JP3981674B2 - High load wastewater treatment system - Google Patents

High load wastewater treatment system Download PDF

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JP3981674B2
JP3981674B2 JP2004120826A JP2004120826A JP3981674B2 JP 3981674 B2 JP3981674 B2 JP 3981674B2 JP 2004120826 A JP2004120826 A JP 2004120826A JP 2004120826 A JP2004120826 A JP 2004120826A JP 3981674 B2 JP3981674 B2 JP 3981674B2
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守央 住本
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株式会社住本科学研究所
守央 住本
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有害物質を含み環境負荷の高い所謂高負荷廃水を濃縮処理するための処理システムに関する。   The present invention relates to a treatment system for concentrating so-called high-load wastewater containing harmful substances and having a high environmental load.

例えば、自動車の塗装工程には塗装後に水洗工程が含まれ大量の水が使用される。この工程において使用された水は、BODやCODの値が高く、未処理のままでは廃棄することができない。このため現在のところ廃水のトン当りの単価と処理量から算出される処理料金を処理業者に支払い、廃水をそのまま引き取ってもらうということがなされている。しかし、処理単価が高額であることと廃水量が多量であることから処理料金が非常に高額化してしまうという問題があり大きな負担となっていた。   For example, a painting process of an automobile includes a washing process after painting, and a large amount of water is used. The water used in this step has a high BOD and COD value and cannot be discarded if left untreated. For this reason, currently, a processing fee calculated from a unit price per ton of wastewater and a processing amount is paid to the processing company, and the wastewater is collected as it is. However, the treatment unit price is high and the amount of wastewater is large, so there is a problem that the treatment fee becomes very expensive, which is a heavy burden.

そこで、そのような工業廃水等の高負荷廃水に含まれる水分をある程度除去し、廃水を濃縮して減容することが考えられ、廃水を加熱し蒸発させて濃縮するという所謂蒸発濃縮装置が提案されている。そのような処理対象廃水を蒸発させて濃縮するようにした装置において、この系内の熱を循環させることで熱効率を高め消費エネルギーを低下させるように工夫されたものが多数提案されており、またその中でも特に高効率にして処理対象廃水の処理を行うことができるものとして特開平5−115857号公報に開示された技術が挙げられる。この技術は、処理槽において処理対象廃水を減圧加熱し、蒸発させて減容すると共に蒸発させた水分を凝縮させる過程において、処理対象水を加熱するための加熱前の熱媒体との間で熱交換させてこれに予熱を与えて熱効率を向上させつつ、凝縮させた水分を再利用できるように構成されるものである。この装置によれば、処理対象廃水を比較的低温での加熱で蒸発させることができるため、高い熱効率や処理効率にして廃水の濃縮処理ができると共に、蒸発水分を凝縮させた凝縮水を洗浄水等として再利用することができる。しかし、それらのような従来の処理装置の技術には加熱部に関する技術事項が開示されておらず、一般的に知られた熱交換器等の加熱器を採用した上述の如くの装置によって、BOD、COD、nヘキサン抽出物質、ph、ss等が高い値を示す所謂高負荷性廃水を処理しようとする場合、処理対象廃水の加熱と濃縮によって腐食性が更に強化され、この廃水に接触させて加熱するための熱部分が腐食し易くなり、長期使用に耐えられないという問題があった。又、減圧するためのポンプの腐食対策も必要であった。   Therefore, it is conceivable to remove water contained in high-load wastewater such as industrial wastewater to some extent, and concentrate and reduce the volume of wastewater. So-called evaporative concentration equipment that heats and evaporates the wastewater is proposed. Has been. Many devices designed to evaporate and concentrate such waste water to be treated have been devised to increase heat efficiency and reduce energy consumption by circulating heat in the system, and Among them, a technique disclosed in Japanese Patent Application Laid-Open No. 5-115857 can be cited as one that can treat wastewater to be treated with particularly high efficiency. In this process, wastewater to be treated is heated under reduced pressure in a treatment tank, evaporated and reduced in volume, and condensed water is evaporated between the heat medium before heating to heat the treatment target water. It is configured so that the condensed water can be reused while being exchanged and preheated to improve thermal efficiency. According to this apparatus, since the waste water to be treated can be evaporated by heating at a relatively low temperature, the waste water can be concentrated with high heat efficiency and treatment efficiency, and the condensed water condensed with the evaporated water can be washed. Etc. can be reused. However, the technical matters regarding the heating unit are not disclosed in the technology of the conventional processing apparatus such as those, and the BOD can be obtained by the apparatus as described above employing a heater such as a generally known heat exchanger. , COD, n-hexane extract material, ph, ss, etc., when so-called high-load wastewater is to be treated, the corrosiveness is further enhanced by heating and concentration of the wastewater to be treated. There was a problem that the hot part for heating was easily corroded and could not withstand long-term use. In addition, it was necessary to take countermeasures against corrosion of the pump to reduce the pressure.

また、耐食性に優れた熱交換器としては、特開平10−81930号公報に開示された技術がある。これは、耐食性に優れた合金によって形成された加熱部を採用することによって、熱伝導性に優れた比較的耐食性のある熱交換器を得ることができるというものである。しかし、このような熱交換器を上述の如くの高負荷廃水の処理を行うための蒸発濃縮装置の加熱機構として採用した場合、処理対象廃水の種類によっては合金でできた加熱部の溶出が避けられず、処理対象廃水中に金属イオン等を生成してしまい二次処理を必要とするという問題や加熱部の劣化や損傷が激しく、度重なるメンテナンスが必要となり、その間の処理の停止やメンテナンス費用がかかってしまう等の問題が生じていた。また、そのような処理方法或いは装置の場合、ランニングコストが高額であり、処理後に更に濃縮した廃水を処理業者に引き取ってもらうと、トータルの処理費用が高額化して見合わないという問題があった。
特開平5−115857号公報 特開平10−81930号公報
Moreover, as a heat exchanger excellent in corrosion resistance, there is a technique disclosed in JP-A-10-81930. By adopting a heating part formed of an alloy having excellent corrosion resistance, a heat exchanger having relatively high corrosion resistance and excellent thermal conductivity can be obtained. However, when such a heat exchanger is used as a heating mechanism of an evaporating and concentrating apparatus for treating high-load wastewater as described above, elution of a heating part made of an alloy is avoided depending on the type of wastewater to be treated. The problem is that metal ions are generated in the wastewater to be treated and secondary treatment is required, and the heating part is severely deteriorated and damaged, requiring repeated maintenance. There was a problem that it took a long time. In addition, in the case of such a treatment method or apparatus, there is a problem that the running cost is high, and if the waste water further concentrated after the treatment is collected by the treatment contractor, the total treatment cost becomes high and cannot be paid. .
Japanese Patent Laid-Open No. 5-115857 JP-A-10-81930

この発明は、上記の如くの従来の問題点に鑑みてなされたものであり、高負荷廃水による処理装置の腐食が無く耐久性の極めて高い、廃水の連続処理が高効率且つ低コストで行える高負荷廃水の処理システムを提供せんとするものである。   The present invention has been made in view of the conventional problems as described above, and does not corrode treatment equipment due to high-load wastewater, has extremely high durability, and enables high-efficiency and low-cost continuous treatment of wastewater. It is intended to provide a wastewater treatment system.

上記課題を解決するために本発明が採った手段は、廃水処理槽と、この槽内に未処理の処理対象廃水を投入するための流入路と流入量調整機能とを備えた投入手段と、少なくともその一部が前記槽内に収容された前記廃水に接触するように配置され任意の高温熱源から得られた蒸気をその内部に通過させるようにしたフッ素樹脂製チューブを結束してなる処理対象廃水を加熱処理するための加熱手段と、該槽内において処理され所定の濃度に濃縮された処理済み廃水を該槽内から取り出すための流出路と流出量調整機能を備えた取出手段と、処理対象廃水を加熱したことによって気化分離された蒸気を捕集し且つ凝縮して分離水を生成するための、降下勾配を以て配置され外面に吸水体を被覆してなる冷却管の内部に前記蒸気を通過させ、下部に適当な間隔で内外に貫通した孔を設けてなる水パイプを前記冷却管の上部に、該冷却管に沿って配置して、該水パイプ内に水を通して前記孔から水が冷却管に滴下されるように構成してなる分離水生成手段と、を備え、廃水処理槽内において、該槽内に収容された処理対象廃水を前記加熱手段によって加熱気化させ、該槽内に収容された前記廃水の水分量を減量して濃縮し、前記廃水を気化して分離した蒸気を前記分離水生成手段によって捕集し且つ凝縮させて分離水を抽出し、前記廃水が所定の濃度になるように前記投入手段と取出手段の調整を行って、投入速度と取出速度を所定の量に調整し、連続的に処理することができるようにしたことを特徴とする。


Means that the invention is taken in order to solve the above problems, a waste water treatment tank, a dosing means provided with inflow path and the inflow amount adjusting function for inputting processed wastewater unprocessed this tank , A process comprising bundling a fluororesin tube that is arranged so that at least a part thereof is in contact with the wastewater contained in the tank and allows vapor obtained from an arbitrary high-temperature heat source to pass therethrough A heating means for heat-treating the target wastewater; an outflow path for taking out the treated wastewater that has been treated in the tank and concentrated to a predetermined concentration; and an extraction means having an outflow amount adjusting function; Steam that is vaporized and separated by heating the wastewater to be treated is collected and condensed to produce separated water, and the steam is disposed inside a cooling pipe that is arranged with a descending gradient and that has an outer surface covered with a water absorbent. Pass through and below A water pipe having holes penetrating inside and outside at an appropriate interval is disposed along the cooling pipe at the top of the cooling pipe, and water is dropped into the cooling pipe through the water through the water pipe. A separation water generating means configured as described above, and in the wastewater treatment tank, the waste water to be treated contained in the tank is heated and vaporized by the heating means, and the wastewater treatment tank accommodated in the tank The water content of the waste water is reduced and concentrated, and the vapor separated by vaporizing the waste water is collected and condensed by the separated water generating means to extract the separated water so that the waste water has a predetermined concentration. The feeding means and the taking-out means are adjusted so that the feeding speed and the taking-out speed are adjusted to predetermined amounts so that they can be processed continuously.


本発明によれば、高負荷廃水に接触して加熱するヒータ部分が、フッ素樹脂からなるため前記高負荷廃水に含まれる酸やアルカリによる腐食が殆ど無く、長期使用にも耐え過度なメンテナンスを不要とすることができるという効果がある。又、フッ素樹脂のヒーター部分は、高温でも不純物の付着、焼付を回避出来、熱交換率の低下を防止出来るのに対し、ステンレスの熱交換器では、その表面に不純物が付着し焼付いて熱交換面積が減少するおそれがある。   According to the present invention, the heater portion that is heated in contact with the high-load wastewater is made of fluororesin, so there is almost no corrosion due to acid or alkali contained in the high-load wastewater, and it can withstand long-term use and does not require excessive maintenance. There is an effect that can be. Also, the fluororesin heater part can avoid adhesion and seizure of impurities even at high temperatures and prevent a decrease in the heat exchange rate. On the other hand, in a stainless steel heat exchanger, impurities adhere to the surface and seize and heat exchange. The area may decrease.

また、電気抵抗発熱等を用いる方式や、処理装置に備えられたボイラーによって処理槽内に収容された処理対象廃水を直接加熱する方式と異なり、任意の高温熱源から得られる水蒸気等の温熱流体を、加熱手段としてのフッ素樹脂性チューブ内に通すことで該チューブを高温化させて処理対象廃水を加熱するという熱交換方式としたことによって、工場内に発生する廃熱等を利用することができ、廃水処理のためのランニングコストを抑制することができるという効果がある。   In addition, unlike a method using electrical resistance heat generation or a method in which the waste water to be treated contained in the treatment tank is directly heated by a boiler provided in the treatment apparatus, a thermal fluid such as water vapor obtained from an arbitrary high-temperature heat source is used. By using a heat exchange system that heats the wastewater to be treated by passing the tube through a fluororesin tube as a heating means, waste heat generated in the factory can be used. There is an effect that the running cost for waste water treatment can be suppressed.

また、連続的に処理対象廃水を処理することができるため処理稼動率を高度化することができるという効果がある。   Moreover, since the waste water to be treated can be treated continuously, there is an effect that the treatment operation rate can be enhanced.

また、処理対象廃水から気化分離して得られた分離水を工業用水として再利用することができ新水の使用量を減量することができるという効果がある。   In addition, there is an effect that the separated water obtained by vaporization and separation from the waste water to be treated can be reused as industrial water, and the amount of new water used can be reduced.

また、処理対象廃水から水分を分離し、前記廃水を濃縮して減量できるため排出量を削減することができ、処理業者に対して支払う処理費用を低額化することができて上記効果等を含め結果として、処理対象廃水の処理に要するトータルコストを圧縮することができるという効果がある。   In addition, water can be separated from the wastewater to be treated, and the wastewater can be concentrated to reduce the amount of waste, so that the amount of discharge can be reduced, and the processing cost paid to the processing contractor can be reduced, including the above effects. As a result, there is an effect that the total cost required for treatment of the wastewater to be treated can be compressed.

この発明の好ましい実施の形態を、図を参照しながら以下に詳細に説明する。図1は、本発明のシステム全体の概念を示す図、図2は本発明の装置における加熱手段の構成を示す図であり、図3は図2のAA’断面を示す図であり、図4は図2のBB’断面を示す図である。   A preferred embodiment of the present invention will be described below in detail with reference to the drawings. 1 is a diagram showing the concept of the entire system of the present invention, FIG. 2 is a diagram showing the configuration of the heating means in the apparatus of the present invention, FIG. 3 is a diagram showing the AA ′ cross section of FIG. FIG. 3 is a view showing a BB ′ cross section of FIG. 2.

図1に示すように、本実施の形態例の高負荷廃水の処理装置は、原水(V)即ち未処理の処理対象廃水を収容するための貯留槽(1)と、原水(V)を処理するための処理槽(2)と、前記貯留槽(1)から原水(V)を取り出して処理槽(2)へ移送するための流入路(3)と、前記処理槽(2)に投入する原水(V)の量を調整するための前記流入路(3)上に設けられる流入量調整手段(4)と、前記処理槽(2)内において処理対象廃水(W)を加熱気化処理するための加熱手段(5)と、この加熱手段(5)に温熱流体を導通させるための流通路(6)と、前記処理槽(2)内において加熱気化されて廃水(W)から分離された蒸気を前記処理槽(2)内から取り出すための蒸気取出手段(7)と、この蒸気取出手段(7)によって取り出された蒸気を捕集しつつ凝縮するための分離水生成手段(8)と、前記処理槽(2)内において水分を気化除去して所定の濃度に濃縮された廃水を前記処理槽(2)の外部に取り出すための流出路(9)と、前記処理槽(2)から取り出す濃縮廃水(X)の量を調整するための前記流出路(9)上に設けられる流出量調整手段(10)と、濃縮廃水(X)を一時的に貯留しておくための濃縮廃水貯留槽(11)と、を備えて構成される。   As shown in FIG. 1, the high load wastewater treatment apparatus according to the present embodiment treats raw water (V), that is, a storage tank (1) for containing untreated waste water to be treated, and raw water (V). Processing tank (2) for removing the raw water (V) from the storage tank (1) and transferring it to the processing tank (2) and the processing tank (2) Inflow amount adjusting means (4) provided on the inflow path (3) for adjusting the amount of raw water (V) and heat treatment vaporization treatment of waste water (W) to be treated in the treatment tank (2) Heating means (5), a flow passage (6) for passing a hot fluid through the heating means (5), and steam vaporized by heating in the treatment tank (2) and separated from the waste water (W) For removing the steam from the treatment tank (2), and separated water generating means for collecting and condensing the steam taken out by the steam taking means (7) ( ), An outflow path (9) for taking out the waste water which has been evaporated and removed in the treatment tank (2) and concentrated to a predetermined concentration, and the treatment tank (2) ) For adjusting the amount of concentrated waste water (X) to be taken out from the outflow channel (9) for adjusting the amount of concentrated waste water (X) and the concentration for temporarily storing the concentrated waste water (X) And a waste water storage tank (11).

貯留槽(1)は、未処理の処理対象廃水である原水(V)を貯留するための適当な容積を有するタンクであり、工場等から出された処理対象廃水を適時にその内部に投入し得るように構成されている。また、この貯留槽(1)は収容する廃水が腐食性の強い高負荷廃水であっても長期間に渡って保持し得る耐食性と頑強性を有することが好ましく、コンクリート等で周囲を補強して構成することが望ましい。   The storage tank (1) is a tank having an appropriate volume for storing raw water (V) that is untreated processing target wastewater, and the processing target wastewater discharged from a factory or the like is introduced into the tank in a timely manner. Configured to get. The storage tank (1) preferably has corrosion resistance and robustness that can be maintained for a long time even if the wastewater to be stored is highly corrosive wastewater, and the surroundings are reinforced with concrete or the like. It is desirable to configure.

処理槽(2)は、適当な容積を有するステンレス製のタンクであり、タンクの下方に処理対象廃水の流入口(12)と、濃縮廃水(X)を取り出すための流出口(13)とを有し、タンク上部に加熱気化して分離された蒸気を処理槽(2)の外部に排出するための排出口(14)を設けて構成され、またタンク上部には加熱手段(5)が配置される。勿論、処理槽(2)は高負荷廃水に対する高温下における耐食性があって長期間に渡って収容することができ、効率的に熱交換を行うことができ、また廃水から気化分離した蒸気や濃縮した廃水を効率的に処理槽(2)外に取り出すことができるものであればよく、形状や流入口(12)、流出口(13)、排出口(14)や加熱手段(5)の取り付け位置等は適宜選択することが可能である。   The treatment tank (2) is a stainless steel tank having an appropriate volume, and an inlet (12) for the wastewater to be treated and an outlet (13) for taking out the concentrated wastewater (X) below the tank. It has a discharge port (14) for discharging vapor separated by heating and vaporization to the outside of the processing tank (2) at the upper part of the tank, and heating means (5) is arranged at the upper part of the tank. Is done. Of course, the treatment tank (2) is resistant to high-load wastewater at high temperatures and can be accommodated for a long period of time, efficiently exchanging heat, vaporized and separated from wastewater, and concentrated. Wastewater can be removed from the treatment tank (2) efficiently, and the shape, inlet (12), outlet (13), outlet (14) and heating means (5) are installed. The position and the like can be appropriately selected.

流入路(3)は、高負荷廃水に対する耐食性が高い素材で形成されたパイプで構成され、その一端が前記貯留槽(1)内に収容された原水(V)の水面より低位置に配置され、他端が前記処理槽(2)の流入口(12)に連結される。この流入路(3)上には、貯留槽(1)から処理槽(2)へ移送する処理対象廃水の量を調整するための流入量調整手段(4)が設けられることが好ましい。   The inflow channel (3) is composed of a pipe formed of a material having high corrosion resistance against high-load wastewater, and one end thereof is arranged at a position lower than the surface of the raw water (V) accommodated in the storage tank (1). The other end is connected to the inlet (12) of the treatment tank (2). It is preferable that an inflow amount adjusting means (4) for adjusting the amount of waste water to be treated transferred from the storage tank (1) to the treatment tank (2) is provided on the inflow channel (3).

流入量調整手段(4)は、好ましくは、前記貯留槽(1)から原水を汲み出してそれを前記処理槽(2)へ送り出すためのポンプ(15)と、流入路(3)内を流通する原水(V)の量を調整し得る流入量規制バルブ(16)と、処理槽(2)内に収容された廃水(W)の量を、多過ぎる場合には貯留槽(1)に廃水を戻すようにして、所定量に調整するためのレベルコントローラー(17)と、から構成され前記流入路(3)上に設けられる。   The inflow rate adjusting means (4) preferably circulates in the inflow channel (3) with a pump (15) for pumping raw water from the storage tank (1) and sending it to the treatment tank (2). An inflow control valve (16) that can adjust the amount of raw water (V) and the amount of waste water (W) stored in the treatment tank (2), if there is too much, waste water is stored in the storage tank (1). A level controller (17) for adjusting to a predetermined amount so as to return is provided on the inflow path (3).

図2及び図3にも示すように加熱手段(5)は、複数のフッ素樹脂製のチューブ(18)の両端同士をそれぞれ揃えて結束し、この結束されたそれぞれの端部を一つの開口にまとめ、前記処理槽(2)内に、前記チューブ(18)の外表面に該処理槽(2)内に収容された前記処理対象廃水(W)が接触するように配置し、任意の高温熱源から得られる温熱流体を前記チューブ(18)それぞれの内部に通過させ、前記温熱流体の熱を該チューブ(18)を介して前記処理槽(2)内に収容された前記廃水(W)に伝達して該廃水(W)を効率的に加熱気化させることができるように構成される。更に、前記処理槽(2)内において廃水(W)内に上記加熱手段(5)を潜在せさたときに、浮力による浮上や廃水の流動等による加熱手段(5)の遊動を防止する目的で支持部材(19)等を用いて加熱手段(5)を固定することが望ましい。以上のように加熱手段(5)を構成することによって、高効率で熱交換を行うことができると共に、高温下における高負荷廃水による高度な耐食性や環境ストレスクラッキングを得ることができ、長期使用にも耐え得るようにすることが可能である。加熱手段(5)の下部にエア噴出管(31)を配置し、該噴出管(31)から下向きにエアを噴出させることにより、廃水の撹拌及び蒸発を促進させると共に、加熱手段の表面に異物が付着するのを防止する。   As shown in FIG. 2 and FIG. 3, the heating means (5) has a plurality of fluororesin tubes (18) aligned at both ends and bound together, and each of the bound ends is formed into one opening. In summary, in the treatment tank (2), the waste water (W) to be treated contained in the treatment tank (2) is in contact with the outer surface of the tube (18), and an arbitrary high-temperature heat source The thermal fluid obtained from is passed through each of the tubes (18), and the heat of the thermal fluid is transferred to the waste water (W) accommodated in the treatment tank (2) via the tubes (18). Thus, the waste water (W) can be efficiently heated and vaporized. Furthermore, when the heating means (5) is hidden in the waste water (W) in the treatment tank (2), the purpose of preventing floating of the heating means (5) due to buoyancy, waste water flow, etc. It is desirable to fix the heating means (5) using a support member (19) or the like. By configuring the heating means (5) as described above, heat exchange can be performed with high efficiency, and high corrosion resistance and environmental stress cracking due to high-load wastewater at high temperatures can be obtained for long-term use. It is possible to endure even. An air jet pipe (31) is arranged below the heating means (5), and air is jetted downward from the jet pipe (31) to promote stirring and evaporation of the wastewater and foreign matter on the surface of the heating means. To prevent adhesion.

流通路(6)は、任意の高温熱源によって加熱されて生成される温熱流体の生成位置から前記加熱手段(5)まで温熱流体を流通させ、該加熱手段(5)内に温熱流体を導入させるためのものであり、耐熱性及び低熱伝導性のパイプを用いて構成されることが好ましいが、勿論これに限らず、温熱流体を加熱手段(5)内に導通させることができるものであればよい。また、この流通路(6)を通じて加熱手段(5)内に導通する温熱流体の量を調整するための流通量調整手段(20)としてのバルブを設けることが可能である。   The flow path (6) allows the hot fluid to flow from the position where the hot fluid generated by heating by an arbitrary hot heat source is generated to the heating means (5), and introduces the hot fluid into the heating means (5). However, the present invention is not limited to this, and of course, as long as the hot fluid can be conducted into the heating means (5). Good. Further, it is possible to provide a valve as a flow rate adjusting means (20) for adjusting the amount of the thermal fluid conducted into the heating means (5) through the flow passage (6).

蒸気取出手段(7)は、処理槽(2)内において加熱気化されて廃水(W)から分離された蒸気を前記処理槽(2)内から該処理槽(2)に設けられた排出口(14)から取り出すためのファンであるが、このファンとしては従来公知の技術を採用することが可能であり、特に限定されるものではない。またこの蒸気取出手段(7)としてのファンは必ず無ければならないというものではなく、有っても無くてもよく適宜選択できるが、ファンを取り付けた方が、濃縮効率を高めることができ好ましい。   The steam take-out means (7) discharges steam that has been vaporized by heating and separated from the waste water (W) in the treatment tank (2) from the treatment tank (2) to the discharge port (2) provided in the treatment tank (2). 14), the fan can be a conventionally known technique and is not particularly limited. Further, the fan as the vapor extraction means (7) does not necessarily have to be present, and may or may not be selected as appropriate, but it is preferable to attach the fan because the concentration efficiency can be increased.

図4にも示すように、分離水生成手段(8)は、前記蒸気取出手段(7)によって取り出された蒸気を捕集しつつ凝縮して、分離水(Z)を得るためのものであり、所定の長さを有する高熱伝導性のパイプ(21)を降下勾配を以て配置し、このパイプ(21)の外面に布等の吸水体(22)を被覆して冷却用パイプ(23)とし、この上部の開口(24)から下部の開口(25)に向かって該冷却用パイプ(23)の内部に前記蒸気取出手段(7)によって前記処理槽(2)から取り出された蒸気を通過させるようにし、下部に適当な間隔で内外に貫通した孔(26)を設けてなる水パイプ(27)を前記冷却用パイプ(23)の上部に、該冷却用パイプ(23)に沿って配置して、該水パイプ(27)内に冷却用水(Y)()を通して前記孔(26)から該冷却用水(Y)()が前記冷却用パイプ(23)に滴下されるようにし、前記冷却用パイプ(23)の下部の開口(25)にほぼ鉛直方向に向けた鉛直パイプ(28)を配置して蒸気に含まれていたガスと水分とを最終的に分け、該鉛直パイプ(28)の下端に分離水貯留槽(29)を配置し、上端に該鉛直パイプ(28)内に雨水等が侵入するのを防止するための傘(30)を配置して構成され、水パイプ(27)から滴下して冷却用パイプ(23)の外面に施された前記吸水体(22)に吸水された冷却用水(Y)()は、その後、冷却用パイプ(23)内を通過する蒸気の熱との間で熱交換がなされて気化し、該冷却用パイプ(23)内を流通していた蒸気が冷却されて該冷却用パイプ(23)内を通過し終える前に凝縮し、分離水(Z)が得られるようになっている。   As shown also in FIG. 4, the separated water generating means (8) is for collecting and condensing the steam taken out by the steam taking out means (7) to obtain separated water (Z). The pipe (21) having a predetermined length is disposed with a descending gradient, and the outer surface of the pipe (21) is covered with a water absorbent body (22) such as cloth to form a cooling pipe (23). From the upper opening (24) toward the lower opening (25), the steam extracted from the processing tank (2) by the steam extraction means (7) is allowed to pass through the cooling pipe (23). A water pipe (27) provided with holes (26) penetrating inside and outside at an appropriate interval in the lower part is disposed above the cooling pipe (23) along the cooling pipe (23). The cooling water (Y) () is passed through the water pipe (27) through the hole (26) and dropped into the cooling pipe (23), and the cooling pipe A vertical pipe (28) oriented in a substantially vertical direction is arranged in the lower opening (25) of (23) to finally separate the gas and moisture contained in the steam, and the lower end of the vertical pipe (28) The separated water storage tank (29) is arranged at the top, and an umbrella (30) for preventing rainwater and the like from entering the vertical pipe (28) is arranged at the upper end from the water pipe (27). The cooling water (Y) () dripped and absorbed by the water absorbing body (22) applied to the outer surface of the cooling pipe (23) is then heated with the heat of steam passing through the cooling pipe (23). The steam exchanged between the two pipes is vaporized, and the steam flowing through the cooling pipe (23) is cooled and condensed before passing through the cooling pipe (23). ) Can be obtained.

流出路(9)は、高温下における高負荷廃水に対する耐食性のパイプで構成され、前記処理槽(2)内において濃縮された廃水を前記処理槽(2)の外部に取り出すために前記処理槽(2)の下端に設けられた流出口(13)に一端が連結され、他端が濃縮廃水貯留槽(11)に濃縮廃水(X)が送り出されるように配置される。また、この流出路(9)上には、該流出路(9)内を流通する濃縮廃水(X)の量を調整するための流出量調整手段(10)としてのバルブを設けることが可能である。   The outflow channel (9) is composed of a corrosion-resistant pipe against high-load wastewater at high temperatures, and the treatment tank (2) is used to take out the wastewater concentrated in the treatment tank (2) to the outside of the treatment tank (2). One end is connected to the outlet (13) provided at the lower end of 2), and the other end is arranged so that the concentrated waste water (X) is sent out to the concentrated waste water storage tank (11). On the outflow channel (9), a valve as an outflow rate adjusting means (10) for adjusting the amount of concentrated waste water (X) flowing through the outflow channel (9) can be provided. is there.

濃縮廃水貯留槽(11)は、前記処理槽(2)内において所定の濃度に濃縮処理された濃縮廃水(X)をその処理業者に引き渡すまでの間貯留しておくための適当な容積を有するステンレス製のタンクであり、収容する濃縮廃水(X)が腐食性の極めて強いものであっても長期間に渡って保持し得る耐食性と頑強性を有することが好ましく、コンクリート等で周囲を補強して構成することが望ましい。   The concentrated waste water storage tank (11) has an appropriate volume for storing the concentrated waste water (X) concentrated to a predetermined concentration in the processing tank (2) until it is delivered to the processing company. It is a stainless steel tank, and it is preferable to have corrosion resistance and robustness that can be retained for a long period of time even if the concentrated wastewater (X) is extremely corrosive. It is desirable to configure.

以上説明した装置を用いる場合には、工場等から出された高負荷廃水を貯留槽(1)に導入しそこから調整された所定の速度で原水をポンプ(15)で汲み出してレベルコントローラー(17)を経由して処理槽(2)に投入する。このレベルコントローラー(17)によって処理槽(2)内の廃水(W)の量を調整して、該量が一定に保持されるようにして多過ぎるときには、レベルコントローラー(17)を通じて貯留槽(1)に還元される。処理槽(2)においては、任意の高温熱源によって加熱された温熱流体を用いて加熱手段(5)を通じて廃水(W)との間で熱交換がなされ、該廃水(W)が加熱される。この加熱は、該廃水(W)が気化する程度の温度までなされ、これによって該廃水(W)に含まれる水分が蒸発し、蒸気取出手段(7)であるファンによって前記処理槽(2)内から吸い出される。この吸い出された蒸気は、分離水生成手段(8)を通じて凝縮されて分離水(Z)とガスとに分けられ、分離水(Z)は捕集されて再利用可能となる。一方、前記処理槽(2)内において水分が気化され水分量が減量されて濃縮した廃水は、投入量と蒸発量及び流出量を調整することによって所定の濃度に保持されつつ連続的に流出口(13)から取り出され濃縮廃水貯留槽(11)に繰り出され収容される。   In the case of using the apparatus described above, high-load wastewater discharged from a factory or the like is introduced into the storage tank (1), and raw water is pumped out by a pump (15) at a predetermined speed adjusted from there. ) To the treatment tank (2). When the amount of waste water (W) in the treatment tank (2) is adjusted by the level controller (17) and the amount is kept so as to be kept constant, the storage tank (1 ). In the treatment tank (2), heat is exchanged with the wastewater (W) through the heating means (5) using a hot fluid heated by an arbitrary high-temperature heat source, and the wastewater (W) is heated. This heating is performed to a temperature at which the waste water (W) is vaporized, whereby the water contained in the waste water (W) evaporates, and the fan in the treatment tank (2) is vaporized by the steam extraction means (7). Sucked out. The sucked vapor is condensed through the separated water generating means (8) and separated into separated water (Z) and gas, and the separated water (Z) is collected and can be reused. On the other hand, the waste water that has been evaporated in the treatment tank (2) and reduced in water amount and concentrated is continuously discharged while being maintained at a predetermined concentration by adjusting the input amount, evaporation amount, and outflow amount. It is taken out from (13) and drawn out and stored in the concentrated wastewater storage tank (11).

本発明のシステム全体の概念を示す図The figure which shows the concept of the whole system of this invention 本発明の装置における加熱手段の構成を示す図The figure which shows the structure of the heating means in the apparatus of this invention. 図2のAA’断面を示す図The figure which shows the AA 'cross section of FIG. 図2のBB’断面を示す図The figure which shows the BB 'cross section of FIG.

符号の説明Explanation of symbols

1 貯留槽
2 処理槽
3 流入路
4 流入量調整手段
5 加熱手段
6 流通路
7 蒸気取出手段
8 分離水生成手段
9 流出路
10 流出量調整手段
11 濃縮廃水貯留槽
12 流入口
13 流出口
14 排出口
15 ポンプ
16 流入量規制バルブ
17 レベルコントローラー
18 チューブ
19 支持部材
20 流通量調整手段
21 パイプ
22 吸水体
23 冷却用パイプ
24 上部の開口
25 下部の開口
26 孔
27 水パイプ
28 鉛直パイプ
29 分離水貯留槽
30 傘
31 エア噴出管
V 原水
W 廃水
X 濃縮廃水
Y 冷却用水
Z 分離水
DESCRIPTION OF SYMBOLS 1 Storage tank 2 Processing tank 3 Inflow path 4 Inflow amount adjustment means 5 Heating means 6 Flow path 7 Steam extraction means 8 Separation water generation means 9 Outflow path 10 Outflow amount adjustment means 11 Concentrated waste water storage tank 12 Inlet 13 Outlet 14 Exhaust Outlet 15 Pump 16 Inflow control valve 17 Level controller 18 Tube 19 Support member 20 Flow rate adjusting means 21 Pipe 22 Water absorber 23 Cooling pipe 24 Upper opening 25 Lower opening 26 Hole 27 Water pipe 28 Vertical pipe 29 Separated water storage Tank 30 Umbrella 31 Air outlet pipe V Raw water W Waste water X Concentrated waste water Y Cooling water Z Separated water

Claims (1)

廃水処理槽と、A wastewater treatment tank;
この槽内に未処理の処理対象廃水を投入するための流入路と流入量調整機能とを備えた投入手段と、An input means having an inflow path and an inflow amount adjusting function for introducing untreated wastewater to be treated into the tank,
少なくともその一部が前記槽内に収容された前記廃水に接触するように配置され任意の高温熱源から得られた蒸気をその内部に通過させるようにしたフッ素樹脂製チューブを結束してなる処理対象廃水を加熱処理するための加熱手段と、A treatment target formed by bundling a fluororesin tube that is arranged so that at least a part thereof is in contact with the wastewater contained in the tank and allows vapor obtained from an arbitrary high-temperature heat source to pass therethrough. Heating means for heat treating the waste water;
該槽内において処理され所定の濃度に濃縮された処理済み廃水を該槽内から取り出すための流出路と流出量調整機能を備えた取出手段と、An outflow path for taking out the treated wastewater treated in the tank and concentrated to a predetermined concentration from the inside of the tank, and an extraction means having an outflow amount adjusting function;
処理対象廃水を加熱したことによって気化分離された蒸気を捕集し且つ凝縮して分離水を生成するための、降下勾配を以て配置され外面に吸水体を被覆してなる冷却管の内部に前記蒸気を通過させ、下部に適当な間隔で内外に貫通した孔を設けてなる水パイプを前記冷却管の上部に、該冷却管に沿って配置して、該水パイプ内に水を通して前記孔から水が冷却管に滴下されるように構成してなる分離水生成手段と、Steam that is vaporized and separated by heating the wastewater to be treated is collected and condensed to generate separated water, and the steam is disposed inside a cooling pipe that is arranged with a descending gradient and has an outer surface coated with a water absorbent. A water pipe having a hole penetrating inward and outward at an appropriate interval in the lower part is disposed at the upper part of the cooling pipe along the cooling pipe, and water is passed through the water pipe from the hole. Separated water generating means configured to be dripped into the cooling pipe,
を備え、With
廃水処理槽内において、該槽内に収容された処理対象廃水を前記加熱手段によって加熱気化させ、該槽内に収容された前記廃水の水分量を減量して濃縮し、In the wastewater treatment tank, the waste water to be treated contained in the tank is heated and vaporized by the heating means, and the water content of the wastewater contained in the tank is reduced and concentrated.
前記廃水を気化して分離した蒸気を前記分離水生成手段によって捕集し且つ凝縮させて分離水を抽出し、Steam separated by vaporizing the waste water is collected and condensed by the separated water generating means to extract the separated water,
前記廃水が所定の濃度になるように前記投入手段と取出手段の調整を行って、投入速度と取出速度を所定の量に調整し、連続的に処理することができるようにしたことを特徴とする高負荷廃水の処理システム。By adjusting the charging means and the discharging means so that the waste water has a predetermined concentration, the charging speed and the discharging speed are adjusted to a predetermined amount, and can be continuously processed. High load wastewater treatment system.
JP2004120826A 2004-04-15 2004-04-15 High load wastewater treatment system Expired - Fee Related JP3981674B2 (en)

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