JP4933115B2 - Waste water crystallization treatment equipment - Google Patents

Waste water crystallization treatment equipment Download PDF

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JP4933115B2
JP4933115B2 JP2006056975A JP2006056975A JP4933115B2 JP 4933115 B2 JP4933115 B2 JP 4933115B2 JP 2006056975 A JP2006056975 A JP 2006056975A JP 2006056975 A JP2006056975 A JP 2006056975A JP 4933115 B2 JP4933115 B2 JP 4933115B2
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crystallization
stirrer
treatment apparatus
reaction tank
waste water
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JP2007229670A (en
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紀夫 山田
康彦 鈴木
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Swing Corp
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Swing Corp
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Description

本発明は、晶析対象成分を含む排水、例えば下水、し尿、浄化槽汚泥、一般廃棄物処理場浸出水、工場排水、またはこれらを生物処理した排水の晶析処理、特に、炭酸カルシウム、又はリン酸ヒドロキシアパタイトの晶析処理装置に関するものである。   The present invention relates to crystallization treatment of wastewater containing a crystallization target component, for example, sewage, human waste, septic tank sludge, general waste treatment plant leachate, industrial wastewater, or wastewater obtained by biological treatment of these, particularly calcium carbonate or phosphorus. The present invention relates to an apparatus for crystallizing acid hydroxyapatite.

従来のこの種の排水の晶析処理装置として、排水を収容する晶析反応槽を備え、該晶析反応槽に晶析対象成分を含む排水を収容し、縦型攪拌機で薬品を添加しながら攪拌混合して、炭酸カルシウム又はリン酸ヒドロキシンアパタイト等の晶析種晶を晶析する晶析処理装置がある。
特開2004−321992号公報
As a conventional waste water crystallization treatment apparatus, a crystallization reaction tank for containing waste water is provided, and waste water containing crystallization target components is contained in the crystallization reaction tank, while adding chemicals with a vertical stirrer. There is a crystallization treatment apparatus that mixes with stirring to crystallize a crystal seed crystal such as calcium carbonate or hydroxyapatite phosphate.
JP 2004-321992 A

上記従来の排水の晶析処理装置において、攪拌機が停止すると、晶析物が晶析反応槽の底部に沈降圧密し固くなってしまう。この後、攪拌機を再起動しようとすると、攪拌機の攪拌羽根がこの沈降圧密して固まった晶析物に拘束され、起動に非常に大きな動力が必要となったり、再起動ができなくなるという問題があった。 In the conventional waste water crystallization treatment apparatus, when the stirrer stops, the crystallization product settles and becomes hard at the bottom of the crystallization reaction tank. After that, when trying to restart the stirrer, the stirrer blade of the stirrer is restrained by the sedimentation-consolidated and solidified crystallized matter, and there is a problem that very large power is required for starting or restarting is impossible. there were.

本発明は上述の点に鑑みてなされたもので、上記問題点を除去し、攪拌機が停止し、晶析物が晶析反応槽の底部に沈降圧密し固くなってしまっても攪拌機を大きな動力を必要とすることなく、再起動できる排水の晶析処理装置を提供することを目的とする。 The present invention has been made in view of the above-mentioned points, and eliminates the above problems, stops the stirrer, and even if the crystallized product settles and becomes hard at the bottom of the crystallization reaction tank, An object of the present invention is to provide a wastewater crystallization treatment apparatus that can be restarted without requiring any other.

上記課題を解決するため本願発明は、晶析対象成分を含む排水を収容する晶析反応槽と、該晶析反応槽内の排水を攪拌する攪拌機と、該攪拌機を搭載し支持する攪拌機搭載架台を備えた排水の晶析処理装置において、前記晶析反応槽内の内側側面に沿って筒状のバッフル板を設け、前記バッフル板内を貫通して前記攪拌機の回転軸を配置し、前記攪拌機を昇降する昇降装置を設けたことを特徴とする。 In order to solve the above-described problems, the present invention provides a crystallization reaction tank that contains wastewater containing a crystallization target component, a stirrer that stirs the wastewater in the crystallization reaction tank, and a stirrer-mounted base that carries and supports the stirrer. In the waste water crystallization treatment apparatus, a cylindrical baffle plate is provided along the inner side surface in the crystallization reaction tank, the rotating shaft of the stirrer is disposed through the baffle plate, and the stirrer An elevating device for elevating and lowering is provided.

また、本願発明は、上記排水の晶析処理装置において、前記昇降装置は前記攪拌機搭載架台に設置され、前記攪拌機自体を昇降できるようになっていることを特徴とする。 Further, the present invention provides a crystallization apparatus of the waste water, said lifting device is installed in the agitator mounting frame, characterized in that it can now lift the agitator itself.

また、本願発明は、上記排水の晶析処理装置において、前記攪拌機搭載架台は前記昇降装置に設置され、該攪拌機搭載架台を昇降することにより、前記攪拌機を昇降するようになっていることを特徴とする。 Further, the present invention is characterized in that the crystallization apparatus of the waste water, the agitator mounting frame is placed in the lifting device, by elevating the the stirring agitator mounting frame is adapted to lift the agitator And

また、本願発明は、上記排水の晶析処理装置において、前記バッフル板の下部が前記晶析反応槽内側面寄りに傾斜していることを特徴とする。 Further, the present invention provides a crystallization apparatus of the waste water, characterized in that the lower portion of the baffle plate is inclined to the crystallization reaction tank side nearer.

また、本願発明は、上記排水の晶析処理装置において、晶析物の流動を、前記攪拌機による攪拌と、上向水流攪拌又は空気攪拌の併用としたことを特徴とする。 Further, the present invention provides a crystallization apparatus of the waste water, the flow of the crystallization product, wherein the agitation by the stirrer, that it has a combination of upward flow agitation or air agitation.

また、本願発明は、上記排水の晶析処理装置において、前記晶析反応槽の下部に晶析物を排出する排出管を設けたことを特徴とする。 Further, the present invention provides a crystallization apparatus of the waste water, characterized in that a discharge pipe for discharging the crystallization product at the bottom of the crystallization reaction tank.

本願発明によれば、攪拌機を昇降する昇降装置を設けたので、攪拌機が停止し、晶析物が圧密した場合、攪拌機の攪拌羽根を沈降し固く圧密した晶析物の上に位置するように上昇させることにより、攪拌羽根が沈降し固く圧密した晶析物により拘束されることなく、再起動の際、小さい動力で攪拌羽根を回転させて水流を発生させることができ、この水流を固く圧密した晶析物に与えながら、攪拌羽根を徐々に降下させることで、沈降晶析物全体を流動化させることが可能となる。また、晶析反応槽内の内側側面に沿って筒状のバッフル板を設け、バッフル板内を貫通して前記攪拌機の回転軸を配置したので、このバッフル板に囲まれた領域に晶析対象成分を含む排水を供給し、該バッフル板内の排水を攪拌機で攪拌することにより、バッフル板の外側にある処理水に影響を与えることなく、排水とバッフル板の内側の晶析物のみを攪拌できる。 According to the present invention , since an elevating device for raising and lowering the stirrer is provided, when the stirrer is stopped and the crystallized product is consolidated, the stirring blade of the stirrer is settled so as to be positioned on the hard compacted crystallized product. By raising, the stirring blades are not restrained by the settled and compacted crystallized product, and at the time of restarting, the stirring blades can be rotated with a small power to generate a water flow. while applying the the crystallization product, by lowering the stirring blade gradually, it is possible to fluidize the entire precipitation crystallization product. In addition, a cylindrical baffle plate is provided along the inner side surface in the crystallization reaction tank, and the rotating shaft of the stirrer is disposed through the baffle plate. By supplying wastewater containing ingredients and stirring the wastewater in the baffle plate with a stirrer, only the wastewater and the crystallized material inside the baffle plate are stirred without affecting the treated water outside the baffle plate. it can.

また、本願発明によれば、昇降装置は前記攪拌機搭載架台に設置され、攪拌機自体を昇降できるようになっているので、攪拌機の攪拌羽根を晶析反応槽の上下方向の所定の位置に移動させることができる。 Further , according to the present invention , the elevating device is installed on the stirrer mounting base and is capable of moving the stirrer itself, so that the stirring blade of the stirrer is moved to a predetermined position in the vertical direction of the crystallization reaction tank. be able to.

また、本願発明によれば、昇降装置は攪拌機搭載架台を昇降して攪拌機を昇降するようになっているので、攪拌機の攪拌羽根を晶析反応槽の上下方向の所定の位置に移動させることができる。 Further , according to the present invention , the elevating device is configured to elevate the agitator mounting base and elevate the agitator, so that the agitating blade of the agitator can be moved to a predetermined position in the vertical direction of the crystallization reaction tank. it can.

また、本願発明によれば、バッフル板の下部が晶析反応槽内側面寄りに傾斜して下部の径が拡大しているので、バッフル板の内側の晶析反応部容積を大きくすることができ、またバッフル板の外側を沈降していく晶析物がバッフル板の外側に堆積するのを防止できる。バッフル板の下部の傾斜角度Bは、図1に示すように50度〜70度とするのが好適である。 Further , according to the present invention , since the lower part of the baffle plate is inclined closer to the inner surface of the crystallization reaction tank and the diameter of the lower part is enlarged, the volume of the crystallization reaction part inside the baffle plate can be increased. In addition, it is possible to prevent the crystallized matter that has settled outside the baffle plate from being deposited outside the baffle plate. The inclination angle B of the lower part of the baffle plate is preferably 50 to 70 degrees as shown in FIG.

また、本願発明によれば、攪拌機が停止した際に、水流又は空気攪拌が継続されるため、晶析物の圧密が軽減される。 Moreover, according to this invention , when a stirrer stops, since a water flow or air stirring is continued, consolidation of a crystallized substance is reduced.

また、本願発明によれば、晶析反応槽の下部に晶析物を排出する排出管を設けたので、晶析反応槽の下部に流動している晶析物を流動性のある晶析物と水の混合状態で晶析反応槽外に排出できるので、排出管内の晶析物詰まりを防止できる。 Further , according to the present invention , since the discharge pipe for discharging the crystallized substance is provided at the lower part of the crystallization reaction tank, the crystallized substance flowing at the lower part of the crystallization reaction tank is converted into a crystallized substance having fluidity. Since it can be discharged out of the crystallization reaction tank in a mixed state of water and water, clogging of crystallized substances in the discharge pipe can be prevented.

以下、本発明の実施の形態を図面に基づいて説明する。図1は本発明に係る排水の晶析処理装置の構成例を示す図である。図示するように、晶析処理装置は晶析対象成分を含む排水100を収容する円筒状の晶析反応槽1を備え、該晶析反応槽1の内側に円筒状のバッフル板2を側面に沿って設けている。該バッフル板2の下部2a晶析反応槽1内側面寄りに傾斜している。3は縦型攪拌機であり、該縦型攪拌機3は回転軸6を具備し、該回転軸6に上下方向に所定の間隔で複数ヶ所(図では2ヶ所)の攪拌羽根7−1、7−2が水平面内で回転できるように取り付けられている。なお、図示は省略するが攪拌羽根は該回転軸下方1ヶ所設けてもよい。 Hereinafter, embodiments of the present invention will be described with reference to the drawings. FIG. 1 is a diagram showing a configuration example of a wastewater crystallization treatment apparatus according to the present invention. As shown in the figure, the crystallization treatment apparatus includes a cylindrical crystallization reaction tank 1 that contains drainage 100 containing a crystallization target component, and a cylindrical baffle plate 2 is disposed on the side of the crystallization reaction tank 1. It is provided along. The bottom 2a of the baffle plate 2 is inclined crystallization reaction tank 1 inside surface closer. Reference numeral 3 denotes a vertical stirrer. The vertical stirrer 3 includes a rotating shaft 6, and the rotating shaft 6 has a plurality of stirring blades 7-1 and 7- at predetermined intervals in the vertical direction (two in the figure). 2 is mounted so that it can rotate in a horizontal plane. Incidentally, the stirring blades omitted illustrated may be provided one position downward the rotating shaft.

縦型攪拌機3はチェーンやロープ等の吊り下げ部材4aを介して昇降装置4に吊り下げられ、該昇降装置4は攪拌機搭載架台5に取り付けられている。該昇降装置4はチェーンブロック等の巻上機からなり、吊り下げ部材4aを巻き取り巻き戻すことにより、縦型攪拌機3はガイド部材10に沿って上下に昇降するようになっている。これにより、縦型攪拌機3の攪拌羽根7−1、7−2を晶析反応槽1の上下方向に任意の位置に移動させることができる。また、モータや減速機からなる駆動機8により回転軸6を回転させることにより、攪拌羽根7−1、7−2は水平面内で回転し、回転晶析対象成分を含む排水100が攪拌されるようになっている。 Vertical agitator 3 is suspended to the lifting device 4 via the suspension member 4a such as a chain or a rope, the lifting device 4 is mounted et the agitator mounting frame 5. The elevating device 4 includes a hoist such as a chain block, and the vertical agitator 3 moves up and down along the guide member 10 by winding and unwinding the suspension member 4a. Thereby, the stirring blades 7-1 and 7-2 of the vertical stirrer 3 can be moved to an arbitrary position in the vertical direction of the crystallization reaction tank 1. Further, by rotating the rotating shaft 6 by a driving machine 8 including a motor and a speed reducer, the stirring blades 7-1 and 7-2 rotate in a horizontal plane, and the waste water 100 including the component for rotation crystallization is stirred. It is like that.

晶析対象成分を含む排水100は、排水流入管11を通って晶析反応槽1内のバッフル板2の内側に流入し、攪拌羽根7−1、7−2で攪拌され、排水100は流動する。ここで排水100に、例えば晶析対象成分としてCaが含まれている場合、晶析に必要な薬品として炭酸ナトリウム104を薬品供給管12を通してバッフル板2の内側の排水100に添加されると、新たな晶析物である炭酸カルシウムが流動晶析物の表面に生成される。この晶析物析出により、晶析対象成分が除去された処理水101は、矢印Aに示すように、バッフル板2の下端をくぐり、バッフル板2と晶析反応槽1の間の領域に流入し、この領域で、晶析物と処理水に固液分離する。この処理水101は晶析反応槽1の上部に設けた処理水排出管14を通って槽外に流出する。また、晶析反応槽1内を流動する流動晶析物102は、晶析反応槽1に設けた流動晶析物排出管13を通って流動晶析物102が排出される。   The drainage 100 containing the crystallization target component flows into the inside of the baffle plate 2 in the crystallization reaction tank 1 through the drainage inflow pipe 11 and is stirred by the stirring blades 7-1 and 7-2. To do. Here, when Ca is contained as a crystallization target component in the drainage 100, for example, when sodium carbonate 104 is added to the drainage 100 inside the baffle plate 2 through the chemical supply pipe 12 as a chemical necessary for crystallization, A new crystallized product, calcium carbonate, is generated on the surface of the fluidized crystallized product. As shown by the arrow A, the treated water 101 from which the crystallization target component has been removed by precipitation of the crystallized material passes through the lower end of the baffle plate 2 and flows into the region between the baffle plate 2 and the crystallization reaction tank 1. In this region, the liquid crystal is separated into a crystallized product and treated water. This treated water 101 flows out of the tank through the treated water discharge pipe 14 provided in the upper part of the crystallization reaction tank 1. In addition, the fluidized crystallized substance 102 flowing in the crystallization reaction tank 1 is discharged through the fluidized crystallized substance discharge pipe 13 provided in the crystallization reaction tank 1.

図2は攪拌羽根7−2の構成を示す図で、図2(a)平面図、図2(b)は側面図である。図示するように攪拌羽根7−2は回転軸6の下端部に4枚の羽根板7−2aを同一水平面上に取り付けた形状で、各羽根板7−2aは水平面に対して所定角度θ傾けて配置されている。該攪拌羽根7−2を回転軸6を中心に水平面上で回転させることにより、晶析反応槽1内の排水や流動晶析物に水流を発生させ、攪拌することができる。なお、撹拌羽根7−1も同一構成であり、攪拌羽根7−1の羽根板7−1a(図示せず)と攪拌羽根7−2の羽根板7−2aは水平位置をずらして配置するのが良い。また、羽根板7−1a、7−2aは4枚に限定されるものではなく、例えば2枚、3枚、それ以上でもよい。 2A and 2B are diagrams showing the configuration of the stirring blade 7-2. FIG. 2A is a plan view and FIG. 2B is a side view. As shown in the figure, the stirring blade 7-2 has a shape in which four blade plates 7-2a are mounted on the same horizontal plane at the lower end of the rotating shaft 6, and each blade plate 7-2a is inclined at a predetermined angle θ with respect to the horizontal plane. Are arranged. By rotating the stirring blade 7-2 on a horizontal plane around the rotation shaft 6, a water flow can be generated in the waste water and the fluidized crystallized material in the crystallization reaction tank 1 and stirred. The stirring blade 7-1 has the same configuration , and the blade plate 7-1a (not shown) of the stirring blade 7-1 and the blade plate 7-2a of the stirring blade 7-2 are arranged with their horizontal positions shifted. Is good. Further, the number of blades 7-1a and 7-2a is not limited to four, and may be two, three, or more, for example.

上記構成の排水の晶析処理装置において、停電等により縦型攪拌機3が停止すると、流動晶析物が晶析反応槽1の底部に沈降する。ここで、炭酸カルシウム又はリン酸ヒドロキシアパタイトなどの晶析物は、砂のように沈降後固く圧密し、図3に示すように晶析反応槽1の底部に堆積して沈降圧密晶析物103となってしまう。沈降圧密晶析物103の中に攪拌羽根7−2が存在すると、該沈降圧密晶析物103よって攪拌羽根7−2が拘束される。その後、縦型攪拌機3を再起動しようとしても、攪拌羽根7−2に大きな抵抗がかかり、起動できない場合がある。   In the wastewater crystallization treatment apparatus having the above-described configuration, when the vertical stirrer 3 is stopped due to a power failure or the like, the fluidized crystallization product settles at the bottom of the crystallization reaction tank 1. Here, a crystallized product such as calcium carbonate or hydroxyapatite phosphate is hard compacted after settling like sand, and is deposited on the bottom of the crystallization reaction tank 1 as shown in FIG. End up. When the stirring blade 7-2 exists in the sedimentation-consolidated crystallized product 103, the stirring blade 7-2 is restrained by the sedimentation-consolidated crystallized product 103. Then, even if it tries to restart the vertical stirrer 3, a big resistance will be applied to the stirring blade 7-2 and it may be unable to start.

そこで、停電等により縦型攪拌機3が停止し、図3の状態になった後、図4に示すように、昇降装置4により、縦型攪拌機3を上昇(引き上げ)させ、攪拌羽根7−2を沈降圧密晶析物103の上になるように上昇させ、その位置に保持する。縦型攪拌機3の再起動の際、この状態で駆動機8を起動して、縦型攪拌機3を再起動させると、攪拌羽根7−2は沈降圧密晶析物103の上の排水100中にあるから、小さい動力で再起動し、排水100の攪拌により水流が起こり、沈降圧密晶析物103の上部の晶析物が巻き上がる。一旦巻き上がり流動した晶析物は、排水100と同程度の攪拌抵抗しかかからないため、この状態で徐々に、縦型攪拌機3を降下させ、その攪拌羽根7−2を下げ、所定の位置に戻し、沈降晶析物全体を流動化させることができる。 Therefore, after the vertical stirrer 3 stops due to a power failure or the like and enters the state of FIG. 3, as shown in FIG. Is raised so as to be above the sedimentation-condensed crystallized product 103 and held in that position. When the vertical stirrer 3 is restarted, when the drive unit 8 is started in this state and the vertical stirrer 3 is restarted, the stirring blade 7-2 is put into the drainage 100 on the sedimentary consolidated crystallized product 103. Therefore, it is restarted with a small power, a water flow is generated by stirring the drainage 100, and the crystallized material on the upper part of the sedimentation consolidated crystallized product 103 is rolled up. Once vortices flow was crystallization product, since it only takes the same degree of agitation resistance and drainage 100, gradually in this state, a vertical agitator 3 is lowered, lowering the stirring blade 7-2 back in place The entire precipitated crystallized product can be fluidized.

上記のように、縦型攪拌機3を昇降装置4により昇降できるようにすることにより、晶析反応槽1の底部に沈降圧密する沈降圧密晶析物103に対しても、容易に縦型攪拌機3を再起動させることができる。なお、上記例では、縦型攪拌機3の上部に昇降装置4を介して攪拌機搭載架台5に取り付けられ、該昇降装置4により縦型攪拌機3自体を昇降装置4で昇降するように構成したが、図5に示すように、攪拌機搭載架台5を昇降装置9に搭載し、該昇降装置9で攪拌機搭載架台5を昇降させることにより、間接的に縦型攪拌機3を昇降するようにしてもよい。   As described above, the vertical stirrer 3 can be moved up and down by the lifting device 4 so that the vertical stirrer 3 can be easily applied to the sedimentation-condensed crystallized product 103 that settles and compacts at the bottom of the crystallization reaction tank 1. Can be restarted. In the above example, the vertical stirrer 3 is attached to the agitator mounting base 5 via the lifting device 4 via the lifting device 4, and the vertical stirring device 3 itself is lifted and lowered by the lifting device 4 by the lifting device 4. As shown in FIG. 5, the vertical agitator 3 may be lifted or lowered indirectly by mounting the stirrer mounting base 5 on the lifting device 9 and lifting the stirrer mounting base 5 by the lifting device 9.

円筒状のバッフル板2の下部2aを晶析反応槽1内側面寄りに傾斜させていることにより、即ちバッフル板2の下端2aをラッパ型に拡径することにより、バッフル板内側の晶析反応部容積を大きくすることができ、バッフル板2の外側を沈降していく晶析物がバッフル板外側に堆積するのを防止できる。   By inclining the lower part 2a of the cylindrical baffle plate 2 toward the inner surface of the crystallization reaction tank 1, that is, by expanding the lower end 2a of the baffle plate 2 into a trumpet shape, the crystallization reaction inside the baffle plate 2 The part volume can be increased, and the crystallized matter that settles outside the baffle plate 2 can be prevented from accumulating on the outside of the baffle plate.

なお、図示は省略するが、晶析物の流動を、縦型攪拌機3による攪拌と、上向水流攪拌又は空気攪拌との併用とすることもできる。これにより縦型攪拌機3が停止した際に、水流又は空気攪拌が継続されるため、晶析物の圧密が軽減される。   In addition, although illustration is abbreviate | omitted, the flow of a crystallized substance can also be made into the combined use of stirring by the vertical stirrer 3 and upward water flow stirring or air stirring. Thereby, when the vertical stirrer 3 is stopped, water flow or air stirring is continued, so that compaction of the crystallized product is reduced.

また、上記例では、縦型攪拌機3は、上下方向に2個の攪拌羽根7−1、7−2を設けた構成としたが、攪拌羽根の個数はこれに限定されるものではなく、下方に1ヶ所又は上下方向に3ヶ所以上設けてもよい。   In the above example, the vertical stirrer 3 has a configuration in which two stirring blades 7-1 and 7-2 are provided in the vertical direction. However, the number of stirring blades is not limited to this, and the lower One or three or more in the vertical direction may be provided.

図1に示す構成の排水の晶析処理装置において、晶析対象成分のCaを含む最終処分場浸出水に、炭酸ナトリウムを加え、炭酸カルシウムの晶析物を析出させ、Caを除去する試験を行った。図6に示すように、昇降装置4がある場合を実施例1(本発明)とし、ない場合を比較例(従来例)としている。その試験条件は図7に示すように、晶析槽(晶析反応槽1)の容量:100L、原水(排水100):最終処分場浸出水、晶析物:炭酸カルシウム、晶析物平均粒径:70μm、晶析物沈降堆積高さ(沈降圧密晶析物103の堆積高さ):120mmである。   In the waste water crystallization treatment apparatus having the configuration shown in FIG. 1, a test is performed in which sodium carbonate is added to the final disposal site leachate containing the crystallization target component Ca to precipitate a crystallized product of calcium carbonate and remove Ca. went. As shown in FIG. 6, the case where the lifting device 4 is provided is referred to as Example 1 (the present invention), and the case where the lifting device 4 is not provided is referred to as a comparative example (conventional example). As shown in FIG. 7, the test conditions are as follows: capacity of crystallization tank (crystallization reaction tank 1): 100 L, raw water (drainage 100): final disposal site leachate, crystallized substance: calcium carbonate, average crystallized grain Diameter: 70 μm, crystallized sediment deposition height (sedimentation compacted crystallized material 103 deposition height): 120 mm.

この条件で運転している縦型攪拌機3を一旦停止し、実施例1(本発明)では図4に示すように、昇降装置4により縦型攪拌機3を上昇させ、攪拌羽根7−2を沈降圧密晶析物103上に位置させ、比較例(従来例)では図3に示すように、沈降圧密晶析物103中に攪拌羽根7−2を位置させている。この状態で縦型攪拌機3を再起動させようとした場合、比較例(従来例)では、過負荷で縦型攪拌機3を再起動できなかった。これに対し、実施例1(本発明)では、縦型攪拌機3を再起動でき、再起動後、縦型攪拌機3を徐々に下げその攪拌羽根7−2を徐々に下げることにより、晶析物が沈降圧密晶析物103の上部から徐々に巻き上がり流動化し、通常の動力で問題なく、最終的に沈降圧密晶析物103全体を流動化させることができた。



The vertical stirrer 3 operating under these conditions is temporarily stopped, and in Example 1 (the present invention), as shown in FIG. 4, the vertical stirrer 3 is lifted by the lifting device 4 and the stirring blade 7-2 is settled. In the comparative example (conventional example), as shown in FIG. 3, the stirring blade 7-2 is positioned in the sedimented consolidated crystallized product 103. When trying to restart the vertical stirrer 3 in this state, in the comparative example (conventional example), the vertical stirrer 3 could not be restarted due to overload. In contrast, in Example 1 (the present invention), a vertical stirring machine 3 can restart after reboot, lowering the vertical agitator 3 progressively by lowering the stirring blade 7-2 gradually, crystallization product There was up fluidized wound gradually from the top of the settling compaction crystallization product 103, no problem in a normal power, the whole finally settled compacted crystallization product 103 could be fluidized.



以上、本発明の実施形態を説明したが、本発明は上記実施形態に限定されるものではなく、特許請求の範囲、及び明細書と図面に記載された技術的思想の範囲内において種々の変形が可能である。なお直接明細書及び図面に記載のない何れの形状・構造・材質であっても、本願発明の作用・効果を奏する以上、本願発明の技術的思想の範囲内である。例えば、昇降装置4は縦型攪拌機3を安定して昇降できる攪拌羽根7−2を上下方向の任意の位置に安定して維持できるものであれば、どのような構成のものでも良い。また、昇降装置9も攪拌機搭載架台5を安定して昇降させ、縦型攪拌機3の攪拌羽根7−2を上下方向の任意の位置に安定して維持できるものであれば、どのような構成のものでも良い。   Although the embodiments of the present invention have been described above, the present invention is not limited to the above-described embodiments, and various modifications can be made within the scope of the technical idea described in the claims and the specification and drawings. Is possible. It should be noted that any shape, structure, and material not directly described in the specification and drawings are within the scope of the technical idea of the present invention as long as the effects and advantages of the present invention are exhibited. For example, the lifting device 4 may have any configuration as long as it can stably maintain the stirring blade 7-2 that can lift and lower the vertical stirrer 3 at an arbitrary position in the vertical direction. Further, the lifting device 9 can also lift and lower the stirrer mounting base 5 stably so that the stirring blade 7-2 of the vertical stirrer 3 can be stably maintained at an arbitrary position in the vertical direction. Things can be used.

本発明に係る排水の晶析処理装置の構成例を示す図である。It is a figure which shows the structural example of the crystallization processing apparatus of the waste_water | drain based on this invention. 本発明に係る排水の晶析処理装置の攪拌羽根の構成例を示す図である。It is a figure which shows the structural example of the stirring blade of the crystallization processing apparatus of the waste_water | drain based on this invention. 本発明に係る排水の晶析処理装置の攪拌機の攪拌羽根が沈降圧密晶析物中に位置する状態を示す図である。It is a figure which shows the state in which the stirring blade of the stirrer of the crystallization processing apparatus of the waste_water | drain which concerns on this invention is located in a sedimentation compacted crystallized substance. 本発明に係る排水の晶析処理装置の攪拌機の攪拌羽根を沈降圧密晶析物上に位置させた状態を示す図である(縦型攪拌機のみを吊り上げる構成)。It is a figure which shows the state which has located the stirring blade of the stirrer of the crystallization processing apparatus of the waste_water | drain which concerns on this invention on a sedimentation compacted crystallized substance (structure which lifts only a vertical stirrer). 本発明に係る排水の晶析処理装置の攪拌機の攪拌羽根を沈降圧密晶析物上に位置させた状態を示す図である(縦型攪拌機と攪拌機搭載架台の両方を上げる構成)。It is a figure which shows the state which has located the stirring blade of the stirrer of the crystallization processing apparatus of the waste_water | drain which concerns on this invention on a sedimentation compacted crystallization thing (structure which raises both a vertical stirrer and a stirrer mounting stand). 本発明に係る排水の晶析処理装置の攪拌機再起動の試験結果を示す図である。It is a figure which shows the test result of the stirrer restart of the waste water crystallization processing apparatus which concerns on this invention. 本発明に係る排水の晶析処理装置の攪拌機再起動の試験条件を示す図である。It is a figure which shows the test conditions of the stirrer restart of the crystallization processing apparatus of the waste_water | drain based on this invention.

符号の説明Explanation of symbols

1 晶析反応槽
2 バッフル板
3 縦型攪拌機
4 昇降装置
5 攪拌機搭載架台
6 回転軸
7−1 攪拌羽根
7−2 攪拌羽根
8 駆動機
9 昇降装置
10 ガイド部材
11 排水流入管
12 薬品供給管
13 流動晶析物排出管
14 処理水流出管
DESCRIPTION OF SYMBOLS 1 Crystallization reaction tank 2 Baffle plate 3 Vertical stirrer 4 Lifting device 5 Stirrer mounting base 6 Rotating shaft 7-1 Stirring blade 7-2 Stirring blade 8 Drive unit 9 Lifting device 10 Guide member 11 Drain inflow pipe 12 Chemical supply pipe 13 Fluidized crystal discharge pipe 14 Treated water outflow pipe

Claims (6)

晶析対象成分を含む排水を収容する晶析反応槽と、該晶析反応槽内の排水を攪拌する攪拌機と、該攪拌機を搭載し支持する攪拌機搭載架台を備えた排水の晶析処理装置において、
前記晶析反応槽内の内側側面に沿って筒状のバッフル板を設け、前記バッフル板内を貫通して前記攪拌機の回転軸を配置し、
前記攪拌機を昇降する昇降装置を設けたことを特徴とする排水の晶析処理装置。
In a crystallization reaction tank containing a crystallization reaction tank containing waste water containing a crystallization target component, a stirrer that stirs the waste water in the crystallization reaction tank, and a stirrer mount that supports and supports the stirrer ,
A cylindrical baffle plate is provided along the inner side surface in the crystallization reaction tank, and the rotating shaft of the stirrer is disposed through the baffle plate.
A waste water crystallization treatment apparatus comprising a lifting device for lifting and lowering the agitator.
請求項1に記載の排水の晶析処理装置において、
前記昇降装置は前記攪拌機搭載架台に設置され、前記攪拌機自体を昇降できるようになっていることを特徴とする排水の晶析処理装置。
In the wastewater crystallization treatment apparatus according to claim 1,
The drainage crystallization treatment apparatus is characterized in that the lifting device is installed on the stirrer mounting base and is capable of lifting and lowering the stirrer itself.
請求項1に記載の排水の晶析処理装置において、
前記攪拌機搭載架台は前記昇降装置に設置され、該攪拌機搭載架台を昇降することにより、前記攪拌機を昇降するようになっていることを特徴とする排水の晶析処理装置。
In the wastewater crystallization treatment apparatus according to claim 1,
The waste water crystallization treatment apparatus, wherein the stirrer mount is installed in the lifting device, and the stirrer is lifted by moving the stirrer mount.
請求項1乃至3のいずれか1項に記載の排水の晶析処理装置において、
前記バッフル板の下部が前記晶析反応槽内側面寄りに傾斜していることを特徴とする排水の晶析処理装置。
In the wastewater crystallization treatment apparatus according to any one of claims 1 to 3 ,
A waste water crystallization treatment apparatus, wherein a lower portion of the baffle plate is inclined toward the inner surface of the crystallization reaction tank.
請求項1乃至4のいずれか1項に記載の排水の晶析処理装置において、
晶析物の流動を、前記攪拌機による攪拌と、上向水流攪拌又は空気攪拌の併用としたことを特徴とする排水の晶析処理装置。
In the wastewater crystallization treatment apparatus according to any one of claims 1 to 4 ,
A waste water crystallization treatment apparatus characterized in that the flow of the crystallized product is a combination of stirring by the stirrer and upward water flow stirring or air stirring.
請求項1乃至5のいずれか1項に記載の排水の晶析処理装置において、
前記晶析反応槽の下部に晶析物を排出する排出管を設けたことを特徴とする排水の晶析処理装置。
In the wastewater crystallization treatment apparatus according to any one of claims 1 to 5 ,
A waste water crystallization treatment apparatus comprising a discharge pipe for discharging a crystallized product at a lower portion of the crystallization reaction tank.
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Families Citing this family (6)

* Cited by examiner, † Cited by third party
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JP6520464B2 (en) * 2015-06-26 2019-05-29 セイコーエプソン株式会社 Liquid container
CN108014737B (en) * 2017-11-20 2024-01-30 浙江长江搅拌设备有限公司 Variable flow reactor
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Family Cites Families (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3494139A (en) * 1967-01-23 1970-02-10 Virtis Co Inc Freeze concentrator
DE3660343D1 (en) * 1985-03-25 1988-08-04 Duphar Int Res Device for concentrating solutions
JP2813674B2 (en) * 1990-09-01 1998-10-22 エム・テクニック株式会社 Stirrer and fluid stirring method

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