Deprecated: The each() function is deprecated. This message will be suppressed on further calls in /home/zhenxiangba/zhenxiangba.com/public_html/phproxy-improved-master/index.php on line 456
JPS6052850B2 - Filtration device and filtration method using the filtration device - Google Patents
[go: Go Back, main page]

JPS6052850B2 - Filtration device and filtration method using the filtration device - Google Patents

Filtration device and filtration method using the filtration device

Info

Publication number
JPS6052850B2
JPS6052850B2 JP52020418A JP2041877A JPS6052850B2 JP S6052850 B2 JPS6052850 B2 JP S6052850B2 JP 52020418 A JP52020418 A JP 52020418A JP 2041877 A JP2041877 A JP 2041877A JP S6052850 B2 JPS6052850 B2 JP S6052850B2
Authority
JP
Japan
Prior art keywords
liquid
filtrate
container
path
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.)
Expired
Application number
JP52020418A
Other languages
Japanese (ja)
Other versions
JPS53105770A (en
Inventor
忠 桐沢
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.)
NIPPON ENBAIRO KOGYO KK
Original Assignee
NIPPON ENBAIRO KOGYO KK
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 NIPPON ENBAIRO KOGYO KK filed Critical NIPPON ENBAIRO KOGYO KK
Priority to JP52020418A priority Critical patent/JPS6052850B2/en
Publication of JPS53105770A publication Critical patent/JPS53105770A/en
Publication of JPS6052850B2 publication Critical patent/JPS6052850B2/en
Expired legal-status Critical Current

Links

Landscapes

  • Filtration Of Liquid (AREA)

Description

【発明の詳細な説明】 本発明は濾過、洗滌工程の能率化を図るとともに準ク
ローズドシスムを構成して濾過装置からの排出物をでき
るだけ減少せしめることを目的とするものであり、濾過
工程により排出される濾波を備蓄し、これを洗滌液とし
て使用し、排出されるj洗滌汚液は圧搾濾過しその濾波
を濾過装置に送通される被処理液側に還送せしめること
を骨子とするものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention aims to improve the efficiency of the filtration and washing processes and reduce the amount of waste discharged from the filtration device as much as possible by configuring a semi-closed system. The main idea is to stockpile filtered water, use it as a washing liquid, press-filtrate the discharged washing sewage, and return the filtered water to the liquid to be treated that is passed through the filtration device. It is.

本発明を図に示す一実施例により説明すれば、1は蓋
1Aを付した密閉可能な容体であり機枠2上に載置され
る。
The present invention will be described with reference to an embodiment shown in the drawings. Reference numeral 1 denotes a sealable container equipped with a lid 1A, which is placed on a machine frame 2.

容体1内には空気抜孔3、洗滌汚液排出管4、原液槽4
Aに連絡するポンプ5を設けた注液管6が連絡する。7
は中空かつ内孔8A1外孔8Bを設けた回転軸であり、
容体1をシールして被処理液と濾液との混合を防ぐ軸受
9,10により容体1内に横方向に支持される。
Inside the container 1, there are an air vent hole 3, a washing sewage discharge pipe 4, and a stock solution tank 4.
A liquid injection pipe 6 equipped with a pump 5 communicates with A. 7
is a rotating shaft that is hollow and has an inner hole 8A1 and an outer hole 8B,
It is laterally supported within the container 1 by bearings 9 and 10 that seal the container 1 and prevent mixing of the liquid to be treated and the filtrate.

回転軸7には中空ソロバン玉状の濾過材7Aが複数個取
付けられ、容体1からの外出部において外筒11に被覆
される。濾過材7Aとしては中空ソロバン玉状の濾材に
濾布を被覆する構成、多孔質な硬質材料それ自体を中空
ソロバン玉状に形成する構成等がとなれる。容体1の直
上部には脚部13Aを介して濾液貯槽13が設置せられ
、濾液貯槽13には回転軸7と外筒11との間の間隙1
2にバルブ13″Bを介して連絡する濾液排出管13B
1および濾液排出管13Bにバルブ13″Cを介して連
絡する洗滌液送通管13Cが合一して連絡せられ、洗滌
液送通管13Cには更にバルブ13″Dを介して排出管
13Dを連絡し、更に外筒11の端部はメカニカルシー
ル14によつてシールせられる。回転軸7根端部はベア
リング軸受け15によつて支持せられ、更にプーリ−1
6が固着せられ、プーリ−16はベルト17を介して駆
動装置18に連絡する。上記装置の他、例えば濾液排出
径路、洗滌液径路は回転軸と別個にしてもよい。上記濾
過機の一個または二個以上を並列せしめ、該濾過機の容
体1の洗滌汚液排出管4を貯液槽4Bに連絡する。
A plurality of filter media 7A in the form of hollow beads are attached to the rotating shaft 7, and are covered with the outer cylinder 11 at the part extending from the container 1. The filtering material 7A may have a structure in which a filter material in the shape of a hollow Soroban bead is covered with a filter cloth, or a structure in which a porous hard material itself is formed in the shape of a hollow Soroban bead. A filtrate storage tank 13 is installed directly above the container 1 via leg portions 13A, and the filtrate storage tank 13 has a gap 1 between the rotating shaft 7 and the outer cylinder 11.
2 via valve 13″B.
1 and the filtrate discharge pipe 13B through a valve 13''C, and the cleaning liquid conveyance pipe 13C is further connected to a discharge pipe 13D through a valve 13''D. Further, the end of the outer cylinder 11 is sealed by a mechanical seal 14. The root end of the rotating shaft 7 is supported by a bearing 15, and is further supported by a pulley 1.
6 is fixed, and the pulley 16 communicates via a belt 17 to a drive 18. In addition to the above device, for example, the filtrate discharge path and the washing liquid path may be separate from the rotating shaft. One or more of the above-mentioned filters are arranged in parallel, and the washing waste liquid discharge pipe 4 of the container 1 of the filter is connected to the liquid storage tank 4B.

貯液槽4Bは更に送液ポンプー21、圧搾濾過装置22
を介して還送管23により原液槽4Aに連絡する。第5
〜9図に示す圧搾濾過装置において、容器31および容
器32は受け環33および受け環33aに間通する枢軸
34によつて相互に枢着され.る。
The liquid storage tank 4B is further equipped with a liquid feeding pump 21 and a compression filtration device 22.
It is connected to the stock solution tank 4A via a return pipe 23. Fifth
In the press filtration apparatus shown in FIGS. 9 to 9, a container 31 and a container 32 are pivotally connected to each other by a receiving ring 33 and a pivot 34 passing through the receiving ring 33a. Ru.

35は間隔板であり、上縁の支枠36の孔37および下
縁の受け環38によつて同様に枢軸34に枢着され、容
器31と容器32との間に介在する。
Reference numeral 35 denotes a spacing plate, which is similarly pivotally connected to the pivot 34 through a hole 37 in a support frame 36 on the upper edge and a receiving ring 38 on the lower edge, and is interposed between the containers 31 and 32.

容器31、容器32は側面、底面ともに内壁31A,3
2A1外壁31B,32Bからなる−ニ重壁で、内壁3
1A,32Aは多孔板または凹凸のあるゴム板よりなり
、更に底部には吐出口31C,32Cが設けられる。間
隔板35にも枠体35Aの両側に多孔板35Bまたは凹
凸のあるゴム板が張設せられている。容器31の一側面
にはボルト杆39,40が枢着せられ、更にU字状の係
合杆41が枢着せられる。容器32の対応する側面には
ボルト39,40を受けるボルト受け39A,40およ
び固定枠42内の保持せられたハンドル43Aを付した
油圧シリンダー43取付けられ、油圧シリンダー43の
ピストン杆44の先端には容器31の係合杆41と係合
する把手45が固設せられる。l かくして容器31は
機台46上に設置せられ、容器31,32の直下には排
出口47Aを設けた受け皿47が配設せしめられる。
The containers 31 and 32 have inner walls 31A and 3 on both side and bottom surfaces.
2A1 consists of outer walls 31B and 32B - double wall, inner wall 3
1A and 32A are made of perforated plates or rubber plates with unevenness, and discharge ports 31C and 32C are provided at the bottom. The spacer plate 35 is also provided with perforated plates 35B or uneven rubber plates stretched on both sides of the frame body 35A. Bolt rods 39 and 40 are pivotally attached to one side of the container 31, and a U-shaped engagement rod 41 is further pivotally attached. A hydraulic cylinder 43 with bolt receivers 39A, 40 for receiving bolts 39, 40 and a handle 43A held within the fixed frame 42 is attached to the corresponding side of the container 32, and a piston rod 44 of the hydraulic cylinder 43 has a piston rod 44 at its tip. A handle 45 that engages with the engagement rod 41 of the container 31 is fixedly provided. l Thus, the container 31 is placed on the machine stand 46, and a tray 47 provided with a discharge port 47A is provided directly below the containers 31, 32.

21は送液ポンプであり、送液管49と連絡し、送液管
49先端は枝管49A,49Bに分岐み、バルブ50A
,・50Bを介して容器31,32内に連絡する。
21 is a liquid feeding pump, which communicates with a liquid feeding pipe 49, and the tip of the liquid feeding pipe 49 branches into branch pipes 49A and 49B, and a valve 50A.
, 50B to the inside of the containers 31 and 32.

開放状態の容器31,32内に、上部に注入口51Aを
設けた袋状の濾布51を夫々収納し、底部の開放部を折
りたたんだのちに注入口51Aを送液管49の枝管79
A,49Bに夫々連絡す゜る。次いで容器31,32を
間隔板35を介して閉合し、容器31の係合杆41を容
器32の油圧シリンダー43のピストン杆44の先端に
設けられた把手45に係合し、ハンドル43Aを作動さ
せて油圧シリンダー43内の油圧を高め、ピストン杆4
4を押出すと係合杆41は把手45に牽引せられ、容器
31,32は間隔板35を介して閉鎖状態に固定せられ
る。
A bag-like filter cloth 51 with an injection port 51A provided at the top is stored in each of the open containers 31 and 32, and after folding up the opening at the bottom, the injection port 51A is inserted into the branch pipe 79 of the liquid supply pipe 49.
I will contact A and 49B respectively. Next, the containers 31 and 32 are closed via the spacer plate 35, the engaging rod 41 of the container 31 is engaged with the handle 45 provided at the tip of the piston rod 44 of the hydraulic cylinder 43 of the container 32, and the handle 43A is operated. to increase the oil pressure in the hydraulic cylinder 43, and the piston rod 4
4, the engaging rod 41 is pulled by the handle 45, and the containers 31 and 32 are fixed in a closed state via the spacer plate 35.

かくして容器31のボルト杆39,40を容器32のボ
ルト受け39A,40Aに夫々嵌入してナット395B
,40Bをボルト杆39,40先端より螺合して締付け
る。ボルト杆39,40とナット39B,40Bの締付
けは係合杆41と油圧シリンダー43のピストン杆44
との係合による予備固定により極めて容易となる。かく
して第9図に示すように濾過機の閉鎖固定を行えば容器
31,32内には濾過室が形成せられる。上記装置にお
いて、濾液排出管13Bのバルブ13″Bを開き、洗滌
液送通管13Cのバルブ13″Cを閉じ、排出管13D
のバルブ13″Dを開き、ポンプ5により被処理液を容
体1内に圧送する。
In this way, the bolt rods 39 and 40 of the container 31 are fitted into the bolt receivers 39A and 40A of the container 32, respectively, and the nuts 395B are inserted.
, 40B from the tips of bolt rods 39 and 40 and tighten. The bolt rods 39, 40 and nuts 39B, 40B are tightened by the engaging rod 41 and the piston rod 44 of the hydraulic cylinder 43.
Preliminary fixation by engagement with the holder is extremely easy. Thus, when the filter is closed and fixed as shown in FIG. 9, a filter chamber is formed within the containers 31 and 32. In the above device, the valve 13''B of the filtrate discharge pipe 13B is opened, the valve 13''C of the washing liquid delivery pipe 13C is closed, and the valve 13''B of the filtrate discharge pipe 13B is closed.
The valve 13''D is opened, and the liquid to be treated is pumped into the container 1 by the pump 5.

被処理液は濾過材7Aにより固形分を濾別され、濾液は
濾過材7内部に流入し、内孔8Aより回転軸7内に至り
、外孔8Bから回転軸7と外筒11との間の間隙12に
至り、濾液排出管13Bから排出せられ濾液貯槽13に
貯蓄せられ、更に過剰の濾液は洗滌液送通管13Cを介
して排出管13Dから排出せられる。濾過工程が終了し
たバルブ13″B,l3″Dを閉じバルブ13″Cを開
いて濾液貯槽13Cから洗滌液送通管13Cから濾液を
洗滌液として送通する。濾液である洗滌液はヘッド圧に
より間隙12から外孔8Bを介して回転軸7内に流入し
、内孔8Aから濾過材7A内に流出する。洗滌液送通と
ともに、あるいは洗滌液送通後適当時間を経て駆動装置
18にて回転軸7を回転させ、濾過材7Aを回転させる
。濾過材7Aが回転することより濾過材7A内の洗滌液
にかかる遠心力は濾過材7A中心から円周方向に向かう
The solid content of the liquid to be treated is filtered out by the filter material 7A, and the filtrate flows into the filter material 7, reaches the inside of the rotating shaft 7 through the inner hole 8A, and flows between the rotating shaft 7 and the outer cylinder 11 through the outer hole 8B. The filtrate reaches the gap 12, is discharged from the filtrate discharge pipe 13B and stored in the filtrate storage tank 13, and the excess filtrate is discharged from the discharge pipe 13D via the cleaning fluid delivery pipe 13C. After the filtration process is completed, the valves 13''B and 13''D are closed, the valve 13''C is opened, and the filtrate is passed from the filtrate storage tank 13C to the washing liquid delivery pipe 13C as a washing liquid. The water flows into the rotating shaft 7 from the gap 12 through the outer hole 8B, and flows out into the filter material 7A from the inner hole 8A. The rotary shaft 7 is rotated to rotate the filter medium 7A.As the filter medium 7A rotates, the centrifugal force applied to the cleaning liquid within the filter medium 7A is directed from the center of the filter medium 7A in the circumferential direction.

したがつて濾過材7Aが回転軸に垂直な濾過面を有する
場合は洗滌液の遠心力方向と濾過面とが平行になり遠心
力が濾過面に対する逆洗圧として有効に作用しない。し
かしソロバン玉状の濾過材7Aにあつては濾過面が遠心
力方向に対して傾斜しているから遠心力は濾過面に対す
る逆洗圧として有効に作用する。更に本発明の濾過材7
Aでは濾過材7A内の洗滌液が中心から円周方向に向か
つた結果濾過材中央部には負圧が生じ、したがつて濾過
材7A内への洗滌液の流入は円滑に行なわれ、更にこの
部分で濾過材7A外部の洗滌液を濾過材内に吸引するこ
とになり、この反動で濾過材7A内外の洗滌液に第10
図に示すような渦流が生じ濾過材内の洗滌液流は濾過材
軸と垂直方向ではなく外方にねじれた曲線に沿うように
なるから洗滌液はソロバン玉状の濾過材7Aの濾面に略
垂直に近い角度をもつて圧迫し、したがつて遠心力は効
率よく逆洗圧に変換されるのである。上記考察からして
ソロバン玉状の濾過材は少量の逆洗液による逆洗に最適
な形状であり、逆洗液として濾液が極せて有効に使用出
来ることが判明した。かくして濾過材7Aは、濾過材7
A内部から逆洗された容体1に備蓄された洗滌液19内
に下半部を浸漬しつつ回転し、濾過材7Aに付着せる固
形分20は第4図に示すように濾過材7Aの壁面抵抗に
より生じた洗滌液の液位の内外差によるヘッドhの圧力
と上記遠心力にもとずく逆洗圧との和によつて押されて
濾過材7A表面から若干浮上つた状態になつたところ濾
過材7Aの回転によつて生ずる液抵抗の剪断力によつて
剥離され、更に濾過材7Aの回転によつて生ずる液面の
騒乱摩擦によつて更に完全に固形分20は濾過材7Aか
ら洗い落される。洗滌が終りに近づいたら、洗滌汚液排
出管4を開き洗滌汚液を容体1外に排出する。その後更
に濾過材7Aを回転させると濾過材7Aを湿潤している
洗滌液は遠心力により飛散脱液し、洗滌は更に完全に行
われるようになる。洗滌汚液排出管4より排出された洗
滌汚液は貯液槽4Bに備蓄された後、送液ポンプ21に
よつて送液管49、枝管49A,49Bを介して圧擦濾
過装置22の容器31,32に収納された濾布51内に
注入口51Aを介して夫々圧入せられ、洗滌汚液中の固
形分は濾布51にて濾別せられ、濾液は濾布51から外
出し、容器31,32の内壁31A,32Aを介して容
器31,32の外壁31B,32B1内壁31A,32
A間を流下して吐出口31C,32Cから受け皿47に
排出せられる。
Therefore, if the filter medium 7A has a filtration surface perpendicular to the rotation axis, the direction of the centrifugal force of the washing liquid will be parallel to the filtration surface, and the centrifugal force will not effectively act as backwash pressure on the filtration surface. However, in the case of the Soroban bead-shaped filter medium 7A, since the filtering surface is inclined with respect to the direction of centrifugal force, the centrifugal force effectively acts as a backwash pressure on the filtering surface. Furthermore, the filter medium 7 of the present invention
At A, the cleaning liquid inside the filter medium 7A is directed from the center to the circumferential direction, and as a result, a negative pressure is generated in the center of the filter medium, so that the cleaning liquid flows smoothly into the filter medium 7A. Furthermore, the cleaning liquid outside the filter medium 7A is sucked into the filter medium at this part, and this reaction causes the cleaning liquid inside and outside the filter medium 7A to
As shown in the figure, a vortex is generated and the cleaning liquid flow in the filter medium is not perpendicular to the axis of the filter medium, but follows a curved line twisted outward, so the cleaning liquid flows onto the filter surface of the bead-shaped filter medium 7A. Pressure is applied at an angle close to vertical, so that centrifugal force is efficiently converted into backwash pressure. From the above considerations, it has been found that the Soroban bead-shaped filter material is the most suitable shape for backwashing with a small amount of backwashing liquid, and that the filtrate can be used extremely effectively as the backwashing liquid. Thus, the filter medium 7A is the filter medium 7A.
A rotates while immersing its lower half in the cleaning liquid 19 stored in the container 1 which has been backwashed from inside A, and the solid content 20 attached to the filter medium 7A is deposited on the wall surface of the filter medium 7A as shown in FIG. The head h is pushed by the sum of the pressure on the head h due to the difference in the level of the cleaning liquid caused by the resistance and the backwashing pressure based on the centrifugal force, and is slightly raised above the surface of the filter medium 7A. The solid content 20 is peeled off by the shear force of the liquid resistance generated by the rotation of the filter medium 7A, and furthermore, the solid content 20 is completely washed away from the filter medium 7A by the turbulent friction of the liquid surface caused by the rotation of the filter medium 7A. be dropped. When washing approaches the end, the washed dirty liquid discharge pipe 4 is opened and the washed dirty liquid is discharged to the outside of the container 1. Thereafter, when the filter medium 7A is further rotated, the cleaning liquid that has moistened the filter medium 7A is scattered and removed by centrifugal force, and the cleaning is performed even more completely. The washed filthy liquid discharged from the washed sewage liquid discharge pipe 4 is stored in the liquid storage tank 4B, and then sent to the pressure friction filtration device 22 via the liquid sending pipe 49 and branch pipes 49A and 49B by the liquid sending pump 21. The filter cloths 51 housed in the containers 31 and 32 are press-fitted through the injection ports 51A, and the solid content in the washing liquid is filtered out by the filter cloths 51, and the filtrate comes out from the filter cloths 51. , outer walls 31B, 32B1 of containers 31, 32 via inner walls 31A, 32A of containers 31, 32, inner walls 31A, 32
It flows down between A and is discharged into the receiving tray 47 from the discharge ports 31C and 32C.

上記濾過工程が終了したらボルト杆39,40とナット
39B,40Bの締付けをゆるめる。
After the above filtration step is completed, loosen the bolts 39, 40 and nuts 39B, 40B.

この際も係合杆41とピストン杆44との係合固定によ
り容器31,32、間隔板35が濾過残圧によつて開く
のを防止するからナット39B,40Bをゆるめ締付を
開放することは極めて簡単である。更に油圧シリンダー
の油圧を取り除き、係合杆41を取りはずして容器31
,32および間隔板35を開いて濾布51から固形分を
取出す。かくして洗滌汚液は固形分を高濃度で含む被処
理液の濾過に最つとも適した圧搾濾過装置22により濾
過され、濾液は還送管23を介して原液槽4Aに送通さ
れ、原液に混入される。本発明は叙上のごとく内部にソ
ロバン玉状の中空の濾過材が回転自在に取り付けられた
密閉可能な容体からなる濾過機と、該濾過機上部に設け
られた濾液貯槽、洗滌汚液を備蓄する貯液槽および圧搾
濾過装置を介して貯液槽と原液槽を連絡する還送径路と
からなり、濾過工程においてはソロバン玉状の中空の濾
過材の外面から内面に向けて濾過を行ない、濾過材外面
に固形分が付着し、濾過材内に連絡する濾液排出径路に
濾液を排出し、濾液は濾液貯槽に貯えられ、余分な濾液
は装置外へ排出される。
At this time as well, the engagement and fixation of the engagement rod 41 and the piston rod 44 prevents the containers 31, 32 and the spacer plate 35 from opening due to residual filtration pressure, so loosen the nuts 39B, 40B to release the tightening. is extremely simple. Furthermore, the hydraulic pressure of the hydraulic cylinder is removed, the engaging rod 41 is removed, and the container 31 is removed.
, 32 and the spacer plate 35 are opened to remove the solid content from the filter cloth 51. In this way, the washed waste liquid is filtered by the squeeze filtration device 22, which is most suitable for filtering a liquid to be treated containing a high concentration of solids, and the filtrate is sent to the stock solution tank 4A via the return pipe 23, and is converted into a stock solution. mixed in. As described above, the present invention comprises a filter consisting of a sealable container in which a hollow bead-shaped filter material is rotatably attached, a filtrate storage tank provided on the upper part of the filter, and a storage tank for storing cleaning waste liquid. In the filtration process, filtration is performed from the outer surface to the inner surface of the hollow filter material in the shape of a Soroban bead, Solid content adheres to the outer surface of the filter medium, and the filtrate is discharged into a filtrate discharge path communicating with the inside of the filter medium, the filtrate is stored in a filtrate storage tank, and excess filtrate is discharged outside the device.

洗滌工程においては、上記ソロバン玉状の濾過材の逆洗
効率は非常に大きいのて大量の洗滌液を必要とせず、し
たがつて滌液貯槽に貯えられた濾液を洗滌液として有効
に用いることが出来、これを洗滌液径路により濾過材内
に送通し、濾過材の逆洗を行ない、濾過材の回転とあい
まつて効果的な洗滌を行なう。このように本発明の濾過
機では洗滌液として濾液を有効に利用出来るので、とく
に洗滌液を必要とせず被処理量が増加しないので準クロ
ーズドシステムを構成するには好都合である。また洗滌
汚液は貯液槽に備蓄された後、固形分を高濃度に含む被
処理液の濾過に有効な圧搾濾過装置により濾過されるか
ら外界への漏洩は完全に防止され、かつ固形分が取り除
かれ、該固形分は濃縮されて量が減少しているのみなら
ず含液量が少ないから後処理が非常に簡単になる。固形
分を分離された濾液は還送径路により原液槽に送通され
原液に混入されて、再び本濾過装置に送通され更に完全
に濾過され、ここに廃液等の処理には理想的な準クロー
ズドシステムが形成されるのである。そして本発明では
洗滌液(濾液)の貯槽を容体直上に設けヘッド圧によつ
て濾〜過材内に送通するものである。そして特にヘッド
圧以外に送通圧をかけることは必要ではない。何となれ
ば前記した理由によつてソロバン玉状の濾過材では遠心
力が効率よく逆洗圧となるからである。かくして本発明
では装置の配置が非常にコンパクト化されるのである。
図面の簡単な説明図面は本発明の一実施例を示すもので
あり、第1図は本濾過装置の模式図、第2図は濾過機の
主要部切欠側面図、第3図は濾過機容体部の第2図にお
けるA−N断面図、第4図は濾過機内の濾過材の洗滌液
浸漬部分の断面図である。
In the washing process, the backwashing efficiency of the Soroban bead-shaped filter medium is very high, so a large amount of washing liquid is not required, and therefore the filtrate stored in the washing liquid storage tank can be effectively used as the washing liquid. This is passed through the cleaning liquid path into the filter medium to perform backwashing of the filter medium, and in combination with the rotation of the filter medium, effective cleaning is performed. As described above, in the filter of the present invention, the filtrate can be effectively used as the washing liquid, so the washing liquid is not particularly required and the amount to be processed does not increase, so it is convenient for constructing a semi-closed system. In addition, after the washed waste liquid is stored in a liquid storage tank, it is filtered by a press filtration device that is effective for filtering liquids to be treated that contain a high concentration of solids, so leakage to the outside world is completely prevented, and the solid content is is removed, and the solid content is not only concentrated and reduced in volume, but also has a low liquid content, making post-processing very easy. The filtrate from which the solid content has been separated is sent to the stock solution tank via the return path, mixed with the stock solution, and then sent to the main filtration device again for complete filtration. A closed system is formed. In the present invention, a storage tank for cleaning liquid (filtrate) is provided directly above the container, and the cleaning liquid (filtrate) is passed through the filtration medium by head pressure. In addition, it is not necessary to apply any pressure other than the head pressure. This is because the centrifugal force efficiently becomes backwashing pressure in the soroban bead-shaped filter material for the reason described above. Thus, according to the present invention, the arrangement of the device can be made very compact.
BRIEF DESCRIPTION OF THE DRAWINGS The drawings show one embodiment of the present invention, and FIG. 1 is a schematic diagram of the present filtration device, FIG. 2 is a cutaway side view of the main part of the filtration machine, and FIG. 3 is a casing of the filtration machine. FIG. 4 is a cross-sectional view of the portion of the filter material in the filter machine immersed in the cleaning liquid.

第5〜9図は第1図における圧搾濾過装置22の一実施
例を示す詳細図であり、第5図は分解斜視図、第6図は
開放状態組付平面図、第7図は容体の一部切欠側断面図
、第8図は濾布の斜視図、第9図は閉鎖状態組付正面図
、第10図は濾過材回転時の洗滌液の流れを示す側断面
図である。図中、1・・・・・・容体、4・・・・・・
洗滌汚液排出管、4A・・・・・・原液槽、4B・・・
・・・貯液槽、6・・・・・・注液管、7・・・・・・
回転軸、7A・・・・・・濾過材、13・・・・・・濾
液貯槽、13B・・・・・・濾液排出管、13C・・・
・・・洗滌液送通管、22・・・・・・圧搾濾過装置、
23・・・・・・還送管。
5 to 9 are detailed views showing one embodiment of the compressed filtration device 22 in FIG. 1, FIG. 5 is an exploded perspective view, FIG. 6 is an assembled plan view in an open state, and FIG. 8 is a perspective view of the filter cloth, FIG. 9 is an assembled front view in a closed state, and FIG. 10 is a side sectional view showing the flow of cleaning liquid when the filter material is rotated. In the diagram, 1...Condition, 4...
Washing sewage discharge pipe, 4A... Raw solution tank, 4B...
...Liquid storage tank, 6...Liquid injection pipe, 7...
Rotating shaft, 7A...filter material, 13...filtrate storage tank, 13B...filtrate discharge pipe, 13C...
... Washing liquid delivery pipe, 22 ... Pressure filtration device,
23...Return pipe.

Claims (1)

【特許請求の範囲】 1 密閉可能な容体と、該容体の横方向に設けられた回
転軸と、該回転軸に取付けられた一個または二個以上の
ソロバン玉状の中空濾過材と、該容体内に被処理液を圧
送する送液経路と、該濾過材内に連絡する濾液排出経路
および洗滌液径路とからなり、かつ濾液排出経路と洗滌
液径路を容体直上部に設けた濾液貯槽を介して連絡した
濾過機の一個もしくは二個以上と、該濾過機の容体に洗
滌汚液排出径路を介して連絡する貯液槽と、該貯液槽か
ら圧搾濾過装置を介して該濾過機の送液径路側へ連絡す
る還送経路とからなる濾過装置。 2 密閉可能な容体と、該容体の横方向に設けられた回
転軸と、該回転軸に取付けられた一個または二個以上の
ソロバン玉状の中空濾過材と、該容体内に被処理液を圧
送する送液経路と、該濾過材内に連絡する濾液排出経路
および洗滌液径路とからなり、かつ濾液排出経路と洗滌
液径路を容体直上部に設けた濾液貯槽を介して連絡した
濾過機の一個もしくは二個以上と、該濾過機の容体に洗
滌汚液排出径路を介して連絡する貯液槽と、該貯液槽か
ら圧搾濾過装置を介して該濾過機の送液径路側へ連絡す
る還送経路からなる濾過装置において容体内に送液経路
から被処理液を圧入し、被処理液中の固形分を濾過材に
よつて濾別し、濾液は濾過材内から濾液排出経路を経て
濾液貯槽に備蓄し、上記濾過工程終後は洗滌液径路から
濾液貯槽に蓄積された濾液を洗滌液として濾過材内部に
送通せしめるとともに回転軸を回転させることにより濾
過材を回転させつつ濾過材に付着した固形分を除去洗滌
し、洗滌汚液は洗滌汚液排出径路を介して貯液槽に備蓄
し、更に該貯液槽から圧搾瀘過装置によつて洗滌汚液の
固形分を濾過除去し、濾液を還送経路により上記濾過機
の洗滌液径路側へ還送合一せしめることを特徴とする特
許請求の範囲1項に記載の濾過装置を用いた濾過方法。
[Scope of Claims] 1. A sealable container, a rotating shaft provided in the lateral direction of the container, one or more hollow filter media in the form of beads attached to the rotating shaft, and the container. It consists of a liquid feeding path that pumps the liquid to be treated into the body, and a filtrate discharge path and a washing liquid path that communicate with the inside of the filter medium, and the filtrate discharge path and the washing liquid path are provided directly above the container through a filtrate storage tank. one or more filtration machines connected to each other, a liquid storage tank connected to the container of the filtration machine via a washing sewage discharge path, and a liquid storage tank connected to the filtration machine via a squeeze filtration device. A filtration device consisting of a return path that connects to the liquid path side. 2. A sealable container, a rotating shaft provided in the lateral direction of the container, one or more hollow filter media in the form of beads attached to the rotating shaft, and a liquid to be treated in the container. The filtration machine consists of a liquid feeding path for pressure feeding, a filtrate discharge path and a washing liquid path that communicate with the inside of the filter medium, and the filtrate discharge path and the washing liquid path are connected via a filtrate storage tank provided directly above the container. one or more of them, a liquid storage tank connected to the container of the filtration machine via a washing waste liquid discharge path, and a liquid storage tank connected to the liquid feeding path side of the filtration machine via a squeeze filtration device. In a filtration device consisting of a return route, the liquid to be treated is forced into the container from the liquid feeding route, solids in the liquid to be treated are filtered out by a filter material, and the filtrate is passed from within the filter material through the filtrate discharge route. The filtrate is stored in a filtrate storage tank, and after the filtration process is completed, the filtrate accumulated in the filtrate storage tank is passed through the washing liquid path into the filter medium as a washing liquid, and the rotating shaft is rotated to rotate the filtration medium. The solid content adhering to the filtrate is removed and washed, and the washed sewage liquid is stored in a liquid storage tank via the washed sewage liquid discharge path, and the solid content of the washed sewage liquid is further filtered from the liquid storage tank by a pressing filter device. A filtration method using the filtration device according to claim 1, characterized in that the filtrate is returned to the washing liquid path side of the filter through a return path and combined with the filtrate.
JP52020418A 1977-02-25 1977-02-25 Filtration device and filtration method using the filtration device Expired JPS6052850B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP52020418A JPS6052850B2 (en) 1977-02-25 1977-02-25 Filtration device and filtration method using the filtration device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP52020418A JPS6052850B2 (en) 1977-02-25 1977-02-25 Filtration device and filtration method using the filtration device

Publications (2)

Publication Number Publication Date
JPS53105770A JPS53105770A (en) 1978-09-14
JPS6052850B2 true JPS6052850B2 (en) 1985-11-21

Family

ID=12026477

Family Applications (1)

Application Number Title Priority Date Filing Date
JP52020418A Expired JPS6052850B2 (en) 1977-02-25 1977-02-25 Filtration device and filtration method using the filtration device

Country Status (1)

Country Link
JP (1) JPS6052850B2 (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS55137015A (en) * 1979-04-10 1980-10-25 Nippon Enbairo Kogyo Kk Rotary filter and filtering using the same
US9604162B2 (en) * 2014-04-11 2017-03-28 Advanced Filtration Technologies Inc. Rotary disc filter device
US9555349B2 (en) * 2014-04-11 2017-01-31 Advanced Filtration Technologies Inc. Rotary disc filter device

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS4419673Y1 (en) * 1966-10-15 1969-08-22
JPS5043567A (en) * 1973-08-21 1975-04-19

Also Published As

Publication number Publication date
JPS53105770A (en) 1978-09-14

Similar Documents

Publication Publication Date Title
JPH10128016A (en) Sludge filter, filtration plant and filtration process particularly for liquid fertilizer
EP0428711A1 (en) Method and apparatus for clarifying liquids
JPH0866608A (en) Filtration device with filtrate collection device
JPS6052850B2 (en) Filtration device and filtration method using the filtration device
US5228987A (en) Method and apparatus for clarifying liquids
JP3747100B2 (en) Fluid purification device
JP3385490B2 (en) Waste liquid filtration device and filter material cleaning method
CN208426718U (en) A kind of filtering tank with automatic discharging function
JPS5835297Y2 (en) Filter device with backwashing means
JP4029263B2 (en) Combined microfiltration method and filtration device
JP2001137620A (en) Filtration device
JP2766457B2 (en) Continuous solid-liquid separator
JPS62722B2 (en)
JPH038331Y2 (en)
JP2696666B2 (en) Pressure filtration device
US2293120A (en) Filter
JPH0775646B2 (en) Dehydrator
CN221181793U (en) A filtering mechanism for ethylene carbonate production
CN214360294U (en) A desliming device for papermaking wastewater
JPH0422407A (en) Rotary drum type dehydrating-liquid squeezing device having precoated layer
JP3484632B2 (en) Filtration device
CN224015345U (en) An activated carbon filtration device for water supply in a water plant
CN220609383U (en) Suction filtration groove convenient to clean
JPS6034398Y2 (en) Oil removal device
CN218357688U (en) Walnut oil filter equipment