JP4843265B2 - Waste liquid recycling device - Google Patents

Waste liquid recycling device Download PDF

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JP4843265B2
JP4843265B2 JP2005175605A JP2005175605A JP4843265B2 JP 4843265 B2 JP4843265 B2 JP 4843265B2 JP 2005175605 A JP2005175605 A JP 2005175605A JP 2005175605 A JP2005175605 A JP 2005175605A JP 4843265 B2 JP4843265 B2 JP 4843265B2
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water
waste liquid
tank
treatment tank
wall
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JP2006346569A (en
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昌之 江田
順一 飯伏
穣 末田
勝昭 槙野
美津保 大恵
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Mitsubishi Heavy Industries Machinery Systems Co Ltd
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Mitsubishi Heavy Industries Printing and Packaging Machinery Ltd
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本発明は、印刷機のブランケット胴等のインキが付着する印刷機の構成部品の洗浄時に排出される廃液を再生処理する装置に関し、特に、帯電したインキ顔料、絶縁性の洗浄液、及び導電性の水の3成分が混在した処理槽において、単一の装置でそれらの3成分を分離する廃液再生装置に関する。   The present invention relates to an apparatus for reclaiming waste liquid discharged during cleaning of printing machine components to which ink adheres, such as a blanket cylinder of a printing machine, and in particular, charged ink pigment, insulating cleaning liquid, and conductive The present invention relates to a waste liquid regenerating apparatus for separating three components with a single device in a treatment tank in which three components of water are mixed.

印刷機のブランケット胴や圧胴の洗浄は、石油系の洗浄液を使用するため廃液が出る。従来、廃液は廃棄されていたが、近年では、廃液を再処理して洗浄液を再利用する方式が試みられている。
廃液の再生方法としては、種々の方式が提案されているが、高効率で再生を行えることから、インキ顔料、水、洗浄液の3成分を含んだ廃液中に静電界を発生させ、インキ顔料を廃液中で電気泳動させるとともに、水を静電凝集させて、インキ顔料、水、洗浄液を分離する静電界利用方式が注目されている。
一般に、廃液再生装置は、廃液再生処理槽内の上側にプラス電極を配置し下側にマイナス電極を配置し、印刷機で使用したインキ顔料、水、洗浄液を含んだ廃液を前記廃液再生処理槽内に入れ、前記電極間に電圧を印加させて前記廃液を静電界処理し、前記インキ顔料をマイナス電極に誘導し、凝集した水が前記廃液処理槽内の底部に沈降させ、該水より比重の軽い洗浄液を上澄み液として分離し、前記廃液から洗浄液を再生する。
本出願人は、本発明の提案に先立ち、静電界利用方式を利用した実用性の高い廃液再生装置について提案している(例えば、特許文献1または特許文献2参照)。
以下、図4及び図5により従来の廃液再生装置について説明する。
特許第3586630号公報 特許第3586656号公報
Cleaning the blanket cylinder and impression cylinder of a printing press uses a petroleum-based cleaning liquid, resulting in waste liquid. Conventionally, the waste liquid has been discarded, but in recent years, a method of reprocessing the waste liquid and reusing the cleaning liquid has been attempted.
Various methods have been proposed for recycling the waste liquid, but since it can be regenerated with high efficiency, an electrostatic field is generated in the waste liquid containing the three components of the ink pigment, water, and cleaning liquid, and the ink pigment is removed. Attention has been focused on a method of using an electrostatic field in which electrophoresis is carried out in a waste liquid and water is electrostatically aggregated to separate an ink pigment, water and a cleaning liquid.
Generally, a waste liquid recycling apparatus has a positive electrode on the upper side and a negative electrode on the lower side of the waste liquid recycling treatment tank, and the waste liquid containing ink pigment, water, and cleaning liquid used in the printing press is disposed in the waste liquid recycling treatment tank. The waste liquid is treated with an electrostatic field by applying a voltage between the electrodes, the ink pigment is guided to the negative electrode, and the agglomerated water is allowed to settle at the bottom of the waste liquid treatment tank. Is removed as a supernatant, and the cleaning liquid is regenerated from the waste liquid.
Prior to the proposal of the present invention, the present applicant has proposed a highly practical waste liquid regenerating apparatus using an electrostatic field utilization method (for example, see Patent Document 1 or Patent Document 2).
Hereinafter, a conventional waste liquid recycling apparatus will be described with reference to FIGS.
Japanese Patent No. 3586630 Japanese Patent No. 3586656

図4は、上記提案に係る静電界利用方式を利用した廃液再生装置4の原理的構成を示す概略断面図である。
図4に示したように、廃液再生装置4の容器処理槽61内には、仕切り板62が図中上下方向に配設され、仕切り板62と処理槽61の一方側の縦壁63との間の上部には、廃液6を廃液再生装置4内に導入するための供給口64が設けられている。
また、仕切り板62の下方端部と処理槽61の底部との間に隙間65を形成するとともに、仕切り板62と他方の縦壁66との間には、電極板67を水平方向に並ぶように設置している。なお、この廃液再生装置4では、水7の層がアース電極として機能する。
FIG. 4 is a schematic cross-sectional view showing the basic configuration of the waste liquid recycling apparatus 4 using the electrostatic field utilization method according to the above proposal.
As shown in FIG. 4, a partition plate 62 is arranged in the vertical direction in the figure in the container treatment tank 61 of the waste liquid regenerating apparatus 4, and the partition plate 62 and the vertical wall 63 on one side of the treatment tank 61 are arranged. A supply port 64 for introducing the waste liquid 6 into the waste liquid regenerating apparatus 4 is provided in the upper part.
Further, a gap 65 is formed between the lower end portion of the partition plate 62 and the bottom portion of the processing tank 61 , and the electrode plate 67 is arranged in the horizontal direction between the partition plate 62 and the other vertical wall 66. It is installed in. In this waste liquid recycling apparatus 4, the layer of water 7 functions as a ground electrode.

この廃液再生装置4により実現される廃液再生方法について説明する。処理槽61に供給された廃液6中には、水7、インキ顔料68、石油系の洗浄液が混在している。電極板67に高電圧を印加し、電極板67を+極、水7を−極として、電極板67及び水7間に電界を発生させる。この電界が働くことにより、廃液6中におけるインキ顔料68の電気泳動と水7の静電凝集が始まる。より具体的には、廃液6中の水69は大粒の粒径の凝集水70に凝集し、凝集水70とインキ顔料68はそれぞれ別々に移動し分離してゆく。 A waste liquid regeneration method realized by the waste liquid regeneration apparatus 4 will be described. In the waste liquid 6 supplied to the treatment tank 61 , water 7, ink pigments 68, and petroleum-based cleaning liquid are mixed. A high voltage is applied to the electrode plate 67, and an electric field is generated between the electrode plate 67 and the water 7 using the electrode plate 67 as a positive electrode and the water 7 as a negative electrode. By the action of this electric field, electrophoresis of the ink pigment 68 and electrostatic aggregation of the water 7 in the waste liquid 6 start. More specifically, the water 69 in the waste liquid 6 is aggregated into the aggregated water 70 having a large particle diameter, and the aggregated water 70 and the ink pigment 68 are moved and separated separately.

電界を発生させている状態を長く続けることにより、電界中での反応が進み、廃液中において水69とインキ顔料68とが完全に分離し、水69は一群に凝集して、重力により処理槽61の底部に沈降し、水7の層へ加わる。また、+電荷のインキ顔料68は、−極であるアース電極(水層)の表面(上面)に付着する。これにより、水7,70とインキ顔料68が除去された洗浄液(即ち、洗浄再生液)が得られる。そして、この洗浄液が回収対象とされる。 By continuing the state in which the electric field is generated for a long time, the reaction in the electric field proceeds, the water 69 and the ink pigment 68 are completely separated in the waste liquid 6 , and the water 69 aggregates into a group and is treated by gravity. It settles at the bottom of the tank 61 and joins the water 7 layer. Further, the positively charged ink pigment 68 adheres to the surface (upper surface) of the ground electrode (water layer) which is the negative electrode. As a result, a cleaning liquid from which the water 7 and 70 and the ink pigment 68 have been removed (that is, a cleaning regeneration liquid) is obtained. And this washing | cleaning liquid is made into collection | recovery object.

続いて、以上説明した原理を用いた従来の廃液再生装置について説明する。図5は、従来の廃液再生装置の一構成例の断面概略図である。
図5に示したように、本廃液再生装置5は、廃液供給部71に廃液6を供給し、プラス電極板67と水7とで、電極間のインキ顔料、水、洗浄液の3成分を含んだ廃液中に静電界を発生させ、インキ顔料を廃液中で電気泳動させるとともに、水を静電凝集させて、インキ顔料、水、洗浄液を分離し、再生液8を回収する。ここで操業が進むにつれて、再生液が増加するが、この再生液8はオーバーフロー方式で自動的に処理していた。
Subsequently, a conventional waste liquid recycling apparatus using the principle described above will be described. FIG. 5 is a schematic cross-sectional view of a configuration example of a conventional waste liquid recycling apparatus.
As shown in FIG. 5, the present waste liquid recycling apparatus 5 supplies the waste liquid 6 to the waste liquid supply unit 71, and the plus electrode plate 67 and the water 7 include three components of ink pigment, water, and cleaning liquid between the electrodes. Then, an electrostatic field is generated in the waste liquid, the ink pigment is electrophoresed in the waste liquid, and water is electrostatically aggregated to separate the ink pigment, water, and the cleaning liquid, and the regenerated liquid 8 is recovered. Here, as the operation proceeds, the regenerated liquid increases, but this regenerated liquid 8 was automatically processed by the overflow method.

以上説明したような廃液再生装置においては、静電凝集で発生した水7も増加してゆくことになる。しかしながら、プラス電極67とアース電極である水7の表面間距離LDは所定の距離でないと、正常な静電凝集ができなくなる。
そのため、水7の水位を制御するため、槽内に水位計72を設け、所定水位をオーバーした場合は、排水孔73のバルブ74を開いて、水を排水し、所定水位(電極間距離LD)を確保する必要があった。
しかしながら、このような制御は、自動化を要する為、排水のみのために、水位計と電磁開閉バルブ及び制御装置を必要とし、装置製作コストの上昇を招いていた。また、センサや制御装置のトラブルが発生する危険性もあった。
In the waste liquid regenerating apparatus as described above, the water 7 generated by electrostatic aggregation also increases. However, if the distance LD between the surfaces of the positive electrode 67 and the water 7 as the ground electrode is not a predetermined distance, normal electrostatic aggregation cannot be performed.
Therefore, in order to control the water level of the water 7, a water level gauge 72 is provided in the tank, and when the predetermined water level is exceeded, the valve 74 of the drain hole 73 is opened to drain the water, and the predetermined water level (interelectrode distance LD). ) Had to be secured.
However, since such control requires automation, a water level meter, an electromagnetic opening / closing valve and a control device are required only for drainage, resulting in an increase in device manufacturing cost. There is also a risk that troubles with the sensor and the control device may occur.

本発明は、このような事情に鑑みてなされたものであって、印刷機械の洗浄廃液再生方法及び装置において、簡易な装置構成を提案し、製作コストの低減を実現するとともに、トラブルの発生しにくい安全な廃液再生装置を提供するものである。   The present invention has been made in view of such circumstances, and in a cleaning waste liquid recycling method and apparatus for a printing machine, proposes a simple apparatus configuration, realizes a reduction in production cost, and causes trouble. It is an object of the present invention to provide a difficult and safe waste liquid recycling apparatus.

上記課題を解決するために、本発明は、以下の手段を提供する。
本発明の廃液再生装置は、印刷機で使用した水を含む廃液を貯留する処理槽と、前記処理槽内に電界を発生させる電界生成手段と、を備える廃液再生装置において、前記処理槽内を仕切る第1の仕切壁と、前記処理槽内を前記第1の仕切壁により仕切られた一方の空間である水貯留槽と、前記水貯留槽に設けられた排水開口と、前記処理槽の底面と前記第1の仕切壁との間に設けられた第1の隙間とを備え、前記電界発生手段は、前記廃液中に含まれた水を、前記処理槽の底部に静電凝集させ、前記隙間は、前記静電凝集させた水を前記処理槽内の前記第1の仕切壁により仕切られた他方の空間から前記水貯留槽に導出する連通部として機能し、前記排水開口は、前記水貯留槽内の水を自然排水して前記水貯留槽内の水位を所定水位に調整する水位調整機構として機能することを特徴とする。
水貯留槽と処理槽とを連通させることにより、水と廃液との比重差を利用したバランス機構を実現することができる。
In order to solve the above problems, the present invention provides the following means.
The waste liquid recycling apparatus of the present invention is a waste liquid recycling apparatus comprising: a processing tank for storing waste liquid containing water used in a printing press; and an electric field generating means for generating an electric field in the processing tank . A first partition wall for partitioning, a water storage tank that is one space partitioned by the first partition wall in the processing tank, a drain opening provided in the water storage tank, and a bottom surface of the processing tank and a first gap provided between the first partition wall and said field generating means, the water contained in the waste liquid, is electrostatically agglomerate at the bottom of the treatment tank, the gap, the were electrostatically agglomerated water, acts as a communicating unit that derives the water reservoir from the other space partitioned by the first partition wall of the processing bath, the drainage opening The water in the water storage tank is drained naturally to adjust the water level in the water storage tank to a predetermined water level. Characterized in that it functions as that the water level adjusting mechanism.
By making the water storage tank and the treatment tank communicate with each other, a balance mechanism using the specific gravity difference between the water and the waste liquid can be realized.

また、上記発明においては、前記所定水位は、処理される廃液の比重に基づき定められることが望ましい。
また、上記発明においては、前記排水開口は排水孔であって、前記処理槽は前記底面と周壁とを有し、前記排水開口は前記周壁に設けられ、前記第1の仕切壁は前記周壁の前記排水開口が設けられた第1の内壁面に対向するように設けられていることが望ましい。
また、上記発明においては、前記処理槽は前記底面と周壁とを有し、前記水貯留槽には、前記排水開口に相当する上部開口を有し伸縮可能な排水パイプが設けられることが望ましい。
また、上記発明においては、前記他方の空間を形成する前記周壁に設けられた再生液回収孔と、前記周壁の前記再生液回収孔が設けられた第2の内壁面に対向するとともに、下方端部が前記第1の仕切壁の下方端部よりも上方に配置され前記処理槽の前記底面との間に隙間が形成されるように設けられた第2の仕切壁との間に設けられた回収再生液貯留部と、前記第2の仕切壁の下方端部と前記第2の内壁面との間に水平配置されたプラス電極と、前記処理槽の前記底面に設けられたマイナス電極であるアース電極と、を備え、前記電界発生手段は、前記プラス電極と前記マイナス電極とをそなえていることが望ましい。
In the aspect described above, the predetermined level is preferably determined based on the specific gravity of the waste liquid to be processed.
In the above invention, the drain opening is a drain hole, the treatment tank has the bottom surface and a peripheral wall, the drain opening is provided on the peripheral wall, and the first partition wall is formed on the peripheral wall. It is desirable that the drain opening is provided so as to face the first inner wall surface provided with the drain opening.
Moreover, in the said invention, it is desirable that the said processing tank has the said bottom face and a surrounding wall, and the said water storage tank is provided with the drain pipe which has an upper opening equivalent to the said drain opening, and can expand-contract.
In the above invention, the regeneration liquid recovery hole provided in the peripheral wall forming the other space is opposed to the second inner wall surface provided with the regeneration liquid recovery hole of the peripheral wall, and the lower end And a second partition wall provided so that a gap is formed between the first partition wall and a lower end of the first partition wall and the bottom surface of the processing tank. A recovery / regeneration liquid storage unit; a positive electrode horizontally disposed between a lower end of the second partition wall and the second inner wall surface; and a negative electrode provided on the bottom surface of the processing tank. It is preferable that the electric field generating means includes the plus electrode and the minus electrode.

本発明に係る廃液再生装置および廃液再生方法によれば、従来の装置構成で使用していた水位計と電磁開閉バルブ及び制御装置が不要となり、簡易な装置構成で容易に装置製作が可能となり、製作コストが大幅に削減できる。またセンサや制御装置を使用せず、セルフバランス方式のためトラブルが発生する危険性が激減できる。   According to the waste liquid regenerating apparatus and the waste liquid regenerating method according to the present invention, the water level meter, the electromagnetic open / close valve and the control device used in the conventional apparatus configuration are not required, and the apparatus can be easily manufactured with a simple apparatus configuration. Production costs can be greatly reduced. Moreover, the risk of trouble occurring due to the self-balancing method without using sensors or control devices can be drastically reduced.

以下、本発明に係る廃液再生装置および廃液再生方法につき、図1乃至図に基づき説明する。
本発明に係る廃液再生装置は、廃液処理層内の溶剤と水の比重とバランスする水貯留槽としてセルフバランス水タンクを設けるものであって、言い換えれば、廃液再生処理装置構成において、水と廃液(溶剤)の比重差を利用した水貯留槽を備える構成とするものである。そして、このセルフバランス水タンクを廃液処理槽に連接するように設け、処理中に発生する水の増加分を自動的に排水する方式を採用している。
ここで、アース電極用の水7の水位(h1)、溶剤の水位(h2)、水の比重(ρ1=1)、溶剤の比重(ρ2=0.7)の場合、セルフバランス用の水タンクの水位(h0)は、次の数1に示す式で定義される。
<数1>
(h0×ρ1)=(h1×ρ1)+(h2×ρ2)
よって、処理層内のアース電極の水位(h1)がほぼ一定となるように、セルフバランス水タンクの水位(h0)を決定し、この水位(h0)より増加した水は排水孔から自然排水される構成とすれば、アース電極の水位(h1)はほぼ一定となり、電極板6とアース電極間の距離(LD)は常に一定に保たれる。本発明は、この知見に基づき好適な廃液再生装置および廃液再生方法を提供するものである。
DETAILED DESCRIPTION waste reproducing apparatus and waste reproducing method according to the present invention will be described with reference to FIGS.
Waste reproducing apparatus according to the present invention, there is provided a self-balancing water tank as the water reservoir to balance the specific gravity of the solvent and water waste treatment layer, in other words, the waste liquid reproduction process device configuration, the water 7 It is set as the structure provided with the water storage tank using the specific gravity difference of waste liquid (solvent) 6 . The self-balancing water tank is provided so as to be connected to the waste liquid treatment tank, and a method of automatically draining the increased amount of water generated during the treatment is adopted.
Here, in the case of the water level (h1) of the water 7 for the earth electrode, the water level (h2) of the solvent, the specific gravity of water (ρ1 = 1), and the specific gravity of the solvent (ρ2 = 0.7), a water tank for self-balancing The water level (h0) is defined by the following equation (1).
<Equation 1>
(H0 × ρ1) = (h1 × ρ1) + (h2 × ρ2)
Therefore, the water level (h0) of the self-balancing water tank is determined so that the water level (h1) of the ground electrode in the treatment layer is substantially constant, and the water increased from this water level (h0) is naturally drained from the drain hole. With this configuration, the water level (h1) of the ground electrode is substantially constant, and the distance (LD) between the electrode plate 6 and the ground electrode is always kept constant. The present invention provides a suitable waste liquid recycling apparatus and waste liquid recycling method based on this finding.

〔第の実施形態〕
最初に、本発明に係る廃液再生装置の基本的な構成および再生方法を図1に基づきに説明する。図1は、本発明に係る第1の実施形態としての基本的装置構成を示す概略断面図であり、図1(a)は注水状態、図1(b)は洗浄液供給状態、図1(c)は再生稼動状態を各々示している。
図1に示したように、廃液再生装置1は、周壁に2つの開口(再生液回収孔12,自然排水孔13)を有する処理槽11と、その処理槽11の内部に2つの仕切壁14,15を備える。
First Embodiment
First, a basic configuration and a regeneration method of the waste liquid regenerating apparatus according to the present invention will be described with reference to FIG. FIG. 1 is a schematic cross-sectional view showing a basic apparatus configuration as a first embodiment according to the present invention, FIG. 1 (a) is a water injection state, FIG. 1 (b) is a cleaning liquid supply state, and FIG. ) Shows the regeneration operation state.
As shown in FIG. 1, the waste liquid regenerating apparatus 1 includes a processing tank 11 having two openings (regenerated liquid recovery hole 12 and natural drain hole 13) on a peripheral wall, and two partition walls 14 inside the processing tank 11. , 15 are provided.

ここで、仕切壁14は、処理槽11の自然排水孔13が設けられた内壁面に対向するとともに、仕切壁14の下方端部と処理槽11の底面との間に隙間16が形成されるように設けられる。この仕切壁14と処理槽11の内壁面とに囲まれた空間が、後述するセルフバランス用の水タンク20として機能する。この水タンク20は、図中上方に水供給用の開口を備える。
他方、仕切壁15は、処理槽11の再生液回収孔12が設けられた内壁面に対向するとともに、仕切壁15の下方端部と処理槽11の底面との間に連通部として機能する隙間が形成されるように設けられる。この仕切壁15と処理槽11の内壁面とに囲まれた空間が、洗浄再生液を貯留する回収再生液貯留部となる。
Here, the partition wall 14 faces the inner wall surface of the treatment tank 11 where the natural drain hole 13 is provided, and a gap 16 is formed between the lower end of the partition wall 14 and the bottom surface of the treatment tank 11. It is provided as follows. A space surrounded by the partition wall 14 and the inner wall surface of the treatment tank 11 functions as a water tank 20 for self-balancing described later. This water tank 20 is provided with an opening for supplying water at the top in the figure.
On the other hand, the partition wall 15 faces the inner wall surface of the processing tank 11 where the regenerated liquid recovery hole 12 is provided, and functions as a communication part between the lower end of the partition wall 15 and the bottom surface of the processing tank 11. It is provided so that a gap is formed. A space surrounded by the partition wall 15 and the inner wall surface of the treatment tank 11 serves as a recovery / regeneration liquid storage unit that stores the cleaning / regeneration liquid.

なお、本実施形態でも、従来の廃液再生装置と同様に、既知の手法により、プラス電極17を仕切壁15の下方端部と再生液回収孔12が設けられた処理槽11の内壁面との間に水平配置するととに、処理槽11の底に形成される水7の層をアース電極として機能させる。
そして、上述した仕切壁14と仕切壁15とによって挟まれた領域は、廃液もしくは後述する洗浄液が供給、貯留される空間である廃液供給部18として機能する。この仕切壁14と仕切壁15とにより形成される上部開口18aは、廃液もしくは洗浄液をこの空間に供給するための廃液供給口として機能する。
本実施形態においては、プラス電極となる電極板17を仕切壁15の下方端部に水平に設けたので、この仕切壁14と仕切壁15の下方端部の高低差が、最大に設定可能な電極間距離を左右することになる。
In this embodiment as well, as in the case of the conventional waste liquid regenerating apparatus, the positive electrode 17 is connected to the lower end of the partition wall 15 and the inner wall surface of the treatment tank 11 provided with the regenerating liquid recovery hole 12 by a known method. also with the horizontally disposed between, to function layer of water 7 which is formed in the bottom of the treatment tank 11 as an earth electrode.
And the area | region pinched | interposed by the partition wall 14 and the partition wall 15 mentioned above functions as the waste liquid supply part 18 which is the space where the waste liquid 6 or the washing | cleaning liquid mentioned later is supplied and stored. The upper opening 18a formed by the partition wall 14 and the partition wall 15 functions as a waste liquid supply port for supplying the waste liquid 6 or the cleaning liquid to this space.
In the present embodiment, since the electrode plate 17 serving as a positive electrode is provided horizontally at the lower end portion of the partition wall 15, the height difference between the partition wall 14 and the lower end portion of the partition wall 15 can be set to the maximum. The distance between the electrodes will be affected.

以下、廃液再生装置1 における処理工程につき詳述する。
図1(a)は、本実施形態に係る廃液再生装置の使用開始時の状況を示し、廃液再生装置1の槽内には廃液は入っていない状態である。ここで、処理槽の仕切壁14に隣接して設置した本発明のセルフバランス用の水タンク20に、供給口20aを介して、マイナス電極用の水7を所定水位(h3)まで注水する。
Hereinafter, the processing steps in the waste liquid recycling apparatus 1 will be described in detail.
FIG. 1A shows a situation at the start of use of the waste liquid regenerating apparatus according to the present embodiment, in which the waste liquid 6 is not contained in the tank of the waste liquid regenerating apparatus 1. Here, the water 7 for negative electrodes is poured into the water tank 20 for self-balancing of the present invention installed adjacent to the partition wall 14 of the treatment tank through the supply port 20a to a predetermined water level (h3).

その後、図1(b)に示したように、新しい洗浄液もしくは再生洗浄液8を廃液供給口18aを介して廃液供給部18に供給する。
ここで、供給する新しい洗浄液もしくは再生洗浄液8は、水より比重の軽い比重(ρ2=0.7〜0.8程である。そのため、供給した新しい洗浄液もしくは再生洗浄液8は、処理槽11の底部で層を形成している水7と混水せず、水7の上に乗った状態となる。このまま新しい洗浄液もしくは再生洗浄液8を供給していくと、再生洗浄液8の重量により処理槽11の底部にある水7は、隣接したセルフバランス用の水タンク20へ流入していき、結果として、図1(a)の水位(h3)よりも低い水位(h1)となる。
そして、新しい洗浄液もしくは再生洗浄液8が処理槽11に満杯になり、再生液回収孔12から排出する状態まで新しい洗浄液もしくは再生洗浄液8を供給する。このとき、水タンク20内の水位(h0)は、水7の層の水位をh1、溶剤の水位をh2、水の比重をρ1、溶剤の比重をρ2とすると、(h0×ρ1)=(h1×ρ1)+(h2×ρ2)の関係式を充足するが、本実施形態では、このバランスする位置(h0)に、自然排水孔13を設置する。これにより、廃液処理槽内の廃液と水の量が一定の比率に保たれることになる。ひいては、廃液処理槽内の水と洗浄液の水位が一定に保たれる事により、プラス電極とマイナス電極間の距離が一定に制御できる。
Thereafter, as shown in FIG. 1B, a new cleaning liquid or regenerated cleaning liquid 8 is supplied to the waste liquid supply unit 18 through the waste liquid supply port 18a .
Here, the new washing liquid or reproducing cleaning liquid 8 supplies a lighter specific gravity than water specific gravity ([rho] 2 = 0.7-0. 8 extent). Therefore, the supplied new cleaning liquid or regenerated cleaning liquid 8 is not mixed with the water 7 forming a layer at the bottom of the treatment tank 11, but is put on the water 7. If new cleaning liquid or regenerated cleaning liquid 8 is supplied as it is, the water 7 at the bottom of the treatment tank 11 flows into the adjacent water tank 20 for self-balancing due to the weight of the regenerated cleaning liquid 8. The water level (h1) is lower than the water level (h3) of 1 (a).
Then, the new cleaning liquid or the regenerated cleaning liquid 8 is supplied until the new cleaning liquid or the regenerated cleaning liquid 8 fills the processing tank 11 and is discharged from the regenerated liquid recovery hole 12. At this time, the water level (h0) in the water tank 20 is (h0 × ρ1) = (h1) where the water level of the water 7 layer is h1, the solvent water level is h2, the water specific gravity is ρ1, and the solvent specific gravity is ρ2. Although the relational expression h1 × ρ1) + (h2 × ρ2) is satisfied, in this embodiment, the natural drainage hole 13 is installed at the balanced position (h0). Thereby, the amount of the waste liquid 6 and the water 7 in the waste liquid treatment tank is kept at a constant ratio. As a result, the distance between the positive electrode and the negative electrode can be controlled to be constant by keeping the water level of the water and the cleaning liquid in the waste liquid treatment tank constant.

具体的には、溶剤(洗浄液)の比重をρ=0.7とし、電極水の水位をh1=30mm、溶剤(廃液)の水位をh2=100mmとすると、水タンク20内の水位はh0=100mmとなる。
よって自然排水孔13をタンク底部から100mmの位置に設けると、両者はバランスする。また、本実施形態では、電極板17と水表面間の距離LDは、廃液の比重が溶剤の種類により若干変化することに対応するためLD=35mmで設計した。
なお、図示していないが、自然排13は伸縮性のパイプ状の構成とし、廃液(インキ顔料)の比重に応じて排水孔の位置を調整できる構成としたほうがより好ましい。
Specifically, if the specific gravity of the solvent (cleaning liquid) is ρ 2 = 0.7, the water level of the electrode water is h1 = 30 mm, and the water level of the solvent (waste liquid) is h2 = 100 mm, the water level in the water tank 20 is h0. = 100 mm.
Therefore, if the natural drainage hole 13 is provided at a position of 100 mm from the bottom of the tank, both are balanced. In the present embodiment, the distance LD between the electrode plate 17 and the water surface is designed to be LD = 35 mm in order to cope with the specific gravity of the waste liquid 6 slightly changing depending on the type of solvent.
Although not illustrated, natural drainage hole 13 is a stretch of pipe-shaped configuration, more and more preferably has a structure capable of adjusting the position of the drain holes in accordance with the specific gravity of the waste (ink pigment) 6.

続いて、新しい洗浄液もしくは再生洗浄液8と水7がバランスした状態になった時点から、図1(c)に示したように廃液6を供給開始するとともに、電極板17にプラス電荷をかけ、アース電極に接続された水層とで静電界を発生させる。この電界の発生により、処理槽11内の廃液は、溶剤とインキ顔料と水とに分離され、水とインキ顔料は底部へ沈降し、洗浄液は再生洗浄液8として再生回収孔12から回収される。
本実施形態においては、静電界により廃液から分離した水7は、底部に沈降するが、水位(h1)を保った状態で水タンク20の自然排水孔13から自然に排水されることになる。
よって、廃液が連続して供給され、洗浄液8を再生しながら水7が増加した場合であっても、水7はセルフバランス状態で自然排水されるため、水位(h1)は、ほぼ一定値であり、結果として電極板17とアース電極(水表面)間の距離(LD)は、設計値の値でほぼ一定に保たれることになる。
これにより処理層内のアース電極の水位(h1)を一定に保つため、従来の装置構成で使用していた水位計と電磁開閉バルブ及び制御装置が不要となり、簡易な装置構成で容易に装置製作が可能となり、製作コストが大幅に削減できる。またセンサや制御装置を使用せず、セルフバランス方式のためトラブルが発生する危険性が激減できる。
Subsequently, when the new cleaning liquid or the regenerated cleaning liquid 8 and the water 7 are in a balanced state, the supply of the waste liquid 6 is started as shown in FIG. An electrostatic field is generated with a layer of water 7 connected to the electrodes. Due to the generation of this electric field, the waste liquid in the treatment tank 11 is separated into a solvent, an ink pigment, and water, and the water and the ink pigment settle to the bottom, and the cleaning liquid is recovered from the regeneration recovery hole 12 as the regenerated cleaning liquid 8.
In this embodiment, the water 7 separated from the waste liquid 6 by the electrostatic field settles at the bottom, but is naturally drained from the natural drain hole 13 of the water tank 20 while maintaining the water level (h1). .
Therefore, even when the waste liquid is continuously supplied and the water 7 increases while the cleaning liquid 8 is regenerated, the water 7 is naturally drained in a self-balanced state, so the water level (h1) is almost constant. As a result, the distance (LD) between the electrode plate 17 and the ground electrode (water surface) is kept substantially constant at the design value.
This keeps the water level (h1) of the ground electrode in the treatment layer constant, eliminating the need for the water level gauge, electromagnetic open / close valve, and control device used in the conventional device configuration, and making the device easily with a simple device configuration. Manufacturing costs can be greatly reduced. Moreover, the risk of trouble occurring due to the self-balancing method without using sensors or control devices can be drastically reduced.

〔第2の実施形態〕
以下、本発明の第2の実施形態として、2槽式の廃液再生装置2の概要を図2を用いて説明する。なお、第1の実施形態と同様の機能を有する構成要素には同一の符号を付し、説明を省略する。
図2は、本実施形態に係わる印刷機の廃液再生装置2を示す概略構成図である。
廃液再生装置2は、第1の再生液処理槽21(以下、第1の処理槽とも称す)と第2 の再生液処理槽22(以下、第2の処理槽とも称す)とを有する。第1の処理槽21及び第2の処理槽22は、縦方向に配設されている堰壁23で仕切られている。
また、廃液再生装置1の図中左側にはセルフバランス用の水タンク20が設けられているが、より詳細には、セルフバランス用の水タンク20は、壁部44と仕切り板45で仕切られた印刷機からの排出された廃液6の供給部18に隣接した位置に設けられている。この水タンク20の壁を形成する壁部44の下部には、第1の処理槽21側と連通する隙間(連通部)46が設けられている。
この隙間46により壁部44部は開放されており、容器底部のアース電極である水7が、セルフバランス水タンク20へ流出できる構成となっている。
加えて、第1の処理槽21の堰壁23とこれに対向する反対側壁部44との間には、間隔を空けて仕切り板45が設けられ、この仕切り板45は上下方向に配置されているが、壁部44の下端部よりも仕切り板45の下端部が上方に位置するよう、下端部が第1の処理槽21のほぼ中間位置まで延びている。
[Second Embodiment]
Hereinafter, as a second embodiment of the present invention, an outline of a two-tank waste liquid regenerating apparatus 2 will be described with reference to FIG. Note that components having the same functions as those in the first embodiment are denoted by the same reference numerals, and description thereof is omitted.
FIG. 2 is a schematic configuration diagram showing the waste liquid recycling apparatus 2 for the printing press according to the present embodiment.
The waste liquid regenerating apparatus 2 includes a first regenerating liquid processing tank 21 (hereinafter also referred to as a first processing tank) and a second regenerating liquid processing tank 22 (hereinafter also referred to as a second processing tank). The first processing tank 21 and the second processing tank 22 are partitioned by a dam wall 23 arranged in the vertical direction.
Further, a self-balancing water tank 20 is provided on the left side of the waste liquid recycling apparatus 1 in the figure, but more specifically, the self-balancing water tank 20 is partitioned by a wall portion 44 and a partition plate 45. It is provided at a position adjacent to the supply unit 18 for the waste liquid 6 discharged from the printing press. A gap (communication portion) 46 communicating with the first treatment tank 21 side is provided at the lower portion of the wall portion 44 that forms the wall of the water tank 20.
The lower part of wall portion 44 by a gap 46 is open, the water 7 is a ground electrode of the bottom portion, and has a configuration that can flow out to the self-balanced water tank 20.
In addition, a partition plate 45 is provided between the dam wall 23 of the first treatment tank 21 and the opposite side wall portion 44 opposed thereto, and the partition plate 45 is arranged in the vertical direction. However, the lower end portion extends to a substantially intermediate position of the first processing tank 21 so that the lower end portion of the partition plate 45 is positioned above the lower end portion of the wall portion 44.

第1の処理槽21の底部には、マイナス電極として使用する水7を入れてある。このため、特別な電極を必要としてしない。プラス電極には、仕切り板45と堰壁23との間に水平方向に配置され、洗浄液が流通できる多数の孔が形成されたメッシュ方式の電極板17を用いる。なお、この電極板17の位置により電極間距離が定まるが、例えば、本実施形態においては、廃液供給流量をq=0.5L/min、印加電圧を5kVとし、適性電界強度をDV=0.125V/mmとすると、プラス電極17とマイナス電極の水7面との間の距離はLD1=40mmとなるように設ける。 Water 7 used as a negative electrode is placed at the bottom of the first treatment tank 21. For this reason, a special electrode is not required. As the positive electrode, a mesh-type electrode plate 17 is used, which is horizontally disposed between the partition plate 45 and the dam wall 23 and has a large number of holes through which the cleaning liquid can flow. Although the distance between the electrodes is determined by the position of the electrode plate 17, for example, in the present embodiment, the waste feed stream weight q = 0.5L / mi n, the applied voltage was 5 kV, the suitability field strength DV = When 0.125V / mm, the distance between the water surface 7 of the positive electrode 17 and negative electrode provided so that LD1 = 40 mm.

第2の処理槽22には、堰壁23側に隣接して、処理された洗浄液の供給部24が設けられ、供給部24は堰壁23と仕切り板25で形成されている。洗浄液は、堰壁23を超えて供給部24に流入し、第2の処理槽22に供給される。仕切り板25は、上下方向に配置され下端部が第2の処理槽22のほぼ上下中間位置まで延びており、底面との間の隙間で供給部24側とメッシュ電極板26側とが連通する。そして、仕切り板25に平行して処理槽22の構成壁面となる仕切り板27が配置される。さらに、この仕切り板27に隣接させて回収タンク30を配設している。
第2の処理槽22では、処理された洗浄液が仕切り板27を超えて、回収タンク30に供給され、回収タンク30から不図示の回収装置に回収される。
ここで、この第2の処理槽22におけるプラス電極は、仕切り板25と隔壁27の間に水平方向に配置され、洗浄液が流通できる多数の孔を形成したメッシュ形状の電極板26により構成する。
In the second processing tank 22, adjacent to the weir wall 23 side, the supply portion 24 of the treated washing liquid is provided, the supply unit 24 is formed by the weir wall 23 and the partition plate 25. The cleaning liquid flows into the supply unit 24 beyond the dam wall 23 and is supplied to the second treatment tank 22. The partition plate 25 is arranged in the vertical direction, and the lower end portion extends to a substantially upper and lower intermediate position of the second processing tank 22, and the supply unit 24 side and the mesh electrode plate 26 side communicate with each other through a gap between the partition plate 25 and the bottom surface. . In parallel with the partition plate 25, a partition plate 27 serving as a constituent wall surface of the processing tank 22 is disposed. Further, a collection tank 30 is disposed adjacent to the partition plate 27.
In the second treatment tank 22, the treated cleaning liquid passes through the partition plate 27, is supplied to the collection tank 30, and is collected from the collection tank 30 to a collection device (not shown).
Here, the plus electrode in the second treatment tank 22 is configured by a mesh-shaped electrode plate 26 that is arranged in the horizontal direction between the partition plate 25 and the partition wall 27 and has a large number of holes through which the cleaning liquid can flow. .

第2の処理槽22が第1の処理槽21と異なる点は、処理槽内にマイナス電極として水を使用せず、容器底部自体をマイナス電極28とする、若しくは底部上にマイナス電極28を設ける構成を採用していることにある。マイナス電極28の構成を処理槽21と異ならせた理由は、既に水のほとんどが第1の処理槽21で分離されていること、また水をマイナス電極としない場合には印加電圧は放電しないので、電界強度を強くできることにある。
そのため、本実施例では、第2の処理槽22のプラス電極であるメッシュ電極板26とマイナス電極28には、5kVの電圧を使用する。そして、マイナス電極(容器底部)28までの距離はLD2=30mmとする。この場合の電界強度は、DV=5/30=0.17kV/mmであり、再生洗浄液供給流量q=0.5L/min程度が良好である。
The second processing tank 22 is different from the first processing tank 21 in that water is not used as a negative electrode in the processing tank, and the container bottom itself is used as a negative electrode 28 or a negative electrode 28 is provided on the bottom. The configuration is adopted. The reason why the configuration of the negative electrode 28 is different from that of the treatment tank 21 is that most of the water has already been separated in the first treatment tank 21, and the applied voltage is not discharged when water is not used as the negative electrode. The electric field strength can be increased.
Therefore, in this embodiment, a voltage of 5 kV is used for the mesh electrode plate 26 and the negative electrode 28 that are the positive electrodes of the second treatment tank 22. The distance to the negative electrode (container bottom) 28 is LD2 = 30 mm. The electric field strength in this case is DV = 5/30 = 0.17 kV / mm, and the regenerated cleaning liquid supply flow rate q = about 0.5 L / min is good.

以下、本実施形態に係る廃液再生装置の作用について説明する。
図2に示したように、第一の処理槽21の底部にセルフバランス用の水タンク20から、アース電極用の水を所定量供給しておく。
その後、第1の処理槽21、第2の処理槽22に新しい洗浄液、もしくは再生した溶剤(再生液)を満杯に供給しておく。ここで、水タンク20の水は、第一の処理槽21の底部の水7の水位(h1)と新しい洗浄液、もしくは再生した溶剤(再生液)の水位(h2)とでバランスした水位(h0)となり、自然排水孔13から排水されて、所定の水位バランスを保持する。
この状態で、印加電圧を作用させながら廃液6を供給すると、廃液6は仕切り板45の下部を通過してメッシュ電極17のあるところへ移動する。そして静電界作用により水7とインキ顔料9と洗浄液(溶剤)に分離される。水7は、容器下部に沈降し、インキ顔料9はマイナス電極である水7の表面に付着する。そして、再生された洗浄液8は、メッシュ電極17の穴を通過してメッシュ電極17よりも上の位置にある溶剤回収部となる領域に流れ込む。
Hereinafter, the operation of the waste liquid recycling apparatus according to the present embodiment will be described.
As shown in FIG. 2, a predetermined amount of ground electrode water is supplied from the self-balance water tank 20 to the bottom of the first treatment tank 21.
Thereafter, a new cleaning liquid or a regenerated solvent (regenerated liquid) is supplied to the first processing tank 21 and the second processing tank 22 to a full extent. Here, the water in the water tank 20 is a water level (h0) balanced between the water level (h1) of the water 7 at the bottom of the first treatment tank 21 and the water level (h2) of the new cleaning liquid or the regenerated solvent (regenerated liquid). ) And drained from the natural drain hole 13 to maintain a predetermined water level balance.
In this state, when the waste liquid 6 is supplied while applying the applied voltage, the waste liquid 6 passes through the lower part of the partition plate 45 and moves to a place where the mesh electrode 17 is present. And it is isolate | separated into the water 7, the ink pigment 9, and the washing | cleaning liquid (solvent) by an electrostatic field effect. The water 7 settles in the lower part of the container, and the ink pigment 9 adheres to the surface of the water 7 which is a negative electrode. Then, the regenerated cleaning liquid 8 passes through the holes of the mesh electrode 17 and flows into a region to be a solvent recovery unit located above the mesh electrode 17.

第1の処理槽21の溶剤回収部20に流れ込んだ再生洗浄液は、第1の処理槽21の堰壁23を越えて、第2の処理槽22の供給部24に流れ込む。この第2の処理槽22に流れ込む再生洗浄液は、第1の処理槽21でほぼきれいに分離・再生されているが、わずかに残存するインキ顔料を完全に分離するのが第2の処理槽22の配設目的である。
第2の処理槽22で分離された微小インキ顔料9は、マイナス電極28である容器の底部に付着して溜まる。そして、メッシュ電極26を通過した再生洗浄液は、第2の処理槽22の壁27を越えて、再生洗浄液の回収タンク30に流れ込む。この回収タンク30に流れ込んだ再生洗浄液は、回収装置30により回収され、次の洗浄に使用される。
The regenerated cleaning liquid 8 that has flowed into the solvent recovery unit 20 of the first processing tank 21 flows over the weir wall 23 of the first processing tank 21 and flows into the supply unit 24 of the second processing tank 22. The regenerated cleaning liquid flowing into the second processing tank 22 is separated and regenerated almost cleanly in the first processing tank 21, but the remaining ink pigment is completely separated from the second processing tank 22. It is an installation purpose.
The fine ink pigment 9 separated in the second treatment tank 22 adheres to and accumulates on the bottom of the container, which is the negative electrode 28. The regenerated cleaning liquid 8 that has passed through the mesh electrode 26 flows over the wall 27 of the second treatment tank 22 and flows into the recovery tank 30 for the regenerated cleaning liquid 8 . The regenerated cleaning liquid 8 that has flowed into the recovery tank 30 is recovered by the recovery device 30 and used for the next cleaning.

一方、第1の処理槽21で分離された水は、第一の処理槽21の底部に沈降するが、ここで、本発明のセルフバランス構成により、沈降した水7は隔壁44の下部からセルフバランス用の水タンク20に流出する。流出した水により、水タンク20の水位が上昇するが、所定の水位(h0)位置に、自然排水孔13を設けてあるため、増加した水は自然に外部へ排水され、処理槽底部の水位(h1)はほぼ一定量に保持される。
これによりアース電極である水の表面とプラスのメッシュ電極17間の距離(LD1)は、ほぼ一定に保たれ、常に安定した静電分離が行える。
On the other hand, the water separated in the first treatment tank 21 settles to the bottom of the first treatment tank 21, but here, the settled water 7 is self-reacting from the lower part of the partition wall 44 by the self-balancing configuration of the present invention. It flows out to the water tank 20 for balance. The water level of the water tank 20 rises due to the outflowed water, but since the natural drain hole 13 is provided at the predetermined water level (h0) position, the increased water is drained to the outside naturally, and the water level at the bottom of the treatment tank (H1) is held at a substantially constant amount.
As a result, the distance (LD1) between the surface of the water serving as the ground electrode and the positive mesh electrode 17 is kept substantially constant, and stable electrostatic separation can always be performed.

以上説明したように、第1の処理槽21に供給された廃液6は、第1の処理槽21で一次分離され、第2の処理槽22で二次分離され、高純度に分離・回収される。なおこの処理は連続して行われる。ここで処理槽内に分離されたインキ顔料9及び水7は、それぞれ専用の回収装置にて処理槽外へ定期的に排出される。   As described above, the waste liquid 6 supplied to the first treatment tank 21 is primarily separated in the first treatment tank 21 and secondarily separated in the second treatment tank 22, and separated and recovered with high purity. The This process is performed continuously. Here, the ink pigment 9 and the water 7 separated into the processing tank are periodically discharged out of the processing tank by respective dedicated recovery devices.

〔第3の実施形態〕
以下、本発明の第3の実施形態として、本発明を排水タンク、廃液タンク、再生液タンクを備えたトータルシステムとしての廃液再生装置に用いた場合の適用例を説明する。なお、先の実施形態と同様の機能を有する構成要素には同一の符号を付し、説明を省略する。
図3は、本実施形態にかかる廃液再生システムの概略構成図である。本実施形態に係る廃液再生装置3は、先に説明した第2の実施形態と同様、第1の処理槽21と第2の処理
槽22で構成される。
第1の処理槽21は、廃液6の供給部18と、仕切り板44,45,47と、アース電極としての水7を備える。また、一方の仕切り板44に隣接するようにセルフバランス用の水タンク20を設けてあり、この水タンク2には所定の位置(h0)で自然排水用されるように二重構造で伸縮可能とした排水パイプ81を設けてある。排水パイプ8は、排水タンク32への移送パイプである。
この二重構造で伸縮可能とした排水パイプ81は、印刷機で使用するインキの種類で変化する廃液の比重変化に対処する目的であり、廃液の比重に応じて、バランス水位(h0)を調整できる構成としてある。
[Third Embodiment]
Hereinafter, as a third embodiment of the present invention, an application example when the present invention is used in a waste liquid regenerating apparatus as a total system including a drain tank, a waste liquid tank, and a regenerated liquid tank will be described. In addition, the same code | symbol is attached | subjected to the component which has the function similar to previous embodiment, and description is abbreviate | omitted.
FIG. 3 is a schematic configuration diagram of the waste liquid recycling system according to the present embodiment. The waste liquid recycling apparatus 3 according to the present embodiment includes a first processing tank 21 and a second processing tank 22 as in the second embodiment described above.
The first treatment tank 21 includes a supply unit 18 for the waste liquid 6, partition plates 44, 45, and 47, and water 7 as a ground electrode. Further, a water tank 20 for self-balancing is provided adjacent to one partition plate 44, and this water tank 2 can be expanded and contracted in a double structure so as to be used for natural drainage at a predetermined position (h0). The drainage pipe 81 is provided. Drainage pipe 8 1 is a transfer pipe to the drain tank 32.
The double-structured drainage pipe 81 that can be expanded and contracted is for the purpose of coping with the change in the specific gravity of the waste liquid 6 that varies depending on the type of ink used in the printing press. The balance water level (h0) is determined according to the specific gravity of the waste liquid 6. It can be adjusted.

また、仕切り板44と仕切り板45を隣接させることにより、この間に廃液6の供給部18を形成する。他方の仕切り板45には、メッシュ電極17を取付けている。メッシュ電極17は、水表面との距離LD1に応じて印加電圧を決定する。例えば、本実施形態においては、印加電圧5kV、LD1=35mmとしてある。
なお、静電界で分離しやすいインキ顔料の場合は、LD=30〜40mmとし、分離しにくい顔料の場合は、LD=25〜30mmとした方が、分離し水表面に堆積したインキ顔料が電極6との接触を防止でき、安全に操業できる。
Further, the partition plate 44 and the partition plate 45 are adjacent to each other, thereby forming the supply unit 18 for the waste liquid 6 therebetween. The mesh electrode 17 is attached to the other partition plate 45. The mesh electrode 17 determines the applied voltage according to the distance LD1 with the water surface. For example, in the present embodiment, the applied voltage is 5 kV and LD1 = 35 mm.
In the case of an ink pigment that is easily separated by an electrostatic field, LD = 30 to 40 mm, and in the case of a pigment that is difficult to separate, the ink pigment that is separated and deposited on the water surface is the electrode that has LD = 25 to 30 mm. 6 can be prevented and can be operated safely.

そして、第1の処理槽21から第2の処理槽22へは、洗浄液を供給する流通部50を介して再生洗浄液が流れる構成を採用している。
第2の処理槽22は、再生洗浄液の供給部24を備えるが、下部に隙間を有する2枚の仕切り板25,48で仕切られている。
ここで、上述した第1の処理槽21および第2の処理槽22には、液供給部18,24の中央部に挟まれるように2枚の仕切り板47,48を設けてある。仕切り板47,48を設けた理由は、廃液または洗浄液が処理槽内で攪拌されるのを防止するためである。第2の処理槽22で処理された再生洗浄液8は、流通部51を介して、回収タンク30に流れ込み、回収される。
Then, a configuration is adopted in which the regenerated cleaning liquid 8 flows from the first processing tank 21 to the second processing tank 22 via a circulation unit 50 that supplies the cleaning liquid.
The second treatment tank 22 includes a supply unit 24 for the regenerated cleaning solution 8 , but is partitioned by two partition plates 25 and 48 having a gap in the lower part.
Here, in the first processing tank 21 and the second processing tank 22 described above, two partition plates 47 and 48 are provided so as to be sandwiched between the central portions of the liquid supply units 18 and 24. The reason why the partition plates 47 and 48 are provided is to prevent the waste liquid 6 or the cleaning liquid from being stirred in the treatment tank. The regenerated cleaning liquid 8 processed in the second processing tank 22 flows into the recovery tank 30 via the circulation part 51 and is recovered.

次に、水と廃液の供給や再生洗浄液の回収及び分離した水、インキ顔料の排水・除去方法について説明する。
マイナス電極として使用する水7は、あらかじめ手動もしくは不図示のポンプ等により所定位置まで供給しておく。ここで、水タンク20の水位h0は、上述した実施形態と同様に決定されるが、排水パイプ81の上部開口位置により調整されることになる。
そして、水7を供給した後、送液ポンプ34により、廃液を廃液タンク31から供給パイプを介して第1の処理槽21の供給部へ圧送する。
第2の処理槽22で完全に処理された再生洗浄液8は、バルブ35の開操作で再生液タンク33に回収される。なお、流量規制バルブ42は、第1の処理槽21と廃液タンク31の間の流量を規制するバルブである。
また、再生処理により分離し第1の処理槽21の底部側に沈降した水は、水タンク20に流入し、所定水位(h0)を超えた水は二重構造で伸縮可能とした排水パイプ81によって排水し、パイプにてタンク32に回収される。
以上の廃液供給、再生液回収、分離水排水の作業は、処理作業中は連続して行われる。
Next, supply of water and waste liquid 6 , recovery of the regenerated cleaning liquid 8 , and a method for draining and removing the separated water and ink pigment will be described.
The water 7 used as the negative electrode is supplied in advance to a predetermined position manually or by a pump (not shown). Here, the water level h0 of the water tank 20 is determined in the same manner as in the above-described embodiment, but is adjusted by the upper opening position of the drainage pipe 81.
Then, after supplying the water 7, the waste liquid 6 is pumped from the waste liquid tank 31 to the supply section of the first treatment tank 21 through the supply pipe by the liquid feed pump 34.
The regenerated cleaning liquid 8 completely processed in the second processing tank 22 is collected in the regenerated liquid tank 33 by opening the valve 35. The flow rate regulating valve 42 is a valve that regulates the flow rate between the first treatment tank 21 and the waste liquid tank 31.
In addition, the water 7 separated by the regeneration process and settled on the bottom side of the first treatment tank 21 flows into the water tank 20, and the water 7 exceeding the predetermined water level (h0) can be expanded and contracted by a double structure. The water is drained by the pipe 81 and collected in the tank 32 by the pipe.
The above-described waste liquid supply, reclaimed liquid recovery, and separated water drainage operations are continuously performed during the processing operation.

なお処理により分離したインキ顔料の除去は、上述した処理作業を中止したのち行う。このインキ顔料除去作業は、定期的に(例えば1回/週)行うものである。その手順は、次の通りである。
第1の処理槽21、第2の処理槽22の低部に設けた排水管のバルブ36,37を開き、廃液タンク31の直前に設けてあるインキ顔料除去ろ過器38に、廃液6、水7と一緒に排出する。
この時に、分離して水7の表面に付着しているインキ顔料は、廃液6や水7とともに排出されるが、ろ過器38にてインキ顔料はろ過器38に付着し、廃液6と水7が廃液タンク31へ回収される。ろ過器38に付着したインキ顔料は、ろ過器38に設けてあるフィルターごと廃棄される。その後、新たなフィルターをろ過器38にセットし、次の処理まで待機しておく。
The removal of the ink pigment separated by the treatment is performed after the above-described treatment operation is stopped. This ink pigment removal operation is performed periodically (for example, once / week). The procedure is as follows.
The drain pipe valves 36 and 37 provided in the lower part of the first treatment tank 21 and the second treatment tank 22 are opened, and the waste liquid 6 and water are supplied to the ink pigment removal filter 38 provided immediately before the waste liquid tank 31. Drain together with 7.
At this time, the ink pigment separated and adhering to the surface of the water 7 is discharged together with the waste liquid 6 and the water 7, but the ink pigment adheres to the filter 38 by the filter 38, and the waste liquid 6 and the water 7. Is collected in the waste liquid tank 31. The ink pigment adhering to the filter 38 is discarded together with the filter provided in the filter 38. Thereafter, a new filter is set in the filter 38 and waits until the next processing.

以上、本発明の実施の形態について説明したが、勿論、本発明はこれに限定されることなく、本発明の技術的思想に基いて種々の変形及び変更が可能である。
例えば、上記実施の形態では、再生液処理槽を2槽設けたが、第1の処理槽21及び(または)第2の処理槽22を付加して、3槽以上設けてもよいし、インキ顔料の成分等によっては第1の処理槽21のみでも良い。
またセルフバランス水タンク20の中に、自然排水用の二重構造で伸縮可能とした排水パイプ81を設けてあるが、これに限らず、先に説明した自然排水孔13をタンク0外部に設ける方法でもよい。
The embodiment of the present invention has been described above. Of course, the present invention is not limited to this, and various modifications and changes can be made based on the technical idea of the present invention.
For example, in the above-described embodiment, two regenerated liquid treatment tanks are provided, but three or more tanks may be provided by adding the first treatment tank 21 and / or the second treatment tank 22 or ink. Only the first treatment tank 21 may be used depending on the components of the pigment.
Further, the self-balance water tank 20 is provided with a drainage pipe 81 that can be expanded and contracted with a double structure for natural drainage. However, the natural drainage hole 13 described above is not limited to this and is provided outside the tank 20. The method of providing may be sufficient.

本発明の第1の実施形態に係る廃液再生装置を示す概略構成図である。図1(a)は注水状態、図1(b)は洗浄液供給状態、図1(c)は再生稼動状態を示す。It is a schematic block diagram which shows the waste liquid reproduction | regeneration apparatus which concerns on the 1st Embodiment of this invention. 1A shows a water injection state, FIG. 1B shows a cleaning liquid supply state, and FIG. 1C shows a regeneration operation state. 本発明の第2の実施形態に係る廃液再生装置を示す概略構成図である。It is a schematic block diagram which shows the waste liquid reproduction | regeneration apparatus which concerns on the 2nd Embodiment of this invention. 本発明の第3の実施形態に係る廃液再生装置を示す概略構成図である。It is a schematic block diagram which shows the waste liquid reproduction | regeneration apparatus which concerns on the 3rd Embodiment of this invention. 従来の廃液再生装置の一構成例の断面概略図である。It is the cross-sectional schematic of the example of 1 structure of the conventional waste liquid reproduction | regeneration apparatus. 従来の廃液再生装置の原理的構成を示す概略断面図である。It is a schematic sectional drawing which shows the fundamental structure of the conventional waste-liquid reproduction | regeneration apparatus.

符号の説明Explanation of symbols

1 廃液再生装置
2 廃液再生装置
3 廃液再生装置
5 廃液再生装置
7 水
8 再生洗浄液
9 インキ顔料
11 処理槽
12 再生液回収孔
13 自然排水孔
14,15 仕切壁
16 連通部
17 メッシュ電極
18 廃液供給部
20 水タンク
21 第1の再生液処理槽
22 第2の再生液処理槽
23 堰壁
24 供給部
25 仕切り板
26 メッシュ電極
27 仕切り板
28 マイナス電極
30 回収タンク
31 廃液タンク
32 排水タンク
33 再生液タンク
34 送液ポンプ
35〜37 バルブ
38 顔料除去ろ過器
42 流量規制バルブ
44,45 仕切り板
61 処理槽
62 仕切り板
63,66 縦壁
65 隙間
67 電極
68 インク顔料
69 分離した水
70 分離し凝集した水
72 水位計
73 排水孔
74 バルブ
DESCRIPTION OF SYMBOLS 1 Waste liquid reproduction | regeneration apparatus 2 Waste liquid reproduction | regeneration apparatus 3 Waste liquid reproduction | regeneration apparatus 5 Waste liquid reproduction | regeneration apparatus 7 Water 8 Regenerated washing | cleaning liquid 9 Ink pigment 11 Treatment tank 12 Recycled liquid collection | recovery hole 13 Natural drainage hole 14,15 Partition wall 16 Communication part 17 Mesh electrode 18 Waste liquid supply Section 20 Water tank 21 First regeneration liquid treatment tank 22 Second regeneration liquid treatment tank 23 Weir wall 24 Supply section 25 Partition plate 26 Mesh electrode 27 Partition plate 28 Negative electrode 30 Recovery tank 31 Waste liquid tank 32 Waste tank 33 Regeneration liquid Tank 34 Liquid feed pump 35-37 Valve 38 Pigment removal filter 42 Flow regulating valve 44, 45 Partition plate 61 Processing tank 62 Partition plate 63, 66 Vertical wall 65 Gap 67 Electrode 68 Ink pigment 69 Separated water 70 Separated and aggregated Water 72 Water level gauge 73 Drain hole 74 Valve

Claims (5)

印刷機で使用した水を含む廃液を貯留する処理槽と、
前記処理槽内に電界を発生させる電界生成手段と、を備える廃液再生装置において、
前記処理槽内を仕切る第1の仕切壁と、
前記処理槽内を前記第1の仕切壁により仕切られた一方の空間である水貯留槽と、
前記水貯留槽に設けられた排水開口と、
前記処理槽の底面と前記第1の仕切壁との間に設けられた第1の隙間とを備え、
前記電界発生手段は、前記廃液中に含まれた水を、前記処理槽の底部に静電凝集させ
前記隙間は、前記静電凝集させた水を前記処理槽内の前記第1の仕切壁により仕切られた他方の空間から前記水貯留槽に導出する連通部として機能し、
前記排水開口は、前記水貯留槽内の水を自然排水して前記水貯留槽内の水位を所定水位に調整する水位調整機構として機能する
ことを特徴とする廃液再生装置
A treatment tank for storing waste liquid containing water used in the printing press;
In a waste liquid regenerating apparatus comprising an electric field generating means for generating an electric field in the processing tank,
A first partition wall for partitioning the inside of the treatment tank ;
A water storage tank that is one space partitioned by the first partition wall in the treatment tank ;
A drain opening provided in the water storage tank;
A first gap provided between a bottom surface of the treatment tank and the first partition wall;
It said electric field generating means, the water contained in the waste liquid, is electrostatically agglomerate at the bottom of the treatment tank,
The gap, the were electrostatically agglomerated water, acts as a communicating unit that derives the water reservoir from the other space partitioned by the first partition wall of the processing bath,
The wastewater recycling apparatus , wherein the drainage opening functions as a water level adjusting mechanism that naturally drains the water in the water storage tank and adjusts the water level in the water storage tank to a predetermined water level .
前記所定水位は、処理される廃液の比重に基づき定められることを特徴とする請求項1記載の廃液再生装置。 Wherein the predetermined water level, characterized in that it is determined based on the specific gravity of the waste liquid to be processed, according to claim 1 Symbol placement of waste reproducing apparatus. 前記排水開口は排水孔であって、  The drain opening is a drain hole,
前記処理槽は前記底面と周壁とを有し、  The treatment tank has the bottom surface and a peripheral wall,
前記排水開口は前記周壁に設けられ、  The drain opening is provided in the peripheral wall;
前記第1の仕切壁は前記周壁の前記排水開口が設けられた第1の内壁面に対向するように設けられている  The first partition wall is provided so as to face the first inner wall surface provided with the drainage opening of the peripheral wall.
ことを特徴とする、請求項1又は2記載の廃液再生装置。The waste liquid regenerating apparatus according to claim 1 or 2, characterized by the above.
前記処理槽は前記底面と周壁とを有し、  The treatment tank has the bottom surface and a peripheral wall,
前記水貯留槽には、前記排水開口に相当する上部開口を有し伸縮可能な排水パイプが設けられる  The water storage tank is provided with an extendable drain pipe having an upper opening corresponding to the drain opening.
ことを特徴とする、請求項1又は2記載の廃液再生装置。The waste liquid regenerating apparatus according to claim 1 or 2, characterized by the above.
前記他方の空間を形成する前記周壁に設けられた再生液回収孔と、  A regenerating liquid recovery hole provided in the peripheral wall forming the other space;
前記周壁の前記再生液回収孔が設けられた第2の内壁面に対向するとともに、下方端部が前記第1の仕切壁の下方端部よりも上方に配置され前記処理槽の前記底面との間に隙間が形成されるように設けられた第2の仕切壁との間に設けられた回収再生液貯留部と、  The lower wall is opposed to the second inner wall surface of the peripheral wall provided with the regeneration liquid recovery hole, and the lower end portion is disposed above the lower end portion of the first partition wall. A recovered and regenerated liquid storage section provided between the second partition wall provided so that a gap is formed therebetween,
前記第2の仕切壁の下方端部と前記第2の内壁面との間に水平配置されたプラス電極と、  A positive electrode horizontally disposed between a lower end portion of the second partition wall and the second inner wall surface;
前記処理槽の前記底面に設けられたマイナス電極であるアース電極と、を備え、  A ground electrode that is a negative electrode provided on the bottom surface of the treatment tank,
前記電界発生手段は、前記プラス電極と前記マイナス電極とをそなえている  The electric field generating means includes the positive electrode and the negative electrode.
ことを特徴とする、請求項3又は4記載の廃液再生装置。The waste liquid regenerating apparatus according to claim 3 or 4, characterized by the above.
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