
又は逆錐形に形成した請求項1又は4記載の淨水装置。5. The intermittent air pumping cylinder according to claim 1 or 4, wherein an air chamber for intermittently discharging air is attached to the lower part of the cylindrical body, and the upper part of the cylindrical body is formed into a cylindrical shape or an inverted cone shape. Fresh water equipment.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP3012592A JPH05192512A (en) | 1992-01-21 | 1992-01-21 | Water purifying plant |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP3012592A JPH05192512A (en) | 1992-01-21 | 1992-01-21 | Water purifying plant |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH05192512A true JPH05192512A (en) | 1993-08-03 |
Family
ID=12295058
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP3012592A Pending JPH05192512A (en) | 1992-01-21 | 1992-01-21 | Water purifying plant |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH05192512A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2012115770A (en) * | 2010-12-01 | 2012-06-21 | Maeda Corp | Turbid water treatment apparatus |
JP2016083593A (en) * | 2014-10-23 | 2016-05-19 | 日本ソリッド株式会社 | Polluted water processing method |
-
1992
- 1992-01-21 JP JP3012592A patent/JPH05192512A/en active Pending
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2012115770A (en) * | 2010-12-01 | 2012-06-21 | Maeda Corp | Turbid water treatment apparatus |
JP2016083593A (en) * | 2014-10-23 | 2016-05-19 | 日本ソリッド株式会社 | Polluted water processing method |
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