JP3100053U - Waste liquid treatment equipment - Google Patents

Waste liquid treatment equipment Download PDF

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JP3100053U
JP3100053U JP2003270770U JP2003270770U JP3100053U JP 3100053 U JP3100053 U JP 3100053U JP 2003270770 U JP2003270770 U JP 2003270770U JP 2003270770 U JP2003270770 U JP 2003270770U JP 3100053 U JP3100053 U JP 3100053U
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waste liquid
tank
cylindrical container
filtration
filtrate
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石村 和彦
杉岡 忠雄
吉原 清次
鵜川 直彦
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菱明技研株式会社
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Abstract

【課題】強アルカリ性廃液の中和と含有される高濃度の有機物の除去を行う際、中和時には反応性を向上するために強攪拌を要する一方、後工程では凝集固化により生成するフロック状凝集物をできるだけ大きくする必要性から、弱攪拌が必要である。これらの攪拌操作の調整は非常に困難である上、濾過分離した凝集物の含水率が高くハンドリング上不都合であった。
【解決手段】偏心カム駆動で円周方向に往復させる機能を有する円筒状容器1の内周を複数分割する位置にバッフル6を装備し、該円筒状容器の下部に処理液を自動排出する電動操作弁7を設置した反応槽、該反応槽下部に該処理液を導入するよう配置され、濾過材10を敷いた金網9を上部、濾液を貯留する受槽を下部に配置した濾過槽8、該濾過槽内の濾過液を吸引排出する吸引ポンプ12を備えていることを特徴とする廃液処理装置。
【選択図】 図1
[PROBLEMS] To neutralize strongly alkaline waste liquid and remove high-concentration organic substances contained therein, strong neutralization is required during neutralization to improve reactivity, while floc-like aggregation generated by aggregation and solidification is required in a subsequent step. Because of the need to make the objects as large as possible, weak stirring is required. Adjustment of these stirring operations is extremely difficult, and the water content of the aggregate separated by filtration is high, which is inconvenient in handling.
A baffle (6) is provided at a position where the inner periphery of a cylindrical container (1) having a function of reciprocating in the circumferential direction by eccentric cam drive is divided into a plurality of parts, and an electric motor for automatically discharging a processing liquid to a lower part of the cylindrical container. A reaction tank in which an operation valve 7 is installed, a wire mesh 9 arranged to introduce the treatment liquid into a lower portion of the reaction tank, a wire mesh 9 on which a filter medium 10 is laid, and a filter tank 8 in which a receiving tank for storing the filtrate is arranged at a lower portion; A waste liquid treatment apparatus comprising a suction pump 12 for sucking and discharging a filtrate in a filtration tank.
[Selection diagram] Fig. 1

Description

本考案は主として、空調室内機洗浄、床清掃、床コート剥離処理などで発生する強アルカリ性で高濃度の有機物を含有する廃液の処理装置に関するものである。 The present invention mainly relates to an apparatus for treating a waste liquid containing strongly alkaline and high-concentration organic substances generated in an air-conditioning indoor unit cleaning, floor cleaning, floor coating peeling processing and the like.

空調室内機洗浄、床清掃、床コート剥離処理では、洗浄効果を上げるためアルカリ性液剤を使用するため、pH12以上の強アルカリ性廃液が発生する。通常これらの廃液は50m3/日以下の少量であるため、下水道放流基準の適用外であるものの、このような、強アルカリ水を放流することは、下水処理設備運用の面で好ましいことではない。又これらの廃液にはコート剤として使用される高分子樹脂などが含まれており、そのまま放流することは、高濃度の有機物の放流につながり、環境負荷を増大させることとなり問題である。
従来、これらの問題を解決するため、廃液に酸を加えて中和するとともに、中和に伴なって溶解していた高分子樹脂が析出して生成する浮遊性物質の凝集固化を促進するために凝集剤を添加してフロック状とし、その後フロック状凝集物を分離処理していた。
例えばペール缶やバケツなどの処理容器に廃液を投入して、中和剤、凝集剤を少量ずつ溶かし入れながら、10分間程度撹拌して、pHを6.5〜7.5の中性域に調整すると共に、浮遊性物質を凝集固化させる。次いで処理後の廃液を静置してフロック状とし、このフロック状凝集物をざる等ですくい上げて分離除去する等の方法が用いられている。
In an air-conditioning indoor unit cleaning, floor cleaning, and floor coat peeling treatment, an alkaline liquid is used to enhance the cleaning effect, and a strong alkaline waste liquid having a pH of 12 or more is generated. Usually, these waste liquids are in a small amount of 50 m 3 / day or less, so they are not applicable to the sewage discharge standard. However, discharging such strong alkaline water is not preferable in terms of sewage treatment equipment operation. . Further, these waste liquids contain a polymer resin or the like used as a coating agent, and discharging them as it is leads to discharge of high-concentration organic substances, which increases the environmental load and is a problem.
Conventionally, in order to solve these problems, to neutralize the waste liquid by adding an acid, and to promote coagulation and solidification of the floating substance generated by precipitation of the polymer resin dissolved with the neutralization To form a floc, and then the floc-like aggregate was separated.
For example, the waste liquid is put into a processing container such as a pail can or a bucket, and while the neutralizing agent and the coagulant are being dissolved little by little, stirring is performed for about 10 minutes to adjust the pH to a neutral range of 6.5 to 7.5, Coagulate and solidify the floating substance. Next, a method is used in which the waste liquid after the treatment is allowed to stand to form a floc, and the floc-like aggregate is scooped up and separated and removed.

上述のアルカリ性廃液処理では、中和時には反応性を向上するために強攪拌を要する一方、後工程での濾過速度の上昇と濾液中に漏れ出る凝集物を少なくするためには、凝集固化により生成するフロック状凝集物をできるだけ大きくする必要があり、そのためには弱い攪拌が必要である。従来の人手作業による方法ではこれらの攪拌操作の調整は非常に困難である上、濾過分離した凝集物の含水率が高く、その後の燃焼処分等のハンドリング上極めて不都合であった。また、中和処理、薬剤投入、攪拌、凝集物の分離除去および処理水の廃棄は人手作業にたよっており、時間と労力を要する難点があった。
本考案は上記の課題を解決しようとするものであり、強アルカリ性廃液の中和と含有される高濃度の有機物の除去を短時間に効率良く行える廃液処理装置を提供することを目的とする。
In the above-mentioned alkaline waste liquid treatment, strong neutralization is required to improve the reactivity during neutralization, but in order to increase the filtration rate in the subsequent process and reduce the aggregates leaking out into the filtrate, it is generated by coagulation and solidification. It is necessary to make the floc-like aggregates as large as possible, which requires weak stirring. It is very difficult to adjust these stirring operations by the conventional manual method, and the water content of the aggregate separated by filtration is high, which is extremely inconvenient in handling such as subsequent combustion disposal. Further, the neutralization treatment, the introduction of the chemical, the stirring, the separation and removal of the aggregates, and the disposal of the treated water are manually performed, and have a drawback that time and labor are required.
An object of the present invention is to solve the above-mentioned problem, and an object of the present invention is to provide a waste liquid treatment apparatus capable of efficiently neutralizing a strongly alkaline waste liquid and removing high-concentration organic substances contained therein in a short time.

本考案は、アルカリ性廃液の処理装置において、偏芯カム駆動で円周方向に往復させる機能を有する円筒状容器の内周を複数分割する位置にバッフルを装備し、該円筒状容器の下部に処理液を自動排出する電動操作弁を設置した反応槽、該反応槽下部に該処理液を導入するよう配置され、濾過材を敷いた金網を上部、濾液を貯留する受槽を下部に配置した濾過槽、該濾過槽内の濾過液を吸引排出する吸引ポンプを備えていることを特徴とする廃液処理装置を提供するものである。 The present invention provides an apparatus for treating an alkaline waste liquid, in which a baffle is provided at a position where the inner periphery of a cylindrical container having a function of reciprocating in the circumferential direction by eccentric cam drive is divided into a plurality of portions, and a lower portion of the cylindrical container is treated. A reaction tank equipped with an electrically operated valve that automatically discharges the liquid, a filtration tank arranged so as to introduce the treatment liquid into the lower part of the reaction tank, a wire mesh lined with a filter medium at the top, and a receiving tank for storing the filtrate at the bottom. And a suction pump for sucking and discharging the filtrate in the filtration tank.

上記考案において、円筒状容器が円周方向に往復運動しており、内周にそって設置されたバッフルにより、円筒状容器内の処理廃液は円周にそって一定時間間隔で逆方向に押し流される。このため、円筒状容器内の処理廃液は一定時間間隔ごとに反転する流れを起こし、廃液中に順次投入される中和剤あるいは凝集剤との混合効果が格段に良くなる。その結果、撹拌時間を短くしても確実に中和・凝集反応が進行するようになる。
また、円筒状容器内部に攪拌羽根を設置して混合する場合のように、生成したフロック状凝集物が回転物に直接接触して引きちぎられることがないので、破壊されずに大きくなるため、次の濾過分離工程での濾過抵抗が減少し、濾過時間を飛躍的に短縮できる効果をもたらす。
また濾過材を通過し濾液中に漏れ出る凝集物も少なくなる。さらに、濾過槽に排出された処理液は、吸引ポンプの減圧吸引作用で濾過槽内が減圧された状態で濾過されるので、濾過速度が格段に速くなり、中和・凝集反応と濾過を合わせた処理時間は大幅に短縮されると共に、濾過分離された凝集物の含水率も極めて小さくなる。
よって本考案の廃液処理装置により、作業時間短縮化と省力化が図られる。
In the above invention, the cylindrical container is reciprocating in the circumferential direction, and the processing waste liquid in the cylindrical container is swept in the opposite direction at regular time intervals along the circumference by the baffles installed along the inner circumference. It is. For this reason, the processing waste liquid in the cylindrical container generates a flow that reverses at regular time intervals, and the effect of mixing with the neutralizing agent or the coagulant sequentially added to the waste liquid is remarkably improved. As a result, even if the stirring time is shortened, the neutralization / aggregation reaction proceeds reliably.
Further, unlike the case where mixing is performed by installing stirring blades inside the cylindrical container, the generated floc-like aggregates do not directly come into contact with the rotating object and are not torn off, so that the floc-like aggregates become large without being destroyed. This reduces the filtration resistance in the filtration / separation step, thereby providing an effect of dramatically shortening the filtration time.
Also, the amount of aggregates that pass through the filter medium and leak into the filtrate is reduced. Furthermore, the processing liquid discharged into the filtration tank is filtered in a state where the pressure inside the filtration tank is reduced by the reduced pressure suction of the suction pump, so that the filtration speed is significantly increased, and the neutralization / aggregation reaction and the filtration are combined. The treatment time is greatly reduced, and the water content of the aggregate separated by filtration becomes extremely small.
Therefore, with the waste liquid treatment apparatus of the present invention, the working time can be reduced and labor can be saved.

本考案の実施形態を図面により説明する。第1図は本考案の一実施例の構成図、第2図は反応槽組立て状態の部分的拡大図の例である。 An embodiment of the present invention will be described with reference to the drawings. FIG. 1 is a configuration diagram of one embodiment of the present invention, and FIG. 2 is an example of a partially enlarged view of a reactor assembled state.

インバータ付き駆動モータ軸2に取り付けた偏芯カム3が回転することにより、この回転運動がコネクティングロッド4経由で駆動アーム5に伝えられ、円筒状容器1を円周方向に往復運動させる。
インバータ付き駆動モータ軸2の回転速度は、インバータにより自由に変えることができるので、攪拌効果とフロックの生成に最適となるよう円筒状容器1の円周方向往復運動の速度を調整することが可能である。
When the eccentric cam 3 attached to the drive motor shaft 2 with the inverter rotates, this rotational motion is transmitted to the drive arm 5 via the connecting rod 4, and reciprocates the cylindrical container 1 in the circumferential direction.
Since the rotation speed of the drive motor shaft 2 with an inverter can be freely changed by the inverter, the speed of the reciprocating motion of the cylindrical container 1 in the circumferential direction can be adjusted so as to be optimal for the stirring effect and the generation of flocs. It is.

円筒状容器1の内面には、4分割する位置にバッフル6が設置され、底部中央に排出口を設けて、電動操作弁7が取り付けられ、電動操作弁7の下方配管は直下に設置された濾過槽8の濾過材10の表面に向けて開放されている。 On the inner surface of the cylindrical container 1, a baffle 6 was installed at a position where it was divided into four parts, a discharge port was provided at the center of the bottom, an electrically operated valve 7 was attached, and the lower piping of the electrically operated valve 7 was installed immediately below. It is open to the surface of the filter medium 10 of the filter tank 8.

駆動モータ軸2の起動後、設定(5〜10分)時間後に駆動モータ軸2が停止し、同時に電動操作弁7が開くまでの一連の操作が進行するようタイマー設定してあり、設定時間の変更も可能である。 After the drive motor shaft 2 is started, a timer is set so that the drive motor shaft 2 stops after a set time (5 to 10 minutes) and a series of operations until the electric operation valve 7 opens at the same time. Changes are possible.

pH12以上の強アルカリ性のビル床清掃廃液40リットルを容積70リットルの円筒状容器1に入れ、自動運転を開始した後、凝集剤及び中和剤を順次添加し、pHが6.5〜7.5になるまで中和・凝集処理する。 Put 40 liters of strong alkaline building floor cleaning wastewater of pH 12 or more into a cylindrical container 1 having a capacity of 70 liters, start automatic operation, and then add a flocculant and a neutralizing agent sequentially until the pH becomes 6.5 to 7.5. Neutralize / aggregate.

円筒状容器1底部中央の排出口から抜き出された中和・凝集物生成処理後の廃液は、濾過槽8の濾過材10上に流入する。濾過槽8はフロック状の凝集物を廃水と分離する機能を持ち、金網9の上に敷かれた濾過材10の上に堆積した凝集物は一連の操作終了後、濾過材10と共に取り出し廃棄物として燃焼等の処理をする。濾過材10としては、一般に普及している紙製または布製が適用可能である。 The waste liquid after the neutralization and agglomerate generation process, which has been extracted from the outlet at the center of the bottom of the cylindrical container 1, flows into the filter medium 10 in the filter tank 8. The filtration tank 8 has a function of separating floc-like aggregates from wastewater, and the aggregates deposited on the filter medium 10 laid on the wire mesh 9 are removed together with the filter medium 10 after a series of operations, and the waste is removed. And processing such as combustion. As the filter medium 10, paper or cloth, which is widely used, can be used.

濾過槽8内の廃水を外部に排出するために、濾過槽8の側部に排出ホース11を取りつけ、吸引ポンプ12と接続している。吸引ポンプ12は真空式を使用することで、濾過槽8内を減圧状態に保持しながらフロック状の凝集物を濾過材10上に分離させるので、濾過速度を格段に早くでき,凝集物の含水率も下げることができる。 In order to discharge wastewater in the filtration tank 8 to the outside, a discharge hose 11 is attached to a side of the filtration tank 8 and connected to a suction pump 12. By using a vacuum pump, the suction pump 12 separates floc-like aggregates onto the filter medium 10 while keeping the inside of the filtration tank 8 under reduced pressure, so that the filtration speed can be remarkably increased, and the aggregates contain water. The rate can also be reduced.

本実施例では、円筒状容器1の容積を70リットル、バッフル6の数は4としたが、これらに限定されるものではなく、処理する廃液の量により、その容積は自由に選定できる。
以上の操作によりpH12以上の強アルカリ性で高分子樹脂等の有機物を多量に含んだビル床清掃廃液は、有機物が除去された中性溶液となって、下水道放流しても、環境負荷を上げないレベルまで浄化される。
In the present embodiment, the volume of the cylindrical container 1 is set to 70 liters, and the number of the baffles 6 is set to 4. However, the present invention is not limited to these, and the volume can be freely selected depending on the amount of waste liquid to be treated.
Through the above operation, the wastewater for cleaning the floor of a building containing a large amount of organic substances such as high-polymer resins and a strong alkali having a pH of 12 or more becomes a neutral solution from which the organic substances have been removed, and does not increase the environmental burden even if discharged into the sewer. Purified to the level.

空調室内機洗浄廃液や床コート剥離処理廃液もビル床清掃廃液と同様に処理できる。 The air-conditioning indoor unit cleaning waste liquid and the floor coat peeling treatment waste liquid can be treated in the same manner as the building floor cleaning waste liquid.

本考案の一実施形態に係る装置の説明図である。FIG. 3 is an explanatory diagram of an apparatus according to an embodiment of the present invention. 本考案の反応槽組立て状態の部分的拡大図である。FIG. 3 is a partially enlarged view of the reactor according to the present invention in an assembled state.

符号の説明Explanation of reference numerals

1   円筒状容器
2   駆動モータ軸
3   偏芯カム
4   コネクティングロッド
5   駆動アーム
6   バッフル
7   電動操作弁
8   濾過槽
9   金網
10   濾過材
11   排出ホース
12   吸引ポンプ

1 Cylindrical container
2 Drive motor shaft
3 Eccentric cam
4 Connecting rod
5 Drive arm
6 Baffle
7 Electric operated valve
8 Filtration tank
9 Wire mesh
10 Filter media
11 Discharge hose
12 Suction pump

Claims (1)

有機物を含有するアルカリ性廃液の処理装置において、偏芯カム駆動で円周方向に往復させる機能を有する円筒状容器の内周を複数分割する位置にバッフルを装備し、該円筒状容器の下部に処理液を自動排出する電動操作弁を設置した反応槽、該反応槽下部に該処理液を導入するよう配置され、濾過材を敷いた金網を上部、濾液を貯留する受槽を下部に配置した濾過槽、該濾過槽内の濾過液を吸引排出する吸引ポンプを備えていることを特徴とする廃液処理装置。
In an apparatus for treating an alkaline waste liquid containing an organic substance, a baffle is provided at a position where the inner periphery of a cylindrical container having a function of reciprocating in the circumferential direction by eccentric cam drive is divided into a plurality of portions, and a lower portion of the cylindrical container is treated. A reaction tank equipped with an electrically operated valve that automatically discharges the liquid, a filtration tank arranged so as to introduce the treatment liquid into the lower part of the reaction tank, a wire mesh lined with a filter medium at the top, and a receiving tank for storing the filtrate at the bottom. And a suction pump for sucking and discharging the filtrate in the filtration tank.
JP2003270770U 2003-08-26 2003-08-26 Waste liquid treatment equipment Expired - Fee Related JP3100053U (en)

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