JP2008194553A - Treatment agent and method for sewage generated by removal of floor wax - Google Patents

Treatment agent and method for sewage generated by removal of floor wax Download PDF

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JP2008194553A
JP2008194553A JP2007029242A JP2007029242A JP2008194553A JP 2008194553 A JP2008194553 A JP 2008194553A JP 2007029242 A JP2007029242 A JP 2007029242A JP 2007029242 A JP2007029242 A JP 2007029242A JP 2008194553 A JP2008194553 A JP 2008194553A
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sewage
floor wax
aqueous solution
present
floor
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Yasushi Jo
靖 城
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Fuji-Mentenir Co Ltd
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Fuji-Mentenir Co Ltd
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Abstract

<P>PROBLEM TO BE SOLVED: To enable simple and quick treatment of sewage generated by removal of floor wax. <P>SOLUTION: A treatment agent for the sewage generated by removal of floor wax contains an acid sulfate that actions on the sewage to separate solids dissolved in it. Its treatment method enables the sewage generated by removal of floor wax to be poured into an aqueous solution containing the acid sulfate, which separates the dissolved solids from the sewage. <P>COPYRIGHT: (C)2008,JPO&INPIT

Description

本発明は、建物の床に施工されている床面のワックスを剥離し、再びワックスを塗布して床面を美化再生する工程で、剥離した汚水に含まれるワックス成分を含む溶解物を分離して固める方法とその処理剤に関する。   The present invention is a process of peeling off the wax on the floor surface applied to the floor of the building, reapplying the wax again to beautify and regenerate the floor surface, and separating the melt containing the wax component contained in the separated sewage. It relates to the method of hardening and the treatment agent.

従来汚水処理には、高分子の凝縮剤が専ら工場廃水の処置などに使われており、床面ワックスの剥離汚水の処理にもこれに類似した処理剤が試用されている。これらの方法は、凝集剤を投与してから溶解している固形物が固まるまでに長時間を要し、しかも凝縮物が粘着性を有するなど、ろ過する時に目詰まりをおこし易いなどの欠点があり、ビルディングのメンテナンスで行う剥離作業のような敏速な作業を要求される場合、実用的に大きい問題点が存在する。   Conventionally, a polymer condensing agent has been used exclusively for the treatment of factory wastewater in sewage treatment, and a similar treatment agent has been used for the treatment of floor wax peeling sewage. These methods have a drawback that it takes a long time to solidify the dissolved solid after administration of the flocculant, and the condensate is sticky, which causes clogging easily during filtration. Yes, there is a large practical problem when a quick work such as a peeling work for building maintenance is required.

汚れた床面のワックスを剥離剤で剥離した汚水は、これまで排水で水と共に流して処理されてきた。 近年公害問題が惹起され、汚水の処理は緊急の課題になっている。工場廃水のような大規模でなく、個々の現場ではぺール缶と呼ばれる筒型の容器に回収されるのが常法で、これを排水口に流している現状はこれまであまり注目されていなかった。しかし環境保全の観点から世論は緊急に汚水の垂れ流しの禁止にも動いており、その解決は緊急の課題である。   The sewage from which the wax on the dirty floor has been removed with a release agent has been treated by draining it together with water. In recent years, pollution problems have been raised and sewage treatment has become an urgent issue. It is not a large scale like factory wastewater, but it is usually collected in a cylindrical container called a pail can at each site, and the current situation of flowing this to the drain outlet has not received much attention so far It was. However, from the viewpoint of environmental conservation, public opinion is moving urgently to ban sewage drainage, and its solution is an urgent issue.

ビルディングのメンテナンスにおいて、床面ワックスの剥離汚水処理を実用的レベルで普及させるためには、
1.床面ワックスの剥離汚水が、一般的にはペール缶と呼ばれる18〜20リットル程度の容量がある筒型の容器に集められるため、この単位で処理できることが最も好ましい。
2.作業者は時間に追われて作業しているため、汚水処理は敏速に出来ることが必要であり、凝固が瞬時に起こることが実用上不可欠である。
3.ペール缶に生じた沈澱物の状態が、次の工程すなわち沈澱物の分離に適した性状であることが必要である。すなわち、凝縮物に粘着性がないこと、ろ過などの分離作業に際し、ろ過材の目詰まりを生じないこと、そして濾過速度が速いこと。
4.濾過された固形物の性状が、取り扱いやすいものであること。
などが必要となる。
In building maintenance, in order to disseminate floor wax peeling sewage treatment at a practical level,
1. Since the floor wax peeling wastewater is generally collected in a cylindrical container having a capacity of about 18 to 20 liters called a pail can, it is most preferable that it can be treated in this unit.
2. Since workers are working in time, it is necessary to treat sewage quickly and it is practically essential that solidification occurs instantaneously.
3. It is necessary that the state of the precipitate generated in the pail can be suitable for the next step, that is, separation of the precipitate. That is, the condensate is not sticky, the filter medium is not clogged during separation work such as filtration, and the filtration speed is high.
4). The filtered solid must be easy to handle.
Etc. are required.

通常、高分子凝固剤で汚水を処理する場合、かなり長時間、例えば20分以上放置沈殿させるのが普通であり、これらを除去するろ過工程にも30分以上の時間が掛かることが多い。これらを短時間で行えるかどうかが実用化の成否を決すると言われている。しかしこれらの要求にこたえる手段も、凝固剤も知られていないのが現状である。   Usually, when treating sewage with a polymer coagulant, it is usually left and settled for a considerably long time, for example, 20 minutes or more, and the filtration step for removing these often takes 30 minutes or more. It is said that whether these can be done in a short time will determine the success or failure of practical application. However, at present, neither a means for meeting these requirements nor a coagulant is known.

本発明の第1の効果は、本発明の処理剤を含む水溶液と剥離汚水とを接触させることにより、ただちに凝固がスタートすることである。   The first effect of the present invention is that coagulation starts immediately by bringing the aqueous solution containing the treatment agent of the present invention into contact with the stripped waste water.

本発明の第2の効果は、凝固が沈殿するというよりは、固まるように汚水系から分離する様態を示すところにあり、次第に1つの固形の塊に発展し、固形物と透明な液層に速やかに分離する。   The second effect of the present invention is that the solidification is separated from the sewage system so that it solidifies, rather than solidifying, and gradually develops into one solid lump, resulting in solids and a transparent liquid layer. Separate immediately.

本発明の第3の効果は、固形物の性状が極めて分離しやすいことである。これまで知られている通常の凝固剤による分離固形物に見られるような、沈澱物に粘着性もなく、濾過布や濾紙による濾過作業も必要とせず、金網などできれいに分離することが出来るのである。本発明によって、これまで実用化を妨げていた作業性の問題は解決された。   The third effect of the present invention is that the properties of solids are very easy to separate. Since the precipitates are not sticky, as is the case with conventional solids separated by conventional coagulants, they do not require filtration with a filter cloth or paper, and can be separated neatly with a wire mesh. is there. According to the present invention, the problem of workability that has been impeded until practical use has been solved.

本発明による床面ワックスの剥離汚水の処理剤は、床面ワックスを剥離して得られる剥離汚水に作用して、該剥離汚水に溶解している固形物を分離することを特徴とする酸性硫酸塩を含んでいる。   The treatment agent for floor wax peeling sewage according to the present invention acts on the peeling sewage obtained by peeling off the floor wax to separate the solid matter dissolved in the peeling sewage. Contains salt.

また、本発明による処理方法は、酸性硫酸塩を含む水溶液に床面ワックスを剥離した剥離汚水を注ぎ込むことによって床面ワックスの剥離汚水から、溶解している固形物を分離することを特徴とする。   Further, the treatment method according to the present invention is characterized in that the dissolved solid matter is separated from the stripped waste water of the floor wax by pouring the stripped waste water from which the floor wax has been stripped into an aqueous solution containing acidic sulfate. .

さらに、本発明による処理方法は、床面ワックスを剥離した剥離汚水を、酸性硫酸塩及び酸性硫酸塩を含む水溶液で処理し、溶解している固形物を分離した液体部分を、炭酸塩で中和し、発泡現象の消滅を中和完了の指標とする。   Further, in the treatment method according to the present invention, the stripped sewage from which the floor wax has been peeled is treated with an aqueous solution containing acidic sulfate and acidic sulfate, and the liquid portion from which the dissolved solid matter is separated is mixed with carbonate. The disappearance of the foaming phenomenon is used as an indicator of completion of neutralization.

本発明によって、これまで野放しになっていた床面ワックスの剥離汚水を実用的なレベルで簡単かつ敏速に、そして省力的に容易に行うことができ、作業性はもちろん環境保全の面からも画期的な効果を示し、重要な発明である。   According to the present invention, it is possible to easily and quickly remove floor wax peeling sewage, which has been left open until now, at a practical level, easily and labor-saving. This is an important invention that shows long-term effects.

以下に本発明の特徴を列挙する。   The features of the present invention are listed below.

本発明の特徴のひとつは、汚水の凝固に高分子凝固剤のような有機化合物は一切使用せず無機化合物のみによる事である。さらに本発明の特徴のひとつは、無機化合物に酸性硫酸塩、例えば重硫酸ナトリウム(硫酸水素ナトリウム、酸性硫酸ナトリウムということもある)、重硫酸アンモニウム、重硫酸カリウムからなる群から選ばれる少なくとも1つを含む水溶液を凝固液に使用することにある。   One of the features of the present invention is that no organic compound such as a polymer coagulant is used for coagulating wastewater, and only an inorganic compound is used. Further, one of the characteristics of the present invention is that the inorganic compound contains at least one selected from the group consisting of acidic sulfates such as sodium bisulfate (sometimes referred to as sodium hydrogensulfate and acidic sodium sulfate), ammonium bisulfate, and potassium bisulfate. It is to use an aqueous solution containing the coagulation liquid.

また上記溶液に、塩析効果を出すために、塩化ナトリウム、硫酸ナトリウム、塩化カルシュムなどの無機塩を加えることも出来る。   In addition, an inorganic salt such as sodium chloride, sodium sulfate, or calcium chloride can be added to the above solution in order to produce a salting out effect.

さらに本発明の特徴のひとつは、上記酸性硫酸塩の水溶液を攪拌しながら、少量ずつ加えるのでなく、使用量を一度に加えるところにある。使用量は数回に分けてくわえても良いが、一時に加えるのが最もよい。撹拌しながら小量ずつ滴下することは、避けなければならない。一度に注ぎ込むると、凝固物が団子状となり、濾過の工程を省いて凝固体を、例えば手で取り除くことも出来るし、凝固系を金網に注いで簡単に取り除く事も出来る。   Further, one of the characteristics of the present invention is that the amount of the acid sulfate is added at a time instead of being added little by little with stirring. The amount used may be divided into several times, but it is best to add it at a time. It should be avoided to add a small amount while stirring. When poured at once, the coagulated material becomes dumpling, and the solidified body can be removed by hand, for example, by omitting the filtration process, or it can be easily removed by pouring the coagulation system into a wire mesh.

なぜ床面ワックスの剥離汚水に、酸性硫酸塩水溶液を加えると溶解している樹脂ワックスを含む固形物が分離して団子状に塊るのかについては、その理由は明らかではない。文献にもこのような記述は見られない。この現象は、本発明者が、剥離汚水の処理をいろいろ検討している時に偶然実験的に見出したものである。   The reason why the solid matter containing the dissolved resin wax separates into a dumpling form when an acidic sulfate aqueous solution is added to the floor wax peeling sewage is not clear. There is no such description in the literature. This phenomenon has been found experimentally by chance when the present inventor is considering various treatments for stripped wastewater.

本発明の凝固作業において、本発明の酸性硫酸イオンを含む水溶液の加え方も重要である。もっとも効果的な方法は、常識とは異なり、まず本発明の酸性硫酸イオンを含む水溶液の上から、剥離汚水を注ぎ込む方法が最も優れている。凝固は底部から生じ、汚水の注入で自然に系が攪拌されるので、従来必要とされている撹拌工程が省略できるのである。凝固は底部から生じて徐々の上部に進行し団子状に固まるのでその除去は簡単である。   In the coagulation work of the present invention, it is also important to add the aqueous solution containing the acidic sulfate ion of the present invention. The most effective method is different from common sense, and the method in which the peeled sewage is poured first from the aqueous solution containing the acidic sulfate ion of the present invention is the best. Solidification occurs from the bottom, and the system is naturally agitated by the injection of sewage, so that the agitation step conventionally required can be omitted. Solidification occurs from the bottom, gradually progresses to the top and hardens in a dumpling form, so removal is easy.

もちろんペール缶にまず剥離汚水を入れ、その上から上記酸性硫酸イオンを含む水溶液を一度に注ぐ方法も用いられるが、この場合撹拌効果が得られないので、次の工程が必要になる。すなわち穏やかに撹拌をしないと凝固に時間がかかることになる。この場合激しく攪拌すると沈澱物が細かくなり、濾過に長時間を要し好ましくない。この場合も、一気に注ぎ込むと、攪拌しながら凝固液を滴下する方法よりも沈殿物が団子状の大きい塊となり易く、次工程の分離、ろ過に有利となる。   Of course, a method in which exfoliated sewage is first put in a pail can and an aqueous solution containing the acidic sulfate ion is poured at once is used. However, in this case, the stirring effect cannot be obtained, so the next step is necessary. In other words, it takes time to coagulate unless it is gently stirred. In this case, if the mixture is vigorously stirred, the precipitate becomes fine, and it takes a long time for filtration, which is not preferable. In this case as well, when poured all at once, the precipitate tends to be a large dumpling-like lump than the method of dropping the coagulation liquid while stirring, which is advantageous for separation and filtration in the next step.

本発明を実施するに際し、通常行われているような汚水を攪拌しながら少量ずつ加える方法は好ましくなくむしろ避けるべきである。攪拌しながら凝固剤を滴下するのは、常識化しているが、本発明の実施にはふさわしくない。本発明の実施において、攪拌しながら凝固剤を滴下すると、沈澱物が細かくなって、ろ過に目埋りを生じてろ過に長時間を要し、実用化の面で致命的な欠陥となる。   In practicing the present invention, the method of adding sewage in small portions while stirring, as is usually done, is not preferred and should be avoided. Although it is common sense to add the coagulant while stirring, it is not suitable for the practice of the present invention. In the practice of the present invention, if the coagulant is added dropwise with stirring, the precipitates become finer, resulting in clogging of the filtration and a long time for the filtration, which becomes a fatal defect in practical use.

さらに本発明の特徴のひとつは、沈澱物を含む、あるいは分離した後の残液の処理方法にある。床面剥離汚水は、剥離剤の影響でアルカリ性である。本発明の方法で汚水を処理した後の残液は酸性になっている。このままで廃棄することは出来ないので、これを中性にまで中和する必要がある。通常液を攪拌しながら、液状あるいは粉末状の中和剤を滴下しつつ、インジケーター(指示薬)の色の変化で中和を確認する方法が用いられているが、実際の作業現場でこの作業は大変な労苦を伴うものである。本発明では、これらの作業を合理化して、インジケーターを用いずに中和の確認を得る方法を発見した。   Furthermore, one of the characteristics of the present invention is a method for treating a residual liquid containing a precipitate or after separation. The floor peeling sewage is alkaline due to the influence of the peeling agent. The residual liquid after treating sewage with the method of the present invention is acidic. Since it cannot be discarded as it is, it must be neutralized to neutrality. Usually, a method of confirming neutralization by changing the color of an indicator (indicator) while stirring a liquid or dropping a liquid or powder neutralizer is used. It is very laborious. In the present invention, a method has been found that rationalizes these operations and obtains confirmation of neutralization without using an indicator.

本発明を実施するに際し、剥離汚水から溶解固形物を除いた残液に粉末状または水に溶かした炭酸塩、重炭酸塩を少量ずつ加えると炭酸ガスが発生しながら中和が行われる。上記炭酸塩、重炭酸塩を加えたときに、ガスの発生がみられなくなると中和が完成したことを示す。本方法が何より優れているのは、通常、中和剤を加えすぎるとアルカリ性の側に行過ぎて、また酸を加えて調整する必要が生じ、これらの繰り返しでて作業者は混乱を極める問題点を解決したことである。   When practicing the present invention, neutralization is performed while carbon dioxide gas is generated when carbonate or bicarbonate dissolved in powder or water is added little by little to the residual liquid obtained by removing dissolved solids from exfoliated wastewater. If the generation of gas is not observed when the above carbonates and bicarbonates are added, the neutralization is completed. What is superior to this method is that if the neutralizer is added too much, it goes too far to the alkaline side, and it is necessary to adjust it by adding acid. This is a solution to the problem.

本発明の方法によれば、上記炭酸塩等を加え過ぎても問題はない。なぜなら、系は緩衝溶液となっており、上記炭酸塩等を加え過ぎてもpHに影響しないから中和の状態に保たれるのである。これは実際の作業上きわめて重要な事柄であり、本発明を実施するに当たり重要な位置を占めるものである。   According to the method of the present invention, there is no problem even if the carbonate or the like is added excessively. This is because the system is a buffer solution, and even if the carbonate or the like is added excessively, the pH is not affected, so that the neutralized state is maintained. This is an extremely important matter in actual work, and occupies an important position in carrying out the present invention.

本発明の中和剤としての炭酸塩、重炭酸塩の例としては、炭酸ソーダ、炭酸カリ、重炭酸ソーダ(炭酸水素ナトリウム)、重炭酸カリなどがある。とくに有用なのは重炭酸ソーダがある。これは中和が緩慢に進み作業性が優れていて実際の作業を効率よく安全に行うことが出来る。本中和作業を行うに際し、上記炭酸塩等は、水にとかしてくわえても良いが、もっとも優れた方法は粉末状で加える方法である。作業が簡単であるだけでなく、中和の完成を見るのに、添加したところのガスの発生が確認しやすい点が重要である。   Examples of carbonates and bicarbonates as neutralizing agents of the present invention include sodium carbonate, potassium carbonate, sodium bicarbonate (sodium bicarbonate), potassium bicarbonate and the like. Particularly useful is sodium bicarbonate. This is because the neutralization proceeds slowly and the workability is excellent, and the actual work can be performed efficiently and safely. In carrying out the neutralization operation, the carbonates and the like may be dissolved in water, but the most excellent method is a method of adding them in powder form. It is important not only that the work is simple, but also that it is easy to confirm the generation of the added gas in order to see the completion of neutralization.

本発明を実施するに際し用いられる酸性硫酸塩の量(gr::W)は、処理汚水の容量(m:V)に対してW/V比で1/300〜1/10の範囲であることが好ましく、更に好ましくは、1/200〜1/20ある。この比が1/300より小さければ凝固が不十分になることがあり、1/10より大きいと過剰分が無駄となりかえって環境汚染になる可能性がある。   The amount of acid sulfate (gr :: W) used in carrying out the present invention is in the range of 1/300 to 1/10 in terms of W / V ratio with respect to the capacity (m: V) of treated wastewater. Is more preferable, and more preferably 1/200 to 1/20. If this ratio is less than 1/300, solidification may be insufficient, and if it is more than 1/10, the excess may be wasted and may cause environmental pollution.

本発明は、上述したように、床面を剥離した剥離汚水を極めて簡単な操作で、溶解固形物を分離除去することに成功したもので、環境汚染を防ぐ有力な手段を提供するものである。   As described above, the present invention has succeeded in separating and removing the dissolved solids from the separated sewage from which the floor surface has been peeled off by an extremely simple operation, and provides an effective means for preventing environmental pollution. .

本発明を以下の実施例によってさらに詳しく説明する。   The invention is further illustrated by the following examples.

樹脂ワックスを塗布して半年を経ている汚れた床面を市販の剥離剤溶液で剥離を行い、その汚水の2リットルをテスト汚水とした。酸性硫酸塩として酸性硫酸ナトリウム10グラムを用い、これを300ミリリットルの水に溶解して容器に加えた。その上に2リットルの前記汚水を一気に注ぎ込んだ。瞬時に塊状の沈澱物が生じ、汚濁液は透明な液となった。5分後塊は、簡単に拾いあげ金網に乗せられた。この塊は手で押さえつけると若干の透明な液が絞り出された。液は酸性であった。これに重炭酸ソーダの粉末を加えると細かい泡がでる。緩やかに攪拌しながら重炭酸ソーダの粉末を加え続けるとやがて泡は出なくなった。リトマス試験紙でpHを調べるとpHは7であり、中和がされていることが示された。さらに若干の重炭酸ソーダの粉末をさらに加えてpHを調べるとpHは7で変わりはなかった。   A resin floor was applied and the dirty floor surface that had been half a year old was peeled off with a commercially available release agent solution, and 2 liters of the waste water was used as test waste water. 10 grams of acidic sodium sulfate was used as the acidic sulfate, which was dissolved in 300 milliliters of water and added to the container. On top of that, 2 liters of the sewage was poured all at once. A massive precipitate was instantly formed, and the turbid liquid became a transparent liquid. After 5 minutes, the lump was easily picked up and placed on a wire mesh. When this lump was pressed by hand, some clear liquid was squeezed out. The liquid was acidic. When sodium bicarbonate powder is added to this, fine bubbles appear. When the sodium bicarbonate powder was continuously added with gentle stirring, the bubbles eventually disappeared. When the pH was examined with a litmus paper, the pH was 7, indicating that it was neutralized. Further, when a pH of the sodium bicarbonate powder was further investigated by adding a little powder of sodium bicarbonate, the pH was 7 and was not changed.

酸性硫酸塩として酸性硫酸ナトリウムの代わりに酸性硫酸カリウム20グラムを用いた以外は、実施例1と同じである。本実施例でも同様に剥離汚水を上記酸性水溶液に一気に加えると瞬時に塊状の沈澱物が生じ、汚濁液は透明な液となった。   The same as Example 1 except that 20 grams of acidic potassium sulfate was used as the acidic sulfate instead of acidic sodium sulfate. Also in this example, when exfoliated wastewater was added to the acidic aqueous solution at once, a massive precipitate was instantly formed, and the contaminated liquid became a transparent liquid.

実施例1と同様に重炭酸ソーダの粉末を穏やかに攪拌しながら泡の発生がなくなるまでくわえてpHをリトマス試験紙で調べるとpHは7であった。   In the same manner as in Example 1, the pH of the sodium bicarbonate powder was 7 when the pH was examined with a litmus paper while adding the foam until the generation of bubbles was stopped while gently stirring.

本例では、テスト汚水、酸性硫酸塩とも実施例1と同じものを用いたが、酸性硫酸ナトリウム水溶液の上から剥離汚水液を注ぐのではなく、逆に剥離汚水液の上から酸性硫酸ナトリウム水溶液を一気に注いだ。汚水の上部から瞬時に凝固が進み、塊状の沈澱が生じ時間と共に塊の凝固物が下方に及んでゆくことが観察された。この場合、系の攪拌がなされないので凝固に若干の時間を要し、穏やかに攪拌すると凝固が早くなった。固まった塊状の固形物以外の部分は、透明な液体であった。   In this example, the same test sewage and acidic sulfate as in Example 1 were used, but instead of pouring the peeling sewage liquid from above the acidic sodium sulfate aqueous solution, the acidic sodium sulfate aqueous solution from above the peeling sewage liquid. Was poured all at once. It was observed that coagulation progressed instantaneously from the upper part of the sewage, a massive precipitate formed, and the coagulated mass of the mass extended downward with time. In this case, since the system was not stirred, it took some time for solidification, and solidification was accelerated when gently stirred. The part other than the solid lump solid was a transparent liquid.

(参考例1)
用いた剥離汚水と酸性硫酸ナトリウム水溶液は、実施例1と同じものを用いたが、両者の混ぜ合わし方が異なっている。本参考例では、常識的な一般の方法、すなわち剥離汚水の溶 液を攪拌しながら、凝固液である酸性硫酸ナトリウム水溶液を徐々に滴下した。滴下と同時に沈澱は見られるがその形態は、柔らかいフレーク状若しくは細かい粉状で粘着性があり、ひとつに固まらず、取り除くためにろ過が必要であった。しかも、ろ過の間に濾布の目詰まりをおこし、ろ過に長時間を要した。ろ過した部分は、粘着性を有し取り扱いがきわめて難しかった。
(Reference Example 1)
The same peeling sewage and acidic sodium sulfate aqueous solution as used in Example 1 were used, but the way of mixing them was different. In this reference example, an acidic sodium sulfate aqueous solution, which is a coagulation solution, was gradually added dropwise while stirring a common-sense general method, that is, a solution of exfoliated wastewater. Although precipitation was observed at the same time as dropping, the form was soft flaky or fine powdery and sticky, it did not harden into one, and filtration was necessary to remove it. Moreover, the filter cloth was clogged during the filtration, and the filtration took a long time. The filtered part was sticky and very difficult to handle.

Claims (3)

床面ワックスを剥離して得られる剥離汚水に作用して、該剥離汚水に溶解している固形物を分離することを特徴とする酸性硫酸塩を含む床面ワックスの剥離汚水の処理剤。   A treating agent for exfoliated wastewater of floor wax containing acidic sulfate, which acts on exfoliated wastewater obtained by exfoliating floor wax and separates solids dissolved in the exfoliated wastewater. 酸性硫酸塩を含む水溶液の上から、床面ワックスを剥離した剥離汚水を注ぎ込むか又は剥離汚水の上から前記酸性硫酸塩を含む水溶液を一気に、あるいは数回に分割して注ぎ込むことによって床面ワックスの剥離汚水から、溶解している固形物を分離することを特徴とする床面ワックスの剥離汚水の処理方法。   The floor wax is poured from above the aqueous solution containing acidic sulfate by pouring the stripped sewage from which the floor wax has been peeled off or by pouring the aqueous solution containing the acidic sulfate from the top of the stripped sewage at once or divided into several times. A method for treating floor wax peeling sewage, comprising separating a dissolved solid from the peeling sewage. 床面ワックスを剥離した剥離汚水を、酸性硫酸塩及び酸性硫酸塩を含む水溶液で処理し、溶解している固形物を分離した液体部分を、炭酸塩で中和し、発泡現象の消滅を中和完了の指標とする床面ワックスの剥離汚水の処理方法。   Treating stripped sewage from which floor wax has been stripped with an aqueous solution containing acidic sulfate and acidic sulfate, and neutralizing the liquid portion from which the dissolved solids have been separated with carbonate to neutralize the foaming phenomenon. A method for treating floor wax peeling sewage as an indicator of sum completion.
JP2007029242A 2007-02-08 2007-02-08 Treatment agent and method for sewage generated by removal of floor wax Pending JP2008194553A (en)

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2008207128A (en) * 2007-02-27 2008-09-11 Gunbiru:Kk Polymer wax peeling waste liquid treatment method

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH1024285A (en) * 1996-07-10 1998-01-27 Shin Etsu Chem Co Ltd Decomposing method of oxalic acid in waste water containing chloride ion
JP2000288554A (en) * 1999-04-12 2000-10-17 Sansai Kako Kk Treatment of spent release solution
JP2005118626A (en) * 2003-10-14 2005-05-12 Japan Organo Co Ltd Method and apparatus for treating oxidizing agent

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH1024285A (en) * 1996-07-10 1998-01-27 Shin Etsu Chem Co Ltd Decomposing method of oxalic acid in waste water containing chloride ion
JP2000288554A (en) * 1999-04-12 2000-10-17 Sansai Kako Kk Treatment of spent release solution
JP2005118626A (en) * 2003-10-14 2005-05-12 Japan Organo Co Ltd Method and apparatus for treating oxidizing agent

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2008207128A (en) * 2007-02-27 2008-09-11 Gunbiru:Kk Polymer wax peeling waste liquid treatment method
JP4614979B2 (en) * 2007-02-27 2011-01-19 株式会社グンビル Polymer wax peeling waste liquid treatment method

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