JPH04271802A - Method for removing cake in filter - Google Patents
Method for removing cake in filterInfo
- Publication number
- JPH04271802A JPH04271802A JP3056040A JP5604091A JPH04271802A JP H04271802 A JPH04271802 A JP H04271802A JP 3056040 A JP3056040 A JP 3056040A JP 5604091 A JP5604091 A JP 5604091A JP H04271802 A JPH04271802 A JP H04271802A
- Authority
- JP
- Japan
- Prior art keywords
- filter
- filtration
- liquid
- tank
- air
- 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.)
- Withdrawn
Links
- 238000000034 method Methods 0.000 title claims description 56
- 239000000706 filtrate Substances 0.000 claims abstract description 36
- 238000007599 discharging Methods 0.000 claims abstract description 17
- 239000007788 liquid Substances 0.000 claims description 164
- 238000001914 filtration Methods 0.000 claims description 119
- 239000002893 slag Substances 0.000 claims description 59
- 239000007791 liquid phase Substances 0.000 claims description 5
- 230000002093 peripheral effect Effects 0.000 claims description 4
- 238000000926 separation method Methods 0.000 claims description 2
- 239000000428 dust Substances 0.000 abstract description 17
- 230000018044 dehydration Effects 0.000 abstract description 2
- 238000006297 dehydration reaction Methods 0.000 abstract description 2
- 239000000463 material Substances 0.000 description 20
- 239000005909 Kieselgur Substances 0.000 description 12
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 12
- 239000004744 fabric Substances 0.000 description 10
- 238000004140 cleaning Methods 0.000 description 8
- 239000012065 filter cake Substances 0.000 description 8
- 239000000203 mixture Substances 0.000 description 5
- 238000010586 diagram Methods 0.000 description 4
- 239000006185 dispersion Substances 0.000 description 4
- 239000000835 fiber Substances 0.000 description 4
- 239000010802 sludge Substances 0.000 description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 3
- 239000000853 adhesive Substances 0.000 description 2
- 230000001070 adhesive effect Effects 0.000 description 2
- 238000011001 backwashing Methods 0.000 description 2
- 239000002657 fibrous material Substances 0.000 description 2
- 238000005192 partition Methods 0.000 description 2
- 238000007747 plating Methods 0.000 description 2
- 239000002699 waste material Substances 0.000 description 2
- 238000009835 boiling Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 229910001220 stainless steel Inorganic materials 0.000 description 1
- 239000010935 stainless steel Substances 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
Landscapes
- Filtration Of Liquid (AREA)
Abstract
Description
【0001】0001
【産業上の利用分野】本発明は、メッキ処理液、誘電加
工処理液、研削用処理液等の処理液の濾過に使用される
垂直円筒型加圧管状型濾過機の濾材(濾過部材)の目詰
まりを防止するための濾滓の除去方法に関する。[Industrial Application Field] The present invention relates to a filter medium (filtration member) for a vertical cylindrical pressurized tubular filter used for filtering processing liquids such as plating processing liquids, dielectric processing processing liquids, and grinding processing liquids. The present invention relates to a method for removing filter slag to prevent clogging.
【0002】0002
【従来の技術】メッキ処理液、誘電加工処理液、研削用
処理液等の処理液の濾過に使用される垂直円筒型加圧管
状型濾過機は、円筒形の濾布の外周面に繊維、けい藻土
等の濾過材料が周設された濾過筒を有し、処理液をこの
筒に通すことにより、処理液中の塵挨、油垢等の除去が
行なわれる。濾過を繰り返し行なうことによって濾材に
詰まった塵挨、あるいは塵挨等が詰まって塵挨が強固に
付着した濾材(すなわち濾滓)を除去する方法としては
、例えば、濾材あるいは濾過筒を濾過機から外して洗浄
するという原始的な方法、あるいは新しい濾過筒と交換
する方法が行なわれていた。最近では、下記のような濾
滓の除去(または濾材の洗浄)方法が提案されている。[Prior Art] A vertical cylindrical pressurized tubular filter used for filtering processing liquids such as plating processing liquids, dielectric processing processing liquids, and grinding processing liquids has fibers on the outer peripheral surface of a cylindrical filter cloth. It has a filter cylinder surrounded by a filtering material such as diatomaceous earth, and by passing the processing liquid through this cylinder, dust, oil scale, etc. in the processing liquid are removed. As a method for removing dust that has become clogged in the filter medium due to repeated filtration, or filter medium that has become clogged with dust and has firmly adhered to it (i.e. filter slag), for example, remove the filter medium or filter cylinder from the filter machine. The primitive method of removing and cleaning the filter tube, or replacing it with a new filter tube was used. Recently, the following methods for removing filter dregs (or cleaning filter media) have been proposed.
【0003】(a)特開昭60−222117号公報に
は、下部にドレイン口と流入口とを有する液槽に、濾過
筒を浸漬し、該濾過筒は外筒と該外筒内と濾過部材を介
して連通し且つ清浄水の流出口を有する外筒上部の液溜
とからなる構造の濾過機を用いて、外筒と液相内面との
間に間隙を生じさせ、流入口と流出口とを閉じると共に
、液槽と濾過筒とを離間方向に相対移動させ、外筒下端
が間隙内の液面を越えることにより、液溜内の液を液槽
に急激に落下させて、濾滓を除去する洗浄方法が開示さ
れている。(a) Japanese Unexamined Patent Publication No. 60-222117 discloses that a filter cylinder is immersed in a liquid tank having a drain port and an inflow port at the bottom, and the filter cylinder has an outer cylinder, an inside of the outer cylinder, and a filter. Using a filter structure consisting of a liquid reservoir at the top of an outer cylinder that communicates through a member and has an outlet for clean water, a gap is created between the outer cylinder and the inner surface of the liquid phase, and the inlet and flow are separated. At the same time as closing the outlet, the liquid tank and the filter tube are moved relative to each other in the direction of separation, so that the lower end of the outer cylinder exceeds the liquid level in the gap, causing the liquid in the liquid reservoir to rapidly fall into the liquid tank and filtering. A cleaning method for removing scum is disclosed.
【0004】(b)特開昭61−101216号公報に
は、下部にドレイン口と流入口とを有する液槽を上下方
向の遮蔽板により主槽室と副槽室とに区画し、副槽室内
に空気抜け口を有し、遮蔽板の下端を濾過部材以下とし
、濾過部材以下で主槽室と副槽室とが連通し、副槽室内
の液面のレベル検知できるようにした濾過機を用いて、
流入口と流出口とを閉じ、空気抜口とドレイン口とを開
いて、副槽の液を流下させ、液面の所定レベルの検出と
同時に、液槽内の液を加圧して該液を急速に降下させ、
濾滓を除去する洗浄方法が開示されている。(b) Japanese Unexamined Patent Publication No. 101216/1983 discloses that a liquid tank having a drain port and an inlet at the bottom is divided into a main tank chamber and a sub-tank chamber by vertical shielding plates, and the sub-tank A filtration machine that has an air vent inside the room, the lower end of the shield plate is below the filtration member, the main tank chamber and the sub-tank chamber communicate with each other below the filtration member, and the liquid level in the sub-tank chamber can be detected. Using,
The inlet and the outlet are closed, the air vent and the drain port are opened, and the liquid in the sub-tank is allowed to flow down.At the same time as a predetermined level of the liquid level is detected, the liquid in the liquid tank is pressurized to remove the liquid. descend rapidly,
A cleaning method for removing slag is disclosed.
【0005】(c)特開昭61−238311号公報に
は、下部にドレイン口と流入口とを有する液槽を上下方
向の遮蔽板により主槽室と副槽室とに区画し、かつ主槽
室と副槽室とが隔室壁の下端方で連通し、主槽室に流出
口側を覆う濾過部材を設けると共に、主槽室に、ドレイ
ン口の開放による液槽内の液排出と同期させ、主槽室側
の液面を加圧する手段を備えた濾過機が開示されている
。(c) Japanese Patent Application Laid-Open No. 61-238311 discloses that a liquid tank having a drain port and an inlet at the bottom is divided into a main tank chamber and a sub-tank chamber by vertical shielding plates, and The tank chamber and the sub-tank chamber communicate with each other at the lower end of the partition wall, and the main tank chamber is provided with a filtration member that covers the outlet side, and the main tank chamber is provided with a filter for discharging the liquid in the liquid tank by opening a drain port. A filter is disclosed that includes means for synchronizing and pressurizing the liquid level on the main tank chamber side.
【0006】(d)特開昭61−242610号公報に
は、処理液の流入口を備えたタンク内に、外周面に外周
面に濾過材・布材等の濾材が周設された一個ないし複数
個の濾過筒を並列配置し、さらに、濾過筒と清浄液の流
出口を連通させた濾過機を用いて、流入口と流出口とを
遮断(閉)し、タンク内の処理液を抜き、各液溜室に加
圧空気を連通し、液溜室内の洗浄液を濾過部材から下方
に投下することにより濾滓を除去する方法が開示されて
いる。(d) Japanese Unexamined Patent Publication No. 61-242610 discloses that a filter medium such as a filter material or a cloth material is disposed around the outer circumferential surface of a tank provided with an inlet for processing liquid. Using a filter in which multiple filter cylinders are arranged in parallel, and the filter cylinders and the cleaning liquid outlet are communicated, the inlet and the outlet are shut off (closed), and the treated liquid in the tank is drained. , discloses a method for removing filter slag by communicating pressurized air to each liquid reservoir and dropping the cleaning liquid in the liquid reservoir downward from a filter member.
【0007】上記濾滓除去後に、再度濾過操作を行なう
時には、必要により濾過筒に新しい濾材を、不足分だけ
付着、形成させてから濾過を行なうことが一般的である
。[0007] When performing the filtration operation again after the above-mentioned filter dregs are removed, it is common to attach and form a new filter medium on the filter cylinder as necessary to cover the missing amount, and then perform filtration.
【0008】すなわち、上記(a)特開昭60−222
117号公報、(b)特開昭61−101216号公報
および(d)特開昭61−242610号公報には、濾
液等を一気に落としすことにより濾滓(塵挨および塵挨
の詰まった濾材等)を濾材から取り除き、これにより濾
滓の除去を行なう方法が開示されている。そして、上記
濾滓の除去は、(a)および(b)では濾過槽を隔室壁
で内側を主槽室、外側を副槽室に分け、副槽室の処理液
をエアーを通すことにより、予め処理液をある程度落し
、その形成された空隙を利用して主槽室の濾過液等を一
気に落す方法が用いられている。(d)は主槽室と副槽
室に分けていないが、上記と似た原理で濾過槽内の処理
液を先に除去し、その形成された空隙を利用して、濾過
液を一気に落とす方法が用いられている。[0008] That is, the above (a) JP-A-60-222
No. 117, (b) JP-A-61-101216, and (d) JP-A-61-242610 disclose that filter slag (filter material clogged with dust and etc.) from a filter medium, thereby removing filter slag. In (a) and (b), the filter slag is removed by dividing the filtration tank into a main tank chamber on the inside and a sub-tank chamber on the outside by partition walls, and passing air through the processing liquid in the sub-tank chamber. A method is used in which a certain amount of processing liquid is dropped in advance and the filtrate, etc. in the main tank chamber is dropped all at once using the gap formed. Although (d) is not divided into a main tank chamber and a sub-tank chamber, the process liquid in the filtration tank is first removed using a principle similar to the above, and the filtrate is dropped all at once by using the gap formed. method is used.
【0009】また(c)特開昭61−238311号公
報に開示の方法は、濾材によるドレイン口の目詰まりを
防止するもので、この方法では上記(a)、(b)とは
逆に主槽室の濾過液等をエアーを通すことにより先に処
理液をある程度落し、その空隙を利用して副槽室の処理
液を落としてドレイン口付近の液体を撹拌させることに
よりドレイン口の目詰まりを防止する。ここでは、濾滓
の除去は、上記のように主槽室の濾過液等にエアーを通
じること(すなわち逆洗)により行なわれている。Furthermore, (c) the method disclosed in JP-A No. 61-238311 is to prevent clogging of the drain port by the filter material, and in this method, contrary to the above (a) and (b), By passing air through the filtrate in the tank chamber, a certain amount of the processing liquid is dropped first, and then using that gap to drop the processing liquid in the sub-tank chamber to agitate the liquid near the drain port, which prevents clogging of the drain port. prevent. Here, the filter dregs are removed by passing air through the filtrate and the like in the main tank chamber (ie, backwashing) as described above.
【0010】これら(a)〜(d)の方法の中では、濾
滓の除去は上記(c)の公報に採用されている主槽室の
処理液等にエアーを通じる(すなわち逆洗)方法が、使
用する装置が比較的小さくなること、制御が簡単である
ことなどから、一般に利用されている。しかしながら、
上記方法では、濾過槽に処理液等が大量に入った状態で
逆洗するため、洗浄後もたらされる濾滓(塵挨および塵
挨の詰まった濾材)は処理液と混合されることから大量
となり、この処理に長時間を要することになる。このよ
うな混合物は、一般にフィルターを用いて脱水されてい
る。このように濾滓が大量となる問題は、前述したよう
に(a)(b)および(d)の方法においても存在する
。Among these methods (a) to (d), the filter dregs are removed by the method of passing air through the processing liquid in the main tank chamber (that is, backwashing), which is adopted in the above-mentioned publication (c). However, it is generally used because the equipment used is relatively small and the control is simple. however,
In the above method, the filtration tank is backwashed with a large amount of processing liquid, etc., so the filter slag (dust and dust-filled filter media) produced after washing is mixed with the processing liquid and becomes large. , this process will take a long time. Such mixtures are generally dehydrated using a filter. As described above, the problem of large amounts of filter dregs also exists in methods (a), (b), and (d).
【0011】従って、上記のような濾滓の除去方法のい
ずれを採用しても、ドレイン口から排出される濾滓を含
む廃液が、濾滓だけでなく処理液を含む大量なものとな
るため、大量の廃液を処理する必要となること、および
これを脱水するための脱水機が必要となることなどから
、全体の装置が大型、複雑なものとなるとの問題がある
。[0011] Therefore, no matter which of the above methods for removing filter dregs is adopted, a large amount of waste liquid containing filter dregs is discharged from the drain port, which includes not only filter dregs but also treated liquid. Since it is necessary to treat a large amount of waste liquid and a dehydrator is required to dehydrate it, there is a problem that the entire apparatus becomes large and complicated.
【0012】0012
【発明が解決しようとする課題】本発明は、濾滓の除去
操作によりドレイン口から排出される濾滓に処理液が含
有せず、その脱水を必要としない濾過装置の濾滓除去方
法を提供することを目的とする。また、本発明は、濾滓
の除去操作によりドレイン口から排出される濾滓に含ま
れる処理液の含有量が少なく、その脱水が容易な濾過装
置の簡便な濾滓除去方法を提供することを目的とする。[Problems to be Solved by the Invention] The present invention provides a method for removing slag from a filtration device in which the slag discharged from the drain port during the sludge removal operation does not contain processing liquid and does not require dehydration. The purpose is to Further, the present invention provides a simple method for removing filter slag from a filtration device, in which the content of processing liquid contained in the slag discharged from the drain port during the sludge removal operation is small, and the dewatering of the slag is easy. purpose.
【0013】[0013]
【課題を解決するための手段】上記目的は、濾過槽、そ
の上方に設けられた液溜、および該液溜の下面開口部に
、該濾過槽と該液溜とを連通するように設けられた、濾
材が外周面に周設された一個ないし複数個の濾過筒から
なる濾過装置の濾過筒に形成された濾滓の除去を、(1
) 処理液槽からの処理液の流入を停止させ、濾過操作
により濾過筒に形成された濾滓が離脱しないように、少
なくとも濾過筒内の圧力と同等の圧力を有するエアーを
濾過槽側壁から導入する工程、(2) エアーを供給し
ながら濾過筒内および該液溜内の濾液と、濾過槽内の処
理液とを排出する工程、(3) エアーの供給を間断な
く続けることにより、濾液および処理液を排出して濾過
槽内、濾過筒に周設された濾材および濾滓を液相のない
乾燥または準乾燥状態にする工程、および(4) 液溜
側壁からエアーを供給して、濾過筒に付着している濾滓
を排出する工程、により行うことを特徴とする濾過装置
の濾滓除去方法により達成することができる。[Means for Solving the Problems] The above object is to provide a filter tank, a liquid reservoir provided above the filter tank, and a lower opening of the liquid tank so as to communicate the filter tank and the liquid tank. In addition, the removal of filter slag formed on the filter tube of a filter device consisting of one or more filter tubes with filter media disposed around the outer circumferential surface is performed using (1)
) Stop the inflow of the processing liquid from the processing liquid tank, and introduce air from the side wall of the filter tank with a pressure at least equivalent to the pressure inside the filter cylinder so that the filter slag formed in the filter cylinder during the filtration operation does not come off. (2) discharging the filtrate in the filtration cylinder and the liquid reservoir, and the treated liquid in the filtration tank while supplying air; (3) by continuously supplying air, the filtrate and (4) supplying air from the side wall of the liquid reservoir to carry out filtration; This can be achieved by a method for removing filter dregs from a filtration device, which is characterized by a step of discharging filter dregs adhering to a cylinder.
【0014】本発明の濾過装置の濾滓除去方法の好まし
い態様は以下のとおりである。[0014] Preferred embodiments of the method for removing filter dregs from the filtration device of the present invention are as follows.
【0015】1)上記(1) のエアーを導入する工程
において、該液溜側も通気状態におくことを特徴とする
上記濾過装置の濾滓除去方法。1) A method for removing slag from the filtration device described above, characterized in that in the step of introducing air in the above (1), the liquid reservoir side is also placed in a ventilated state.
【0016】2)該液溜に濾液の流出口を設け、該供給
されたエアーを排出することを特徴とする上記濾過装置
の濾滓除去方法。2) A method for removing slag from the filtration device described above, characterized in that the liquid reservoir is provided with a filtrate outlet and the supplied air is discharged.
【0017】3)該液溜に濾液の流出口を設け、該流出
口から濾液をほぼ流出させた後、上記(2) の処理液
および濾液を排出する工程に移ることを特徴とする上記
濾過装置の濾滓除去方法。3) The above filtration characterized in that the liquid reservoir is provided with an outlet for the filtrate, and after most of the filtrate has flowed out from the outlet, the process proceeds to the step (2) of discharging the treated solution and the filtrate. How to remove slag from the device.
【0018】4)上記(2) の処理液および濾液を排
出する工程において、該液溜側も通気状態におくことを
特徴とする上記濾過装置の濾滓除去方法。4) A method for removing slag from the above-mentioned filtration device, characterized in that in the step of discharging the treated liquid and filtrate in the above (2), the liquid reservoir side is also kept in an aerated state.
【0019】5)該濾過槽下部に排出口を設け、この排
出口を利用し上記(2) の処理液および濾液を排出す
ることを特徴とする上記濾過装置の濾滓除去方法。5) A method for removing slag from the filtration device, characterized in that a discharge port is provided at the bottom of the filtration tank, and the treated liquid and filtrate of (2) above are discharged using this discharge port.
【0020】6)上記(4) の濾過筒の濾滓を排出す
る工程で、液溜側からエアーを供給を、該濾過槽側壁か
らのエアーの供給を停止した後行なうことを特徴とする
上記濾過装置の濾滓除去方法。6) The above method characterized in that in the step of discharging the filter dregs from the filter cylinder in the above (4), air is supplied from the liquid reservoir side after the air supply from the side wall of the filter tank is stopped. Method for removing slag from a filtration device.
【0021】7)上記(4) の濾過筒の濾滓を排出す
る工程で、液溜側壁からエアーの供給を該濾過槽側から
のエアーの供給を停止した後行ない、そして該濾滓が濾
過槽下部に落下した後再度濾過槽側からのエアーの供給
することを特徴とする上記濾過装置の濾滓除去方法。7) In the step of discharging the filter slag from the filter cylinder in (4) above, air is supplied from the side wall of the liquid reservoir after the air supply from the filtration tank side is stopped, and the filter slag is filtered. A method for removing filter slag from a filtration device as described above, characterized in that air is again supplied from the filtration tank side after the slag has fallen to the bottom of the tank.
【0022】また、上記目的は、濾過槽、その上方に設
けられた液溜および該液溜の下面開口部に、該濾過槽と
該液溜とを連通するように設けられた、濾材が外周面に
周設された一個ないし複数個の濾過筒からなる、濾過装
置の濾過筒に形成された濾滓の除去を、(1) 処理液
の流入を停止させ、濾過操作により濾過筒に形成された
濾滓が離脱しないように少なくとも濾過筒内の圧力と同
等の圧力を有するエアーを濾過槽側から導入する工程、
(2) エアーを供給しながら濾過筒内および該液溜内
の濾液と、濾過槽内の処理液とを、濾過槽下部に少量残
して、ほとんど排出する工程、(3) 濾過槽内に処理
液および濾液が残った状態で、エアーの供給を間断なく
続けることにより、濾過筒に周設された濾材および濾滓
を液相のない乾燥または準乾燥状態にする工程、および
(4)液溜側からエアーを供給して濾過筒の濾滓を落下
させ、濾滓と処理液とを混合して排出する工程、により
行うことを特徴とする濾過装置の濾滓除去方法によって
も達成することができる。[0022] Also, the above object is to provide a filtration tank, a liquid reservoir provided above the filtration tank, and a filter medium provided at the bottom opening of the liquid reservoir so as to communicate with the filtration tank and the liquid reservoir. Removal of filter slag formed on the filtration cylinder of a filtration device, which consists of one or more filtration cylinders installed around the surface, is carried out by (1) stopping the inflow of the processing liquid and removing the slag formed on the filtration cylinder by the filtration operation. a step of introducing air having a pressure at least equivalent to the pressure inside the filter cylinder from the filter tank side so that the filter slag does not separate;
(2) A process in which most of the filtrate in the filtration cylinder and the liquid reservoir and the treated liquid in the filtration tank are discharged while supplying air, leaving a small amount at the bottom of the filtration tank; (3) Processing in the filtration tank; (4) a step of bringing the filter medium and filter slag surrounding the filter cylinder into a dry or semi-dry state without a liquid phase by continuously supplying air while the liquid and filtrate remain; This can also be achieved by a method for removing slag from a filtration device, which is characterized by a step of supplying air from the side to cause the slag in the filter cylinder to fall, mixing the sludge with the treatment liquid, and discharging the mixture. can.
【0023】上記本発明の濾過装置の濾滓除去方法の好
ましい態様は以下のとおりである。Preferred embodiments of the method for removing filter dregs from the filtration apparatus of the present invention are as follows.
【0024】1)上記(1) のエアーを導入する工程
において、該液溜側も通気状態におくことを特徴とする
上記濾過装置の濾滓除去方法。1) A method for removing slag from the filtration device described above, characterized in that in the step of introducing air in the above (1), the liquid reservoir side is also placed in a ventilated state.
【0025】2)上記(2) の処理液および濾液を排
出する工程において、該液溜側も通気状態におくことを
特徴とする上記濾過装置の濾滓除去方法。2) A method for removing slag from a filtration device as described above, characterized in that in the step of discharging the treated liquid and filtrate in the above (2), the liquid reservoir side is also kept in an aerated state.
【0026】3)該液溜に濾液の流出口を設け、該流出
口からエアーの供給量の一部を排出することを特徴とす
る上記濾過装置の濾滓除去方法。3) A method for removing slag from the filtration device described above, characterized in that the liquid reservoir is provided with an outlet for the filtrate, and a part of the air supply is discharged from the outlet.
【0027】4)該濾過槽下部に排出口を設け、この排
出口を利用し上記(2) の処理液および濾液を排出す
ることを特徴とする上記濾過装置の濾滓除去方法。4) A method for removing slag from the above-mentioned filtration device, characterized in that a discharge port is provided at the bottom of the filtration tank, and the treated liquid and filtrate of the above (2) are discharged using the discharge port.
【0028】5)上記(4) の濾過筒の濾滓と処理液
との混合物を排出する工程で、液溜側からエアーを供給
を、該濾過槽側からのエアーの供給を停止した後行なう
ことを特徴とする上記濾過装置の濾滓除去方法。5) In the step of discharging the mixture of filter dregs and treated liquid from the filter cylinder in (4) above, supplying air from the liquid reservoir side is carried out after stopping the supply of air from the filter tank side. A method for removing slag from the above-mentioned filtration device.
【0029】6)上記(4) の濾過筒の濾滓と処理液
との混合物を排出する工程で、液溜側からエアーの供給
を、該濾過槽側からのエアーの供給を停止した後行ない
、濾滓が該濾過槽下部に落下した後再度該濾過槽側から
のエアーの供給することを特徴とする上記濾過装置の濾
滓除去方法。6) In the step of discharging the mixture of filter dregs and treated liquid from the filter cylinder in (4) above, supplying air from the liquid reservoir side is carried out after stopping the supply of air from the filter tank side. . A method for removing slag from a filtration device as described above, characterized in that air is supplied from the filtration tank side again after the slag falls to the lower part of the filtration tank.
【0030】[0030]
【実施例】本発明の一実施例を添付図1〜図5を参照し
ながら詳しく説明する。図1に、濾過槽1、その上方に
設けられた液溜2およびこれらを連通するように設けら
れた濾材が周設された濾過筒4からなる基本構成を有す
る濾過装置の断面図を示す。液溜2は、濾過槽1上部に
開口部3を有する蓋板6を介して固定されている。濾過
槽1には、側壁に処理液槽(図示せず)から導入される
処理液の流入口11および一次側エアー供給口12、そ
して下部にドレイン口13および処理液の排出口14が
設けられている。処理液の流入口11は開閉弁11V、
一次側エアー供給口12は開閉弁12V、ドレイン口1
3は開閉弁13Vおよび処理液の排出口14は開閉弁1
4Vをそれぞれ具備している。液溜2には、壁面に濾液
の流出口15と二次側エアー口16とが設けられている
。濾液の流出口15は開閉弁15V、二次側エアー口1
6は開閉弁16Vをそれぞれ具備している。そして、液
溜2の下面開口部3(すなわち蓋板6の開口部3に当た
る)に、濾過槽1と液溜2とを連通するように濾材が外
周面に周設された濾過筒4が設けられている。濾過筒は
、濾過を効率良く行なうために複数個でも良い。濾過筒
は、一般に、濾布に、繊維材、布材、硅藻土等の濾過材
料がコーティングされたものである。濾材とは、本発明
では、濾布および繊維材、布材、硅藻土等の濾過材料を
いう。濾過槽1には処理液が満たされており、液溜2内
と濾過筒4内には濾過された処理液が満たされている。DESCRIPTION OF THE PREFERRED EMBODIMENTS An embodiment of the present invention will be described in detail with reference to the attached FIGS. 1 to 5. FIG. 1 shows a cross-sectional view of a filtration device having a basic configuration consisting of a filtration tank 1, a liquid reservoir 2 provided above the filtration tank 1, and a filtration cylinder 4 around which a filter medium is provided so as to communicate these. The liquid reservoir 2 is fixed to the upper part of the filtration tank 1 via a lid plate 6 having an opening 3. The filtration tank 1 is provided with an inlet 11 for a processing liquid introduced from a processing liquid tank (not shown) and a primary air supply port 12 on the side wall, and a drain port 13 and an outlet 14 for the processing liquid at the lower part. ing. The processing liquid inlet 11 is an on-off valve 11V,
The primary side air supply port 12 has an on-off valve 12V, and a drain port 1
3 is the on-off valve 13V, and the processing liquid discharge port 14 is the on-off valve 1
Each is equipped with 4V. The liquid reservoir 2 is provided with a filtrate outlet 15 and a secondary air port 16 on the wall surface. The filtrate outlet 15 has an on-off valve 15V and a secondary air port 1.
6 is equipped with an on-off valve of 16V. A filter cylinder 4 with a filter material surrounding the outer circumferential surface is provided at the lower opening 3 of the liquid reservoir 2 (that is, corresponding to the opening 3 of the lid plate 6) so as to communicate the filter tank 1 and the liquid reservoir 2. It is being A plurality of filter cylinders may be used for efficient filtration. A filter tube is generally a filter cloth coated with a filtering material such as a fiber material, cloth material, diatomaceous earth, or the like. In the present invention, the term "filter medium" refers to filter cloth and filtration materials such as fiber materials, cloth materials, and diatomaceous earth. A filtration tank 1 is filled with a processing liquid, and a liquid reservoir 2 and a filter cylinder 4 are filled with filtered processing liquid.
【0031】図2に、上記濾過材料が被覆された濾過筒
4の拡大断面図を示す。濾過筒は、円筒形の濾布21の
外周面が硅藻土22により被覆された構造を有し、濾過
筒の内壁にスプリング23が水平方向に固着されている
。スプリングはなくても良いが、濾滓(塵埃、濾材)の
脱離を促進するので、装着されている方が好ましい。
スプリングは、一般にステンレス製で、その形状は、長
さが一般に300〜2000mm、スプリング径は一般
に10〜100mmの範囲である。FIG. 2 shows an enlarged sectional view of the filter tube 4 coated with the above-mentioned filter material. The filter tube has a structure in which the outer peripheral surface of a cylindrical filter cloth 21 is covered with diatomaceous earth 22, and a spring 23 is fixed horizontally to the inner wall of the filter tube. Although the spring may not be provided, it is preferable that the spring be installed, since it facilitates the removal of filter slag (dust, filter material). The spring is generally made of stainless steel, has a length generally in the range of 300 to 2000 mm, and a spring diameter generally in the range of 10 to 100 mm.
【0032】上記濾過装置を用いて処理液の濾過は次の
ように行なわれる。まず、処理液の濾過を行なう前に、
通常、濾過助剤を濾過筒4に下記のようにしてコーティ
ングを行なう。Filtration of the treated liquid using the above-mentioned filtration device is carried out as follows. First, before filtering the treatment liquid,
Usually, the filter cylinder 4 is coated with a filter aid as follows.
【0033】濾過槽1のドレイン口13の開閉弁13V
を閉じ、濾過助剤(硅藻土など)分散液の槽(図示せず
)に管路を切り換えて、濾過助剤分散液を、開閉弁11
Vを開いてポンプにより処理液の流入口11から濾過槽
1内に導入する。分散液は、濾過筒4(この場合はまだ
濾布の状態にある)の外周部に硅藻土を付着させながら
濾過筒4を通過し、濾過液の流出口14から排出される
。そして、この分散液を、再び循環路を経て濾過筒4を
通過させる。このようにして、所望の量の硅藻土を濾過
筒4の外周に付着させる。[0033] Opening/closing valve 13V of drain port 13 of filtration tank 1
, switch the pipe line to a tank (not shown) for filter aid (diatomaceous earth, etc.) dispersion liquid, and transfer the filter aid dispersion liquid to the on-off valve 11.
V is opened and the processing liquid is introduced into the filtration tank 1 from the inlet 11 by the pump. The dispersion liquid passes through the filter tube 4 while adhering diatomaceous earth to the outer periphery of the filter tube 4 (still in the state of a filter cloth in this case), and is discharged from the filtrate outlet 14. Then, this dispersion liquid is passed through the filter cylinder 4 via the circulation path again. In this way, a desired amount of diatomaceous earth is attached to the outer periphery of the filter cylinder 4.
【0034】次いで、処理液の濾過は次のように行なわ
れる。処理液の槽(図示せず)に管路を切り換えて、処
理液を、開閉弁11Vを開き、ポンプを用いることによ
り処理液の流入口11から濾過槽1内に導入する。処理
液は、外周部に硅藻土が充分付着した濾過筒4を通過し
、濾過液の流出口14から流出する。これにより、処理
液は濾過されて塵埃等が除去され、濾過筒4の外周部の
濾過助剤に塵埃等が吸着される。この処理時には、一般
に一次側エアー供給口12の開閉弁12V、ドレイン口
13の開閉弁13Vおよび二次側エアー口16は開閉弁
16Vは閉じた状態におく。Next, the treatment liquid is filtered as follows. The pipe line is switched to a treatment liquid tank (not shown), and the treatment liquid is introduced into the filtration tank 1 from the treatment liquid inlet 11 by opening the on-off valve 11V and using a pump. The treatment liquid passes through the filter cylinder 4 to which diatomaceous earth is sufficiently adhered to the outer periphery, and flows out from the filtrate outlet 14. As a result, the processing liquid is filtered to remove dust and the like, and the dust and the like are adsorbed by the filter aid on the outer periphery of the filter cylinder 4 . During this process, the on-off valve 12V of the primary air supply port 12, the on-off valve 13V of the drain port 13, and the on-off valve 16V of the secondary air port 16 are generally kept closed.
【0035】上記濾過処理を長時間続けるうちに、濾過
筒4の濾布およびその外周部に付着した硅藻土や繊維に
塵埃等が蓄積し、目詰まりを起こすようになる。このた
め、処理液の流入口11の処理液を供給するための圧力
が所定の値(例えば、3kg・f/cm2 )に達した
ところで、本発明の濾過装置の濾滓除去を行なう。As the above-mentioned filtration process continues for a long time, dust and the like accumulate on the filter cloth of the filter tube 4 and on the diatomaceous earth and fibers attached to its outer circumference, causing clogging. Therefore, when the pressure for supplying the processing liquid at the processing liquid inlet 11 reaches a predetermined value (for example, 3 kg·f/cm<2>), the filter slag of the filtration apparatus of the present invention is removed.
【0036】上記図1の濾過装置の濾材の洗浄は、例え
ば下記のように行なわれる。
(1) 濾過液の流出口15の開閉弁15Vを開いたま
ま、流入口11の開閉弁11Vを閉じて処理液の流入を
止める。次いで、一次側エアー口の開閉弁12Vを開い
て一次側エアー口12から流入口11での処理液の液圧
より高い圧力のエアーを加える。ここでは、硅藻土等の
濾過材料の脱落を防止しながら、濾液を流出口より、そ
の一部または大部分を排出する。The cleaning of the filter medium of the filter device shown in FIG. 1 is carried out, for example, as follows. (1) While the on-off valve 15V on the filtrate outlet 15 remains open, the on-off valve 11V on the inlet 11 is closed to stop the inflow of the processing liquid. Next, the on-off valve 12V of the primary air port is opened to apply air at a pressure higher than the liquid pressure of the processing liquid at the inlet 11 from the primary air port 12. Here, part or most of the filtrate is discharged from the outlet while preventing the filter material such as diatomaceous earth from falling off.
【0037】(2) 一次側エアー口12よりエアーの
供給を続けながら、処理液の排出口14の開閉弁14V
を開いて、濾過槽1内の処理液、濾過筒4内および該液
溜2内に残った濾液を排出口14より排出する。この時
、濾過液の流出口15の開閉弁15Vは開いたままの方
が排出が円滑に行なわれるので好ましい。図3に、上記
処理液を排出口より排出する途中の状態を示す。7は、
処理液の表面の位置である液位を示す。一次側エアー口
12よりエアーは、濾過筒4を通って液溜2の上部に溜
ってゆき、処理液だけでなく、上記(1) の工程で流
出しなかった濾過筒4内および該液溜2内の濾液は処理
液の排出口14より排出される。この排出される処理液
には、塵埃、硅藻土や繊維(濾過材料)あるいは濾布の
材料は殆ど含まれていない。これは、一次側エアー口1
2よりのエアー供給により、濾過筒4からの塵埃や濾材
の脱落を防いでいるためである。処理液の排出口14よ
り排出され処理液等は処理液槽に戻され、再度濾過され
る。(2) While continuing to supply air from the primary side air port 12, open and close the on-off valve 14V of the processing liquid discharge port 14.
The processing liquid in the filtration tank 1 and the filtrate remaining in the filtration cylinder 4 and the liquid reservoir 2 are discharged from the outlet 14. At this time, it is preferable for the on-off valve 15V of the filtrate outlet 15 to remain open because the discharge can be carried out smoothly. FIG. 3 shows a state in which the processing liquid is being discharged from the discharge port. 7 is
Indicates the liquid level, which is the position of the surface of the processing liquid. Air from the primary side air port 12 passes through the filter tube 4 and accumulates in the upper part of the liquid reservoir 2, and not only the processing liquid but also the inside of the filter tube 4 that did not flow out in the step (1) above and the liquid reservoir. The filtrate in 2 is discharged from the processing liquid discharge port 14. This discharged processing liquid hardly contains dust, diatomaceous earth, fibers (filter material), or filter cloth materials. This is the primary air port 1
This is because the air supply from 2 prevents dust and filter media from falling off from the filter cylinder 4. The processing liquid and the like discharged from the processing liquid discharge port 14 are returned to the processing liquid tank and filtered again.
【0038】(3) 処理液等が排出された後も一次側
エアー口12からエアーの供給を間断なく続けることに
より、濾過槽内及び周設された濾材を液相のない乾燥ま
たは準乾燥状態にする。処理液は、そこに含まれる液体
が、水、あるいは水と同程度の沸点の液体で媒質も粘着
性を有しないものであることが、濾滓として粘着性のな
い固体状のものが得られ易く好ましい。従って、得られ
る濾滓が粘着性(例えば油性成分が多い)の場合は、後
述する濾滓除去方法を用いることが好ましい。(3) By continuing to supply air continuously from the primary air port 12 even after the processing liquid, etc. is discharged, the inside of the filtration tank and the surrounding filter medium are kept in a dry or semi-dry state with no liquid phase. Make it. The processing liquid must be water or a liquid with a boiling point similar to that of water, and the medium must be non-adhesive so that a non-adhesive solid can be obtained as the filtrate. Easy and preferable. Therefore, if the resulting filter cake is sticky (for example, contains a large amount of oily components), it is preferable to use the filter cake removal method described below.
【0039】(4) 一次側エアー口12からのエアー
の供給を停止し、二次側エアー口16の開閉弁16Vを
開いてエアーを供給すると共に、ドレイン口4のを開口
して、開閉弁16Vを開いてエアーの付与により落下し
た濾滓(塵埃および濾材)を該ドレイン口より排出する
。
図4に、落下した濾滓を該ドレイン口より排出する状態
を示す。8は、濾過槽下部に落下した濾滓を示す。この
ようにして、乾燥した濾滓はドレイン口より良好に排出
される。(4) Stop the supply of air from the primary air port 12, open the on-off valve 16V of the secondary air port 16 to supply air, open the drain port 4, and close the on-off valve 16V. 16V is opened and the filter slag (dust and filter material) that has fallen due to the application of air is discharged from the drain port. FIG. 4 shows a state in which the fallen filter dregs are discharged from the drain port. 8 shows the filter slag that has fallen to the bottom of the filter tank. In this way, the dried filter cake can be better discharged from the drain port.
【0040】(5) 二次側エアー口からのエアーの供
給のままあるいは停止して、一次側エアー口12からエ
アーを加えることにより、該(4) 工程で排出されな
かった濾滓を該ドレイン4よりの排出する。該(4)
工程で濾滓が排出された場合は、この工程を行なう必要
はない。(5) By continuing or stopping the air supply from the secondary air port and adding air from the primary air port 12, the filter slag that was not discharged in the step (4) is removed from the drain. Discharge from 4. (4)
If the process discharges filter cake, there is no need to perform this step.
【0041】一方、上記処理液が、例えば油性成分が主
体である場合は、濾材の完全な乾燥が難しく、濾滓(濾
材および塵埃)が粘着性を帯びた(ドロドロした)状態
となり易い。その際は、上記(3) 工程において処理
液を完全に排出しないで濾過槽下部に適量を残しておき
、下記の工程(6) 〜(8)に移ることが好ましい。On the other hand, if the treatment liquid is mainly composed of oily components, for example, it is difficult to completely dry the filter medium, and the filter slag (filter medium and dust) tends to become sticky (mushy). In that case, it is preferable to leave an appropriate amount of the treatment liquid at the bottom of the filtration tank in step (3) above without completely draining it, and then move on to steps (6) to (8) below.
【0042】(6) 処理液等が排出後、一次側エアー
口12からエアーの供給を間断なく続けることにより、
周設された濾材を液相のほとんどない準乾燥状態にする
。(6) After the processing liquid etc. are discharged, by continuing to supply air from the primary side air port 12 without interruption,
The surrounding filter medium is brought to a semi-dry state with almost no liquid phase.
【0043】(7) 一次側エアー口12からのエアー
の供給を停止し、二次側エアー口16の開閉弁16Vを
開いてエアーを供給すると共に、ドレイン口4のを開口
して、開閉弁16Vを開き、エアーの付与により濾滓を
脱落させ、且つ濾滓と濾過槽下部に残した処理液とを混
合しながらを該ドレインより排出する。図5は、濾滓と
濾過槽下部に残した処理液とを混合しながらをドレイン
より排出する状態を示す図である。8は、濾滓と処理液
との混合物を示す。(7) Stop the supply of air from the primary air port 12, open the on-off valve 16V of the secondary air port 16 to supply air, and open the drain port 4 and close the on-off valve 16V. 16V is opened, the filter dregs are dropped by applying air, and the filter dregs and the processing liquid left at the bottom of the filtration tank are mixed and discharged from the drain. FIG. 5 is a diagram showing a state in which the filter dregs and the processing liquid left at the bottom of the filtration tank are mixed and discharged from the drain. 8 shows a mixture of filter cake and treatment liquid.
【0044】(8) 二次側エアー口16からのエアー
の供給のままあるいは停止して、一次側エアー口12か
らエアーを加えることにより、該(4) 工程で排出さ
れなかった濾材および処理液を該ドレイン4よりの排出
する。(8) By continuing or stopping the air supply from the secondary air port 16 and adding air from the primary air port 12, the filter medium and processing liquid that were not discharged in the step (4) can be removed. is discharged from the drain 4.
【0045】このようにして、本発明の濾滓除去を行な
うことができる。[0045] In this way, the slag removal of the present invention can be carried out.
【0046】本発明の濾過装置の濾滓除去方法は、上記
図1に示す構造を有する濾過装置に限定されるものでは
なく、濾材が周設された濾過筒を用いて処理液を濾過す
る装置であれば、本発明の除去方法を利用することがで
きる。The method for removing slag from a filtration device according to the present invention is not limited to the filtration device having the structure shown in FIG. If so, the removal method of the present invention can be used.
【0047】[0047]
【発明の効果】濾過槽と、その上方に設けられた液溜お
よびこれらを連通するように設けられた外周面に濾材(
繊維、けい藻土等の濾過部材)が周設された濾過筒とか
らなる基本構成を有する濾過装置(いわゆる垂直円筒型
加圧管状濾過機)における濾材の洗浄方法は、濾過液側
からエアーを通じる(すなわち逆洗)方法が一般的であ
るが、本発明では、濾過液および処理液は先に排出した
後、濾滓である塵埃及び濾材を乾燥または準乾燥状態に
して排出する。Effect of the invention: A filter medium (
The cleaning method for the filter media in a filtration device (so-called vertical cylindrical pressurized tubular filter), which has a basic configuration consisting of a filtration cylinder surrounded by a filtration material (filtering material such as fibers or diatomaceous earth), is to blow air from the filtrate side. In the present invention, the filtrate and the treated liquid are first discharged, and then the filter material, which is the filter residue, is dried or semi-dry and then discharged.
【0048】これにより、排出された濾滓(塵挨および
塵挨の詰まった濾材)は処理液と混合されることがない
か、または殆どないことから、得られる濾滓の量は少量
である。さらに、濾滓を処理液と混合しない場合は、濾
滓を脱水する必要がなく、また、処理液と混合する場合
も、その量は極めて少なく脱水するとしても極めて短時
間で行なうことができる。従って、本発明の濾材の濾滓
除去を用いることにより、濾過を効率良く行なうことが
できる。さらに、この除去方法を利用すれば、脱水機を
不要とすることもできるので、濾過機を含む全体の装置
が小型で簡素なものにすることができる。[0048] As a result, the discharged filter slag (dust and dust-filled filter media) is not or hardly mixed with the processing liquid, so the amount of filter slag obtained is small. . Further, if the filter cake is not mixed with the treatment liquid, there is no need to dehydrate the filter cake, and even if the filter cake is mixed with the treatment liquid, the amount thereof is extremely small and even if it is dehydrated, it can be carried out in a very short time. Therefore, by using the slag removal method of the filter medium of the present invention, filtration can be performed efficiently. Furthermore, if this removal method is used, a dehydrator can be made unnecessary, so the entire device including the filter can be made small and simple.
【図1】図1は、濾過槽、その上方に設けられた液溜お
よびこれらを連通するように設けられたが周設された濾
過筒、からなる基本構成を有する濾過装置の断面図で、
本発明の濾過装置の濾滓除去方法の一実施態様を説明す
るための図である。FIG. 1 is a cross-sectional view of a filtration device having a basic configuration consisting of a filtration tank, a liquid reservoir provided above the filtration tank, and a filtration cylinder provided around the periphery to communicate these.
FIG. 2 is a diagram for explaining one embodiment of a method for removing filter dregs from a filtration device of the present invention.
【図2】図2は、上記図1の濾過材料が被覆された濾過
筒4の拡大断面図である。FIG. 2 is an enlarged sectional view of the filter tube 4 coated with the filter material of FIG. 1 above.
【図3】図3は、上記濾滓除去方法の一実施態様におい
て、処理液を排出する途中の状態を示す図である。FIG. 3 is a diagram showing a state in the middle of discharging the processing liquid in one embodiment of the above-mentioned filter dregs removal method.
【図4】図4は、上記濾滓除去方法の一実施態様におい
て、図3の続く工程の、落下させた濾滓をドレイン口よ
り排出する状態を示す図である。FIG. 4 is a diagram showing a state in which the fallen filter dregs are discharged from the drain port in the step following FIG. 3 in one embodiment of the above-mentioned filter dregs removal method.
【図5】図5は、上記図1〜4の濾滓除去方法と別の実
施態様で、上記図1の濾過装置を用いて、濾滓と濾過槽
下部に残した処理液とを混合しながらをドレイン口より
排出する状態を示す図である。FIG. 5 shows another embodiment of the filter slag removal method shown in FIGS. 1 to 4 above, in which the filter dregs and the treated liquid left at the bottom of the filtration tank are mixed using the filtration device shown in FIG. 1. FIG.
1 濾過槽 2 液溜 4 濾過筒 6 蓋板 11 処理液の流入口11 12 一次側エアー口 13 ドレイン口13 14 処理液の排出口 15 流出口 16 二次側エアー口 1 Filtration tank 2 Liquid reservoir 4 Filter cylinder 6 Lid plate 11 Processing liquid inlet 11 12 Primary side air port 13 Drain port 13 14 Processing liquid outlet 15 Outlet 16 Secondary air port
Claims (2)
および該液溜の下面開口部に、該濾過槽と該液溜とを連
通するように設けられた、濾材が外周面に周設された一
個ないし複数個の濾過筒からなる濾過装置の濾過筒に形
成された濾滓の除去を、(1) 処理液槽からの処理液
の流入を停止させ、濾過操作により濾過筒に形成された
濾滓が離脱しないように、少なくとも濾過筒内の圧力と
同等の圧力を有するエアーを濾過槽側壁から導入する工
程、(2) エアーを供給しながら濾過筒内および該液
溜内の濾液と、濾過槽内の処理液とを排出する工程、(
3) エアーの供給を間断なく続けることにより、濾液
および処理液を排出して濾過槽内、濾過筒に周設された
濾材および濾滓を液相のない乾燥または準乾燥状態にす
る工程、および(4) 液溜側壁からエアーを供給して
、濾過筒に付着している濾滓を排出する工程、により行
うことを特徴とする濾過装置の濾滓除去方法。[Claim 1] A filtration tank, a liquid reservoir provided above the filtration tank,
and a filtration cylinder of a filtration device, which is provided at a lower opening of the liquid reservoir so as to communicate the filtration tank and the liquid reservoir, and includes one or more filter cylinders with a filter medium disposed around the outer peripheral surface. (1) Stop the flow of the processing liquid from the processing liquid tank, and reduce the pressure inside the filter cylinder at least so that the filter slag formed in the filter cylinder by the filtration operation does not come off. a step of introducing air having the same pressure from the side wall of the filtration tank; (2) a step of discharging the filtrate in the filtration cylinder and the liquid reservoir and the treated liquid in the filtration tank while supplying air;
3) A step in which the filtrate and the treated liquid are discharged by continuously supplying air to bring the inside of the filtration tank, the filter media and filter slag surrounding the filtration tube into a dry or semi-dry state without a liquid phase, and (4) A method for removing filter slag from a filtration device, characterized by carrying out the step of supplying air from the side wall of the liquid reservoir and discharging the filter slag adhering to the filter cylinder.
よび該液溜の下面開口部に、該濾過槽と該液溜とを連通
するように設けられた、濾材が外周面に周設された一個
ないし複数個の濾過筒からなる、濾過装置の濾過筒に形
成された濾滓の除去を、(1) 処理液の流入を停止さ
せ、濾過操作により濾過筒に形成された濾滓が離脱しな
いように少なくとも濾過筒内の圧力と同等の圧力を有す
るエアーを濾過槽側から導入する工程、(2) エアー
を供給しながら濾過筒内および該液溜内の濾液と、濾過
槽内の処理液とを、濾過槽下部に少量残して、ほとんど
排出する工程、(3) 濾過槽内に処理液および濾液が
残った状態で、エアーの供給を間断なく続けることによ
り、濾過筒に周設された濾材および濾滓を液相のない乾
燥または準乾燥状態にする工程、および(4) 液溜側
からエアーを供給して濾過筒の濾滓を落下させ、濾滓と
処理液とを混合して排出する工程、により行うことを特
徴とする濾過装置の濾滓除去方法。2. A filter medium is provided around the outer peripheral surface of a filtration tank, a liquid reservoir provided above the filtration tank, and a lower opening of the liquid reservoir so as to communicate the filtration tank and the liquid reservoir. (1) Stop the inflow of the processing liquid and remove the slag formed on the filter cylinders by the filtration operation. A step of introducing air having a pressure at least equivalent to the pressure inside the filtration cylinder from the filtration tank side to prevent separation, (2) While supplying air, the filtrate in the filtration cylinder and the liquid reservoir, and the filtrate in the filtration tank. (3) With the processing liquid and filtrate remaining in the filtration tank, by continuing to supply air without interruption, the process of discharging most of the processing liquid, leaving a small amount at the bottom of the filtration tank. (4) supplying air from the liquid reservoir side to drop the filter slag in the filter cylinder, and mixing the filter slag with the treatment liquid; 1. A method for removing slag from a filtration device, the method comprising: removing slag from a filtration device;
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP3056040A JPH04271802A (en) | 1991-02-26 | 1991-02-26 | Method for removing cake in filter |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP3056040A JPH04271802A (en) | 1991-02-26 | 1991-02-26 | Method for removing cake in filter |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH04271802A true JPH04271802A (en) | 1992-09-28 |
Family
ID=13015972
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP3056040A Withdrawn JPH04271802A (en) | 1991-02-26 | 1991-02-26 | Method for removing cake in filter |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH04271802A (en) |
-
1991
- 1991-02-26 JP JP3056040A patent/JPH04271802A/en not_active Withdrawn
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| US2423172A (en) | Backwashing means for filtering apparatus by reverse flow of filtrate | |
| US4643836A (en) | Radial flow filter having air fluidizing backwash means | |
| KR870000158B1 (en) | Liquid filter assembly | |
| JPS646891Y2 (en) | ||
| US6217782B1 (en) | Combined ultrasonic cleaning and washing of filter disks | |
| JPH04501981A (en) | Suspension filtration method and device | |
| US2562730A (en) | Filter tube | |
| US2600458A (en) | Upflow pressure diatomite filtering apparatus | |
| US5635080A (en) | Filter system with external scrubber | |
| US6077446A (en) | Sand filtration filtering system using ozone | |
| EP0158529A2 (en) | Pressure filter | |
| US1993175A (en) | Process and apparatus for filters | |
| JPH04271802A (en) | Method for removing cake in filter | |
| JPH0143567B2 (en) | ||
| KR20020005380A (en) | Apparatus of cleaning dirty water | |
| KR102175759B1 (en) | Separating device of foreign material for water treatment | |
| US2293120A (en) | Filter | |
| RU2173489C2 (en) | Method and device for separating medium into solid-containing and liquid components | |
| KR100661814B1 (en) | Continuous Filtration System Using Container Filter | |
| JPH0761404B2 (en) | Device for removing suspended matter of light specific gravity in liquid | |
| RU2040946C1 (en) | Liquid purification filter | |
| KR200220293Y1 (en) | Waste water filtering device of livestock farm | |
| JP2002011305A (en) | Filter with screen | |
| KR100194329B1 (en) | Filtration Device for Water Treatment | |
| SU1270117A1 (en) | Installation for removing suspended substances and petroleum products from waste water |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| A300 | Application deemed to be withdrawn because no request for examination was validly filed |
Free format text: JAPANESE INTERMEDIATE CODE: A300 Effective date: 19980514 |