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
JPS6018443B2 - Slag filtration device - Google Patents
[go: Go Back, main page]

JPS6018443B2 - Slag filtration device - Google Patents

Slag filtration device

Info

Publication number
JPS6018443B2
JPS6018443B2 JP57085614A JP8561482A JPS6018443B2 JP S6018443 B2 JPS6018443 B2 JP S6018443B2 JP 57085614 A JP57085614 A JP 57085614A JP 8561482 A JP8561482 A JP 8561482A JP S6018443 B2 JPS6018443 B2 JP S6018443B2
Authority
JP
Japan
Prior art keywords
filter
filtrate
guide hole
filtration device
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
JP57085614A
Other languages
Japanese (ja)
Other versions
JPS58199011A (en
Inventor
五郎 佐々木
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.)
Individual
Original Assignee
Individual
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 Individual filed Critical Individual
Priority to JP57085614A priority Critical patent/JPS6018443B2/en
Publication of JPS58199011A publication Critical patent/JPS58199011A/en
Publication of JPS6018443B2 publication Critical patent/JPS6018443B2/en
Expired legal-status Critical Current

Links

Landscapes

  • Filtration Of Liquid (AREA)

Description

【発明の詳細な説明】 この発明は、有機、無機の微粒子懸濁液(以下、原液と
いう。
DETAILED DESCRIPTION OF THE INVENTION The present invention provides a suspension of organic and inorganic particles (hereinafter referred to as a stock solution).

)を水分と微粒子とに分離しその微粒子を脱水して積層
微粒子(以下、ケークという。)とするろ体回転式ろ達
ろ過装置に係るものであって以下に実施例図を参考に詳
しく説明する。原液供給口11aとケーク取出口11b
とを有する処理室11とろ液排出ロー2aを有するろ液
室12とを隔壁1川こて区画した処理箱1の処理室11
内に、後述のる体2を2個以上隣接させて並べてろ体列
とし、それを2列適宜貴隔を隔てて配列し、しかも、ろ
体2の回転軸21は、両隔壁10,1川こ回転自由に水
解状に支持され、その回転軸21の一端を処理箱1の外
に突出させて、モータ等の駆動手段(図示せず)にて回
転させられる伝達歯車Gを設けている。
) is separated into moisture and fine particles, and the fine particles are dehydrated to form laminated fine particles (hereinafter referred to as cake).The filter body rotating type filtration device is described below in detail with reference to example diagrams. do. Stock solution supply port 11a and cake removal port 11b
The processing chamber 11 of the processing box 1 is divided into a processing chamber 11 having a filtrate discharge row 2a and a filtrate chamber 12 having a filtrate discharge row 2a.
Inside, two or more bodies 2, which will be described later, are arranged adjacently to form a filter body row, and these are arranged in two rows with appropriate distances apart, and the rotating shaft 21 of the filter body 2 is connected to both partition walls 10, 1. A transmission gear G is provided, which is supported in a hydrostatic manner so that the river can rotate freely, and has one end of its rotating shaft 21 protruding outside the processing box 1, and is rotated by a driving means (not shown) such as a motor. .

ろ体2は、回転軸21を偏心とした環状(円、だ円又は
たまご形等の任意の形状)のる片22と、それの外周緑
で回転軸21の中心よりの最少距離mよりも直径の小さ
く、偏心していない間座23を交互(又は適宜組合せて
もよい。
The filter body 2 has an annular piece 22 (of any shape such as a circle, an oval, or an egg shape) that is eccentric to the rotation axis 21, and a green outer circumference of the piece 22, which is more than the minimum distance m from the center of the rotation axis 21. Spacers 23 having a small diameter and not being eccentric may be used alternately (or in combination as appropriate).

)に組合せてキーKで回転軸21に固定したものである
。又、ろ体2′には、そのろ片22′に間座23の外周
より外で軸方向にろ液案内孔24を穿ってなるものがあ
り、そのろ体2′は、ろ片22′と間座23を組合せた
ものを軸万向の両端より挟持する固定円板29を設け、
同円板29にはろ片22′のる液案内孔24に照応する
ろ液案内孔24′を穿ち、その厚さは、前記隔壁10よ
りもやや肉厚である。複数のる体2,2′にて形成され
るろ体列の隣庚ろ体2,2同志は、ろ片22,22′が
相手ろ体2,2′の間座23の外周で2枚のる片22,
22,22′,22′間によって形成される間際溝25
に突入させている。
) and fixed to the rotating shaft 21 with a key K. Also, some filter bodies 2' have filtrate guide holes 24 formed in the filter pieces 22' in the axial direction outside the outer periphery of the spacer 23; A fixed disk 29 is provided which holds the combination of the spacer 23 and the spacer 23 from both ends of the shaft in all directions,
A filtrate guide hole 24' corresponding to the liquid guide hole 24 in which the filter piece 22' is mounted is bored in the circular plate 29, and its thickness is slightly thicker than that of the partition wall 10. In the filter bodies 2, 2 adjacent to each other in the filter body row formed by a plurality of filter bodies 2, 2', two filter pieces 22, 22' are arranged on the outer periphery of the spacer 23 of the other filter bodies 2, 2'. Glue piece 22,
22, 22', and the border groove 25 formed between 22'
It is entering into.

なお、図中符号Sはシール材で、ケーク取出口11bの
周囲とそれに最も近いろ体との間をつなぎ原液とケーク
取出口11bに蟹るケークとを完全に分断するものであ
り、Fはケーク取出口11bの閉鎖用ふたで、一定条件
のもとで手動又は自動で開放する。
In addition, the symbol S in the figure is a sealing material that connects between the periphery of the cake outlet 11b and the filter body closest to it and completely separates the undiluted solution from the crab cake at the cake outlet 11b, and F is a sealing material. The lid for closing the cake outlet 11b is opened manually or automatically under certain conditions.

ここで、ろ液案内孔24を有するろ片22′のる体2′
に隣接するろ体2,2′のる片22,22′の外周縁は
、回転軸21の中心からの最も長い距離Lにおいて、ろ
片22′のる液案内孔24を横切る場合又は横切らない
場合がある。
Here, a body 2' on which a filter piece 22' having a filtrate guide hole 24 is mounted.
The outer peripheral edges of the pieces 22, 22' on which the filter pieces 2, 2' adjacent to the filter bodies 2, 2' are placed may or may not cross the liquid guide hole 24 on which the filter pieces 22' are placed, at the longest distance L from the center of the rotating shaft 21. There are cases.

その横切る場合としては、ろ過の精度を余り要求されな
いときで、ろ液案内孔24の周囲に蟹る微粒子を取除い
て一時的にろ摩る週をしなくとも許されるろ過作業に使
用される。ろ体2′の側方には、ろ片22′のる液案内
孔24を洗浄する手段として圧力水噴射ノズル3を設け
てもよい。
The case where it is used is when filtration accuracy is not required so much, and it is used for filtration work that removes fine particles that collect around the filtrate guide hole 24 and does not require a temporary filtration period. . A pressure water injection nozzle 3 may be provided on the side of the filter body 2' as a means for cleaning the liquid guide hole 24 in which the filter piece 22' is placed.

又、原液貯蔵タンクTと原液供給口11aとを結ぶパイ
プPに凝集剤Rの添加用パイプP′を連結してもよい。
又、その凝集剤添加パイプPにバルブVを設けたケーク
取出口11b、ケークの硬さを機的又は機械的に検知し
、バルフVを開閉させて凝集剤の添加量を調整する装置
Aを設けてもよい。又、実施例図では、2種類のる体2
,2′を粗合せたもので示しているが、ろ体2即ちろ片
22にろ液案内孔24がないものを全部又は大半使用す
る場合は、原液供給ローlaはケーク取出口11bの対
向部に設け、原液供給口11aの周囲と、それに最も近
いろ体2とにケーク排出ロー1bと同様のシシール材を
備えなければならない。
Further, a pipe P' for adding the flocculant R may be connected to a pipe P connecting the stock solution storage tank T and the stock solution supply port 11a.
In addition, a cake outlet 11b provided with a valve V on the flocculant addition pipe P, and a device A that mechanically or mechanically detects the hardness of the cake and adjusts the amount of flocculant added by opening and closing the valve V. It may be provided. In addition, in the example diagram, two types of climbing bodies 2 are shown.
, 2' are roughly combined, but if all or most of the filter body 2, that is, the filter piece 22 without the filtrate guide hole 24 is used, the stock solution supply roller la should be placed opposite the cake outlet 11b. A sealing material similar to that of the cake discharge row 1b must be provided around the stock solution supply port 11a and on the filter body 2 closest to it.

しかも、ろ液排出口12aは処理室11でろ体2の背部
(ろ体列間の反対部分。)に設けることになり、ろ液案
内孔24を有するろ体2では、図面のとおりる液室12
を設けてろ液を導く。次に、この発明装置の動作説明を
すると、先ず原液を供給ローlaから処理室11内に流
入させる。
Moreover, the filtrate discharge port 12a is provided at the back of the filter body 2 in the processing chamber 11 (the opposite part between the rows of filter bodies). 12
to guide the filtrate. Next, to explain the operation of the apparatus of the present invention, first, the stock solution is caused to flow into the processing chamber 11 from the supply roller la.

その際ふたFは閉鎖しており、又、各ろ体2,2′は図
中矢印方向に回転している。そこで原液は、各ろ体2,
2′の間隙溝25に入りろ液が案内孔24,24′(ろ
液案内孔24のないろ体22の場合は、ろ片22と隣酸
ろ体2の間座23との間)を通過してろ液排出口12a
から案外に排出される。それと同時に、間隙溝25には
、徐々に微粒子が残燈して充満する。すると次には、そ
の微粒子間がろ過孔となり原液中の水分を通過すること
になる。間隙溝25の微粒子は隣接のる体2,2′によ
ってろ体列間に掻き出される体2,2′の外周に積属し
てケークとなり、ケーク取出口11bへとる体2,2′
の回転にて運ばれる。そして、ケーク取出口11bがケ
ークで満ち、そのケークによって原液が直接ケーク取出
口11bから流出しないようになったとき、ふたFは開
放される。ケークは、その取出口11bから順次出てき
て、その後方から押し出されたケークにて常に原液をケ
ーク取出口11bから流出しないようにろ体2,2′の
回転速度にて調整されている。ろ体2′,2の間隙満2
5でろ液案内孔24の周囲に残った(ろ液案内孔24の
ない場合は、間座23の外周に残った)微粒子は、長時
間の作業の際、それが硬化することになる。
At this time, the lid F is closed, and each filter body 2, 2' is rotating in the direction of the arrow in the figure. Therefore, the stock solution was prepared for each filter body 2,
The filtrate enters the gap groove 25 of 2' and passes through the guide holes 24, 24' (in the case of the filter body 22 without the filtrate guide hole 24, between the filter piece 22 and the spacer 23 of the adjacent acid filter body 2). through the filtrate outlet 12a
It is unexpectedly ejected from. At the same time, the gap groove 25 is gradually filled with afterglow particles. Next, the spaces between the fine particles become filtration pores, allowing the moisture in the stock solution to pass through. The fine particles in the gap groove 25 accumulate on the outer periphery of the bodies 2, 2' scraped out between the rows of filter bodies by the adjacent filter bodies 2, 2' to form a cake, and are taken to the cake outlet 11b.
It is carried by the rotation of Then, when the cake outlet 11b is filled with cake and the cake prevents the stock solution from directly flowing out from the cake outlet 11b, the lid F is opened. The cakes come out one by one from the outlet 11b, and the rotational speed of the filter bodies 2, 2' is adjusted so that the cake pushed out from the rear does not always cause the undiluted liquid to flow out from the cake outlet 11b. Gap between filter bodies 2', 2 full 2
The fine particles remaining around the filtrate guide hole 24 in step 5 (if there is no filtrate guide hole 24, remaining around the outer periphery of the spacer 23) will harden during long-term operation.

そこで、隣接のる体2,2′のる片22,22′の最長
外周緑1の部分が、硬化した微粒子のところに至ったと
きる液案内孔24に全部又は一部を押し入れ(案内孔2
4のないろ体2では間座23の外周から全部又は一部を
掻き取る)再度新しい微粒子を積層させ、即ち、微粒子
間の再生を図りろ達ろ過を連続的なものとさせることに
なる。又、隣接のる体2,2′同志がその回転速度を変
えることは、間隙溝25の微粒子のダイラ−夕ンシ作用
をより確実にできると共に、ろ液案内孔24を有するろ
体2′を使用している場合、案内孔24がろ片22′に
等分に配置されていなくとも全案内孔24には必ず隣接
のる体2,2′のる片22,22′における最長外周緑
1が至ることになる。ここに、この発明はその目的を達
する。
Therefore, the part of the longest outer circumference green 1 of the pieces 22, 22' on which the adjoining bodies 2, 2' rests is pushed in whole or in part into the liquid guide hole 24 when it reaches the hardened particles (the guide hole 2
In the case of the filter body 2 without the spacer 23, new fine particles are layered again (all or part of the outer periphery of the spacer 23 is scraped off), that is, regeneration between the fine particles is attempted and continuous filtration is achieved. Furthermore, changing the rotational speed of the adjacent bodies 2 and 2' makes it possible to more reliably prevent the fine particles in the gap groove 25 from being diluted, and also to improve the filter body 2' having the filtrate guide hole 24. When in use, even if the guide holes 24 are not evenly distributed on the filter pieces 22', all the guide holes 24 will always have the longest outer circumference green 1 in the pieces 22, 22' on which the bodies 2, 2' are attached. will be reached. Here, the invention achieves its purpose.

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

第1図は正断面図、第2図は第1図の×2−×2現断面
図、第3図は第1図の×3一×3硯断図一省略拡大図、
第4図は第3図の底面一部省略図。 1・・…・処理箱、2,2′・・・・・・ろ体、11a
・・・・・・原液供給口、1 1b・・・・・・ケーク
取出口、21…・・・回転軸、22,22′・・・・・
・ろ片、24・・・・・・ろ液案内孔、25・・・・・
・間隙溝、12a・・・・・・ろ液排出口。 茶′図*2図 好J図 繁く凶
Fig. 1 is a front sectional view, Fig. 2 is a x2-x2 current sectional view of Fig. 1, Fig. 3 is an omitted enlarged view of Fig. 1,
FIG. 4 is a partially omitted bottom view of FIG. 3. 1... Processing box, 2, 2'... Filter body, 11a
......Standard solution supply port, 1 1b...Cake removal port, 21...Rotary shaft, 22, 22'...
・Filter piece, 24...Filtrate guide hole, 25...
-Gap groove, 12a...filtrate outlet. Tea' figure *2 figure good J figure frequently bad

Claims (1)

【特許請求の範囲】 1 ろ片と外周に開通した間隙溝を軸方向に交互に有す
るろ体の多数を、互いに相隣接するろ体の間隙溝にろ片
を突入させた状態に並べて原液供給口、ケーク取出口及
びろ液排出口を有する処理管内に配置してなるろ過装置
において、ろ片は、その外周縁が回転軸の中心からの距
離が異なると共に相隣接するろ体又は個々のろ体の回転
速度を異ならせたことを特徴とするろ滓ろ過装置。 2 特許請求の範囲1の装置における全部又は一部のろ
体のろ片には、その軸方向に間隙溝と連結するろ液案内
孔を穿つてなり、しかも同案内孔の一方又は両端は、ろ
液排出口につながつてなるろ滓ろ過装置。 3 特許請求の範囲2の装置におけるろ液案内孔を有す
るろ体のろ液案内孔を洗浄する手段を設けたろ滓ろ過装
置。 4 特許請求の範囲1から3のいずれかの装置において
、原液に凝集剤を添加する装置を設けたろ滓ろ過装置。 5 特許請求の範囲4の装置において、凝集剤の添加量
を自動調整する手断を設けたろ滓ろ過装置。
[Scope of Claims] 1 A large number of filter bodies having filter pieces and gap grooves opened on the outer periphery alternately in the axial direction are arranged in a state in which the filter pieces are inserted into the gap grooves of mutually adjacent filter bodies, and the stock solution is supplied. In a filtration device disposed in a processing tube having a spout, a cake outlet, and a filtrate outlet, the outer periphery of the filter pieces has different distances from the center of the rotation axis, and the filter pieces are separated from adjacent filter bodies or individual filters. A slag filtration device characterized by different rotation speeds of the body. 2. In the device according to claim 1, all or some of the filter pieces of the filter body are provided with a filtrate guide hole connected to the gap groove in the axial direction, and one or both ends of the guide hole are A filtration device connected to a filtrate outlet. 3. A filtration filtration device provided with means for cleaning the filtrate guide hole of the filter body having the filtrate guide hole in the device according to claim 2. 4. A filtration filtration device according to any one of claims 1 to 3, which is provided with a device for adding a flocculant to the stock solution. 5. A slag filtration device according to claim 4, which is provided with a manual cut that automatically adjusts the amount of coagulant added.
JP57085614A 1982-05-18 1982-05-18 Slag filtration device Expired JPS6018443B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP57085614A JPS6018443B2 (en) 1982-05-18 1982-05-18 Slag filtration device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP57085614A JPS6018443B2 (en) 1982-05-18 1982-05-18 Slag filtration device

Publications (2)

Publication Number Publication Date
JPS58199011A JPS58199011A (en) 1983-11-19
JPS6018443B2 true JPS6018443B2 (en) 1985-05-10

Family

ID=13863715

Family Applications (1)

Application Number Title Priority Date Filing Date
JP57085614A Expired JPS6018443B2 (en) 1982-05-18 1982-05-18 Slag filtration device

Country Status (1)

Country Link
JP (1) JPS6018443B2 (en)

Also Published As

Publication number Publication date
JPS58199011A (en) 1983-11-19

Similar Documents

Publication Publication Date Title
US3193105A (en) Continuous disc filter
GB1406490A (en) Filtration system
US3734299A (en) Automatic continuously backflow washing-type filter
US2894632A (en) Drum disc filter
US4919806A (en) Cross-flow type filter system
JPS6018443B2 (en) Slag filtration device
US2588976A (en) Filter
JPS60118209A (en) Filter comprising multiple chambers
US1887129A (en) Continuous filtering apparatus
CA1090264A (en) Rotating interleaved disc filter apparatus
CN215876876U (en) Filtering unit and filtering device
JPH0699041A (en) Rotary type membrane separation device
JP2979296B2 (en) Continuous filtration system for suspension
JPS561296A (en) Dehydrator
JPS6323932Y2 (en)
US3389802A (en) Tank filter with interchangeable clamping plates
JP6432000B1 (en) Hydraulic motor and backwash type filtration device
CN219388667U (en) Reversing valve for petroleum machinery
JPS62731Y2 (en)
US2263852A (en) Filter
CN224077232U (en) Efficient sludge dewatering device for sewage treatment
CN222647740U (en) A natural gas purification production wastewater treatment device
JPH0127843Y2 (en)
JPS6310861Y2 (en)
DE626354C (en) Rotary drum filter working with negative and positive pressure