JP2010075816A - Infiltration purification method for contaminated soil and deep underground inorganization treatment method for contamination - Google Patents
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/30—Wastewater or sewage treatment systems using renewable energies
- Y02W10/37—Wastewater or sewage treatment systems using renewable energies using solar energy
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Abstract
Description
本発明は、地球環境の保全のための汚染土壌の自然循環機能を活用した浄化を目的とする環境技術に関する。 The present invention relates to an environmental technology aimed at purification using a natural circulation function of contaminated soil for the preservation of the global environment.
従来の環境汚染物の浄化法は、有害物質を抽出しておおむね高温焼成などによる高エネルギによる積極物理的な浄化法(無機化)である。この欠点は、環境改善に多くの資源・エネルギが必要でその実施コストと必要エネルギを作るための更なる環境汚染物が生成される。本発明は、山頂に降る雨水が地層に浸透して1000年単位の長期間を経て多くの有害物質を安全なミネラル分に分解してなる水を生成する温泉などに着眼した。深層水の生成過程は活性化学物質である有害な重金属や硫化物などが鉱物地層などを経て、溶解している有害な汚染水が高温高圧の深層地下で長期間を掛けて無害化(安定化)ミネラル成分に生成される。本発明の基本はこの自然循環生成過程を利用する。その基本手段は人工的に地上の有害物質を深層地下に注入して自然分解法則を得る。一般に人間が作り出す短期的な化学生成物は生物にとって長期間を経た生成物と異なり、活性度が高い。これが有害物質と考えることができ、生物の生育環境に適するには1000年単位の長期自然循環を経た物質にすることが環境改善になる。この法則適用には温泉のある地層には生成原理が存在することを根拠に、汚染物を深層地下に注入して、地表に染み出るまでの数千年の時間を掛けた高温高圧の物質安定化(無害化)の自然循環法則を適用する。幸い日本は全土に温泉があり、この原理が全土に適用できよう。 The conventional purification method of environmental pollutants is a positive physical purification method (mineralization) with high energy by extracting harmful substances and generally firing at high temperature. This drawback requires more resources and energy to improve the environment, and its cost of implementation and additional environmental pollutants to produce the required energy are generated. The present invention has focused on hot springs and the like that generate water formed by the decomposition of many harmful substances into safe minerals after a long period of 1000 years when rain water falling on the mountain peak penetrates the formation. In the process of deep water generation, harmful heavy metals and sulfides, which are active chemical substances, pass through mineral formations, etc., and dissolved harmful contaminated water is rendered harmless over a long period of time under high temperature and high pressure (stabilization). ) Produced into mineral components. The basis of the present invention utilizes this natural circulation generation process. The basic means is to artificially inject harmful substances on the ground into the deep underground to obtain the law of natural decomposition. In general, short-term chemical products produced by humans are highly active for organisms, unlike products that have been used for a long time. This can be considered a harmful substance, and in order to be suitable for the living environment of living organisms, a substance that has undergone a long-term natural circulation of 1000 years is an environment improvement. The application of this law is based on the existence of the generation principle in the geological formation with hot springs, and the high-temperature and high-pressure stability of the material, which took thousands of years to inject the contaminants into the deep underground and exude to the surface. Apply the natural circulation law of detoxification (detoxification). Fortunately, Japan has hot springs throughout the country, and this principle can be applied to the whole country.
環境汚染物の土壌汚染の自然循環浄化は周期を考慮すれば、有機物を高温・高圧での長期間の深層地下による無害化の法則である。これらは水を媒体とすることから、法則適用の技術基本となるのは汚染土壌の拡散防止と有害物質の浸透水による洗浄と汚染水の深層地下への搬送を得るための方法と手段の開発である。 Natural circulation purification of soil contamination of environmental pollutants is a law of detoxification of organic matter by deep underground for a long time at high temperature and high pressure, considering the cycle. Since these use water as a medium, the basic technology for applying the law is to develop methods and means for preventing the diffusion of contaminated soil, cleaning harmful substances with infiltrated water, and transporting contaminated water to the deep underground. It is.
自然循環法則を利用した汚染土壌浄化法の技術開発に成功した方法と手段について述べる。この基本技術の構成は、人間が短期間に生成した有害化学物質は全て水に分散・溶解などする。生物環境に適さない有害物質をまず、拡散させないことが重要であり、これには地表地下に貯蔵することが初期の対策として最適であり過去から実施されてきた。しかし、有害物質は水溶・分散溶融して地表に染み出し、地表地下水の流動から拡散して、生物に影響を与える。 This paper describes the methods and means that have succeeded in developing the technology for the purification of contaminated soil using the law of natural circulation. In this basic technology, all harmful chemical substances generated by humans in a short period of time are dispersed and dissolved in water. It is important not to disperse harmful substances that are not suitable for the biological environment, and for this purpose, storage in the ground underground is the best initial measure and has been implemented since the past. However, harmful substances dissolve in water, disperse and ooze out to the surface, diffuse from the groundwater flow, and affect living organisms.
そこで、まず図1の説明図に示す汚染の拡散防止を図る必要がある。対象にする汚染領域全てまたは必要な除染領域を設定する。次いでこれには耐食性が期待できるガラス繊維強化プラスチック製やステンレス製の透水管を対象地域を覆う等間隔で垂直に汚染深さ以上に井戸の様に打設する。この井戸から注水または排水して、地下水の流れを制御して汚染地域を隔離する。ついで汚染源に同様の透水管による井戸を打設して排水または注水して汚染物を土壌洗浄する。必要によっては吸着剤など注水に混入する。集めた土壌透水の洗浄汚染された排水を700メートル以下の地層に、数千年保有害物質が留保安定化できる深層地下に高圧注入する。
Therefore, it is first necessary to prevent the diffusion of the contamination shown in the explanatory diagram of FIG. Set all the contaminated areas or the necessary decontaminated areas. Next, a glass fiber reinforced plastic or stainless steel water permeable tube, which can be expected to have corrosion resistance, is placed vertically at equal intervals covering the target area like a well above the contamination depth. Water is poured or drained from this well to control the flow of groundwater and isolate the contaminated area. Next, a well with a similar permeation pipe is placed in the pollution source, and the soil is washed by draining or pouring water. If necessary, mix with water such as adsorbent. Collected drainage of soil permeated water is injected into the underground layer below 700 meters under high pressure into the deep underground where thousands of years of hazardous substances can be retained and stabilized.
必要によっては排水ポンプの配管をまとめて貯水タンクに入れ、タンクを減圧して有機物の有害ガスを抽出して高温燃焼管内で焼却する。汚染水に吸着・凝集剤やイオン吸着膜を介して汚染水の汚染物を濃縮して同様に深層地下に高圧注水する。すなわち、有害物質を高温償却や化学分解しないで非分解の状態で汚染物質を浸透水により洗浄と深層地下へ注入して、長期間を掛けた自然循環法則による有害物質の無害化を図るシステム。
If necessary, drain pump piping is put into a water storage tank, the tank is depressurized to extract organic harmful gases, and incinerated in a high-temperature combustion pipe. Contaminated water is concentrated in the contaminated water via an adsorbent / flocculant and ion adsorption membrane, and high-pressure water is injected into the deep underground. In other words, a system that cleans and injects pollutants into the deep underground with osmotic water in a non-decomposed state without high-temperature amortization or chemical decomposition, and makes the harmful substances harmless by the law of natural circulation over a long period of time.
本発明の効果は、自然循環法則である1000年から1万年循環周期で深層地下水の重金属など有害化学物質を無害化(安定ミネラル成分に無機化)する。有害物質を透水管により拡散防止して抽出汚染水を深層地下に高圧注入して自然循環法則を適用、土壌有害物質の除染と無害化処理ができる。この方法を用いると、従来の汚染土壌の搬出と積極分解(熱処理)などの手段に比べて、汚染土壌の移動を必要とせず、現状の状態で地下水の流れをつくる微小エネルギ(風車・太陽電池の自然エネルギ)のみで除染して無機化できるため、大幅なコスト軽減と二次的汚染処理問題も解消する。さらに現状の状態で工事が簡単に実施でき短期間で完工、人間に必要な安全な環境が提供でき、約数十年の歳月を掛けて封入された汚染物を安全に自然浄化できる。
The effect of the present invention is to detoxify harmful chemical substances such as heavy metals in deep groundwater (mineralize into a stable mineral component) with a circulation cycle of 1000 to 10,000 years, which is the law of natural circulation. Prevents the diffusion of harmful substances with a permeation pipe, applies high pressure injection of extracted contaminated water into the deep underground, and applies the laws of natural circulation to decontaminate and detoxify soil harmful substances. Using this method, compared to conventional methods such as removal and active decomposition (heat treatment) of contaminated soil, there is no need to move contaminated soil, and the micro-energy (windmills and solar cells) that creates groundwater flow in the current state Can be decontaminated and mineralized only with natural energy), which greatly reduces costs and eliminates secondary pollution problems. In addition, construction can be performed easily in the current state, completed in a short period of time, and a safe environment necessary for human beings can be provided. Contaminated contaminants can be safely purified naturally over several decades.
また、除染効果と除染物の無害化効果の2つがある。それぞれ単独でもその効果を発揮できる。
In addition, there are two effects: decontamination effect and detoxification effect of decontamination product. Each of them can exert its effect.
図1に示す土壌汚染地域の拡散を防止するための周囲、除染する領域に敷設する透水管には必要な透水穴が無数に必要であること、外圧に強いこと、土壌のつまりがないことが要求され、この透水管にはコンクリート製などは強度と目つまりで適さず、ステンレス材に穴あき加工は困難で高価である。FRP廃材を粉砕してなる材料をポリエステル樹脂などで接着してなる遠心成形管はリサイクル材料の透水管としてこの問題を解消するとともに腐食にも耐えて長期間の使用が可能であるばかりか必要な強度も得られるため、注水管・透水管にはFRP廃棄物からなる透水管が最適である。 The permeation pipes installed in the perimeter and the decontamination area shown in Fig. 1 for preventing diffusion of the soil-contaminated area must have innumerable permeation holes, resistant to external pressure, and free from soil clogging. For this permeable tube, concrete and the like are not suitable due to strength and eyes, and it is difficult and expensive to perforate stainless steel. Centrifugal tube made by pulverizing FRP waste material with polyester resin, etc. is not only necessary to solve this problem as a permeable tube of recycled material, but also to withstand corrosion and to be used for a long time. Since strength is also obtained, a water permeation pipe made of FRP waste is optimal for the water injection pipe and water permeation pipe.
深層地下への高圧注水管には、深層地下の石油生産に使用するAPI仕様の管が適する。中でも長期使用と腐食性能を要求するため、ステンレスSUS316材料など腐食に強い金属材料または、ビニルエステル樹脂を使用したFRP遠心成形高圧管が用いられる。とくに遠心成形法によって作られた高圧FRP管は、28メガパスカル以上の耐圧を持ち、さらに40年間の耐久性があり、コスト面でも最も安価であり、注水管として最適である。 For the high-pressure water injection pipe to the deep underground, an API specification pipe used for oil production in the deep underground is suitable. Among them, in order to require long-term use and corrosion performance, FRP centrifugal molded high-pressure pipes using a metal material resistant to corrosion such as stainless SUS316 material or vinyl ester resin are used. In particular, a high-pressure FRP pipe made by centrifugal molding has a pressure resistance of 28 megapascals or more, has a durability of 40 years, is the lowest in cost, and is optimal as a water injection pipe.
水に用いる水は、海水を用いて洗浄して深層地下に高圧注水する方法と、地下水や雨水を用いた汚染物質を排水から集めて、産業廃棄物である化学薬品(例えば硫化ソーダ:NaSH)による汚染水に溶解する重金属を凝集沈殿して濃縮、上澄みを再度注水する自然水を用いる方法が採用される。
The water used for water is washed with seawater and injected into the deep underground under high pressure, and pollutants using groundwater and rainwater are collected from the wastewater, and are chemicals that are industrial waste (for example, sodium sulfide: NaSH). A method using natural water in which heavy metal dissolved in the contaminated water is condensed and precipitated and concentrated, and the supernatant is poured again is adopted.
汚染物質のより分離精度の向上を図る必要がある場合はイオン交換樹脂膜による溶融重金属の吸着分離が採用される。汚染物の除去は膜に付着した重金属を塩酸などで洗浄などして膜を再生するときに分離して、汚染物質を濃縮する。濃縮汚染水を造ることは深層地下に高圧注水する水量を減少させることができる。
When it is necessary to improve the separation accuracy of contaminants, adsorption separation of molten heavy metal by an ion exchange resin membrane is employed. Contaminants are removed by washing the heavy metal adhering to the membrane with hydrochloric acid or the like to separate it when regenerating the membrane, thereby concentrating the contaminants. Making concentrated contaminated water can reduce the amount of water injected into the deep underground.
土壌汚染の透水による洗浄する地下流水エネルギは透水管からの注水と排水であり、地下水頭差を汚染境界と汚染域を一般には50ミリメートルから100ミリメートル程度保つことで必要な透水浄化が得られる。これに必要なエネルギは小さい。さらに濃縮洗浄水を作るためのエネルギも同様である。 最も大きな必要エネルギは高圧注水である。濃縮洗浄水とすると少量となり深層地下注水エネルギも少なくなり、これらの必要エネルギは風車や太陽光発電などの単独または併用により十分まかなえる。また必要な洗浄水も雨水などで必要十分まかなえることから、人工的なエネルギを必要としないで数十年の歳月を掛けて汚染土壌の浄化処理が可能となる。
The groundwater energy to be washed by permeation due to soil contamination is water injection and drainage from the permeation pipe, and necessary permeation purification can be obtained by maintaining the difference between the groundwater head and the contamination boundary and the contaminated area generally from about 50 mm to 100 mm. The energy required for this is small. The energy for making concentrated washing water is the same. The largest energy requirement is high-pressure water injection. Concentrated washing water reduces the amount of deep underground water injection energy, and the required energy can be adequately provided by wind turbines and solar power generation alone or in combination. In addition, since the necessary washing water can be sufficiently provided by rain water or the like, the contaminated soil can be purified over several decades without requiring artificial energy.
透水管の有効な付設と深層地下への必要な高圧注水井戸の付設課題について解決した発明内容を説明する。
The content of the invention which solved the effective attachment of a permeable pipe and the attachment problem of the required high-pressure water injection well to the deep underground will be described.
図1は左が汚染土壌の平面、右がそのAA断面を示す。今仮に除染する優先地域または分割除染地域があると仮定する。その区域を図1に示す除染区域とする。除染を目的とする区域には汚染を拡大しないように境界線上に透水管を垂直に付設する。そして汚染部にも透水管を付設する。適当な汚染地域内に深層地下高圧注入管を必要数付設する。
In FIG. 1, the left side is a plane of contaminated soil, and the right side is an AA cross section thereof. Assume that there is a priority area or a divisional decontamination area to be decontaminated. This area is the decontamination area shown in FIG. In the area intended for decontamination, a permeation pipe will be installed vertically on the boundary line so as not to spread the contamination. A permeation pipe is also attached to the contaminated part. Install the necessary number of deep underground high-pressure injection pipes in the appropriate contaminated area.
図1AA断面に示す地下水の2点鎖線が示す水頭が境界線注水−汚染地域排水で汚染地域が低くなる。すなわち注水と排水により地下で汚染水が一方向に流れて除染する。排水を深層地下に注水すれば、除染区域の汚染物質は時間とともに深層地下に移動する。
The water head indicated by the two-dot chain line in the groundwater shown in FIG. 1AA is the boundary water injection-contaminated area drainage, and the contaminated area is lowered. In other words, contaminated water flows in one direction in the basement by water injection and drainage to decontaminate. If drainage is poured into the deep underground, the pollutants in the decontamination area move to the deep underground with time.
ここで除染地域を汚染地域全体とする場合も同様であり、必要な除染領域を区別しても実施効果は同じである。すなわち、汚染量の多少により区別して除染することが得策である。透水管の数量と注水圧(水頭高さ)排水圧(水頭高さ)により地下水の流速をコントロールするなどして、最適な除染法が設計できる。
The same applies to the case where the decontamination area is the entire contaminated area, and the implementation effect is the same even if the necessary decontamination areas are distinguished. In other words, it is a good idea to decontaminate in accordance with the amount of contamination. The optimal decontamination method can be designed by controlling the flow rate of groundwater by the number of permeable pipes and the water injection pressure (water head height) and drainage pressure (water head height).
汚染物質が無害化する深層地下の安定地層への高圧注水課題について解決した発明内容を説明する。
The content of the invention which solved the high-pressure water injection problem to the stable underground layer where the pollutants are rendered harmless will be described.
図2に示す地層断面は、表面地層(表層)と表面近くの汚染土壌層に敷設した注水管・排水管と深層部に複数の地下安定岩盤層の下に高圧注水管で汚染物を無害化する深層地下汚染物貯蔵の構造模型を示す。一般に温泉が掘削される地層構造は地下安定岩盤層があり、その下部に緩慢な流れをして1000年単位で地上から浸透した水を含む層がある。これらは地表に漏れ出すことなく深層海底へ緩慢な流れをしていると考える。これらの温泉利用されている地下層は約500メートルから1500mの深さであり、さらに5000メートルまでの深層地下は古代の海中微生物の堆積による石油生成する層であり、1億年単位の長期間を掛けて地球生成運動の表層が地下にもぐりこんだ地層である。 日本列島は大陸棚地殻変動領域でありこの地層構造が主体である。
The geological section shown in Fig. 2 is detoxified by water injection pipes and drainage pipes laid on the surface strata (surface layer) and the contaminated soil layer near the surface, and high-pressure water injection pipes under multiple underground stable rock formations in the deep layer. A structural model of storage of deep underground contaminants is shown. In general, the geological structure in which hot springs are excavated has an underground stable bedrock layer, and there is a layer containing water that has permeated from the ground in 1000 years under a slow flow. These are considered to flow slowly to the deep sea floor without leaking to the ground surface. The underground layers used by these hot springs are about 500m to 1500m deep, and the deep underground layers up to 5000m are oil-producing layers due to the accumulation of ancient marine microorganisms, and they are long-term units of 100 million years. It is a geological layer where the surface layer of the Earth generation movement is buried underground. The Japanese archipelago is a continental shelf crustal deformation region and is mainly composed of this strata structure.
山岳部の雨水が浸透して長期間の地中流れで作られる温泉が地下に存在することは、地表との間に防水層(岩盤)などがあり、海底などへの流れで海底温泉などからも周知である。すなわち、この流れの下部にも水の浸透を防止する防水層があることも周知である。温泉地層の無機化されたミネラル水(温泉)は有効に利用されているのでこの地層への高圧注水はできない。さらに深層地下にある有機物堆積層が目的の地下貯蔵層になる。有機物が堆積する層(多く堆積する層には石油・石炭など生成)は1億年以上の歴史と堆積した有機物が地表に漏洩していないことから、安定地層である証明である。
The existence of hot springs in the basement where rainwater infiltrates in the mountains and permeates for a long time exists in the basement, and there is a waterproof layer (bedrock) between the ground surface and the flow from the seabed to the seabed. Is also well known. That is, it is also well known that there is a waterproof layer at the bottom of this flow that prevents water from penetrating. Since mineralized mineral water (hot spring) in the hot spring formation is effectively used, high-pressure water injection into this formation is not possible. In addition, the organic sediment layer in the deep underground is the target underground storage layer. The layer in which organic matter is deposited (oil and coal produced in many layers) is a proof that it is a stable formation because it has a history of over 100 million years and the deposited organic matter has not leaked to the surface.
温泉地層の下部で有機物など存在する安定地層が少なくとも地表・温泉層に漏洩するのに1000年単位の年月を必要とすることから、重金属溶解の汚染水は無機化される。すなわち、自然循環の浄化機構に組み入れられる。
The stable water layer, which contains organic substances in the lower part of the hot spring formation, needs 1000 years to leak at least to the surface and hot spring formation, so the contaminated water dissolved in heavy metals is mineralized. That is, it is incorporated into a natural circulation purification mechanism.
深層地下はおおむね700mから3000mに存在することは、各地の掘削資料から推測できる。したがって、深層地下の材質は岩盤であることから、必要注水圧力は岩盤を引き裂く圧力(岩盤を割ること堆積膨張すること)が必要であり、一般に油田の例から10メガパスカルから15メガパスカル以上が必要とされる。最大で25メガパスカル程度である。この時の温度は1000メートル単位で地下温度が約30度上昇するので50度から110度が推定される。よってこの条件に耐える高圧管が必要である。油田用の注水管がこの仕様に該当する。(API規格管)
It can be inferred from the excavation materials in various places that the deep underground exists in the range of 700m to 3000m. Therefore, since the material of the deep underground is rock mass, the required water injection pressure needs to tear the rock mass (splitting and expanding the rock mass), and generally from 10 to 15 megapascals from the oil field example. Needed. The maximum is about 25 megapascals. The temperature at this time is estimated to be 50 to 110 degrees because the underground temperature rises about 30 degrees in units of 1000 meters. Therefore, a high-pressure pipe that can withstand this condition is required. Oil field water injection pipes meet this specification. (API standard tube)
深層地下注水量の削減効果の汚染物質の濃縮法について課題を解決した発明を説明する。
The invention which solved the problem about the pollutant concentration method of the effect of reducing deep underground water injection will be described.
図3は汚染洗浄水を汚染物質の濃縮による非汚染の再洗浄水に利用、濃縮汚染水の深層地下高圧注水の構造全体を示す。洗浄汚染水を濃縮すると、濃縮汚染水量が少なくなることから、洗浄水の確保(循環)ができる。減量分の水量は天然の雨水などで充足できることから、経済効果が大きい。さらに高圧注入には高エネルギが必要なことから高圧注入量の減少は省エネ効果が大きく、風車・太陽光発電など自然エネルギ利用が可能になり、天然雨水利用を併用すれば完全な人工による自然循環の浄化システムが得られる。
FIG. 3 shows the entire structure of the deep underground high-pressure injection of concentrated contaminated water using contaminated wash water as non-contaminated rewash water by concentrating pollutants. When washing contaminated water is concentrated, the amount of concentrated contaminated water decreases, so that washing water can be secured (circulated). Since the amount of water lost can be satisfied with natural rainwater, etc., the economic effect is great. Furthermore, since high energy is required for high-pressure injection, reducing the amount of high-pressure injection has a significant energy-saving effect, making it possible to use natural energy such as windmills and solar power generation. Purification system.
図4は濃縮方法の1つである吸着・凝集法の説明図である。浸透浄化水(汚染水)を排水ポンプで汚染物質除去タンクに入れ、吸着・凝集剤(例えば硫化ソーダ:NaSHなど)の分散注入による汚染水に溶解する重金属を凝集沈殿して濃縮させる。タンクの上澄みは汚染濃度が低いため再度洗浄水に利用できる。少なくなった沈殿濃縮汚染水を高圧ポンプで深層地下に注水する。注水によって減少する洗浄水は雨水など自然水を用いる方法が採用される。
FIG. 4 is an explanatory diagram of an adsorption / aggregation method which is one of the concentration methods. The permeated purified water (polluted water) is put into a pollutant removal tank by a drainage pump, and heavy metals dissolved in the polluted water by dispersion injection of an adsorption / flocculating agent (for example, sodium sulfide: NaSH) are coagulated and concentrated. The supernatant of the tank can be reused for washing water because of low contamination concentration. The reduced concentrated sedimentary water is poured into the deep underground with a high-pressure pump. A method of using natural water such as rain water is adopted as the washing water that is reduced by water injection.
図4に示す減圧ポンプは汚染水のタンクから揮発分の有機物の抽出に使用する。例えばベンゼンなどは水中に分散して存在することから気化して回収ができる。回収した有機ガスは燃焼または白金触媒などで酸化処理する。この気化物の処理は設備の不具合から集積して爆発事故を防止する効果がある。 The decompression pump shown in FIG. 4 is used for extracting volatile organic substances from a tank of contaminated water. For example, since benzene and the like are dispersed in water, they can be vaporized and recovered. The recovered organic gas is burned or oxidized with a platinum catalyst or the like. The treatment of this vaporized material has an effect of preventing explosion accidents by accumulating from the malfunction of the equipment.
水中分散する揮発性有機物の回収と水に溶解する重金属の回収の発明を説明する。
The invention of recovery of volatile organic substances dispersed in water and recovery of heavy metals dissolved in water will be described.
図5はイオン交換樹脂膜を利用した水溶重金属回収と揮発性有機物の回収処理をしめした。揮発性有機物の減圧・燃焼の回収は前記と同じである。汚染水をイオン交換樹脂膜で汚染水を非汚染水と汚染物を分離することができるのは周知である。その後にイオン交換膜を酸性洗浄剤(例えば塩酸)で洗浄して再生使用する。この汚染物質を濃縮した酸洗浄水を一般廃棄物として中和・化学物質で安定化することも可能である。また、濃縮汚染水を深層地下に高圧注入して処理することも出来る。
FIG. 5 shows a recovery process of water-soluble heavy metals and volatile organic substances using an ion exchange resin membrane. Recovery of decompression and combustion of volatile organic substances is the same as described above. It is well known that polluted water can be separated from non-polluted water and pollutants with an ion exchange resin membrane. Thereafter, the ion exchange membrane is washed with an acidic detergent (for example, hydrochloric acid) and recycled. It is also possible to neutralize the acid wash water concentrated with this pollutant and stabilize it with chemical substances. In addition, the concentrated contaminated water can be treated by high-pressure injection into the deep underground.
(1)水ポンプ
(2)屋外エアコンユニット
(3)熱交換器
(4)コンプレッサー
(5)ガスタンク
(6)電磁弁
(7)冷媒ガス管
(8)屋上・屋根散水
(9)夏場の高温蓄熱
(10)透水管
(11)表層管
(12)深層管
(13)電磁弁
(14)冷媒ガス管
(15)ガスタンク
(16)コンプレッサー
(17)熱交換器
(18)屋外エアコンユニット
(19)給湯
(20)水道
(21)温水タンク
(22)水ポンプ
(23)表層管
(24)A部地下
(25)透水管
(26)深層管
(1) Water pump (2) Outdoor air conditioner unit (3) Heat exchanger (4) Compressor (5) Gas tank (6) Solenoid valve (7) Refrigerant gas pipe (8) Rooftop / roof watering (9) High temperature heat storage in summer (10) Permeable pipe (11) Surface layer pipe (12) Deep layer pipe (13) Solenoid valve (14) Refrigerant gas pipe (15) Gas tank (16) Compressor (17) Heat exchanger (18) Outdoor air conditioner unit (19) Hot water supply (20) Water supply (21) Warm water tank (22) Water pump (23) Surface layer pipe (24) Part A underground (25) Permeable pipe (26) Deep layer pipe
Claims (8)
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Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN103011369A (en) * | 2013-01-22 | 2013-04-03 | 长沙创享环保科技有限公司 | Device for treating arsenic wastewater |
CN105880272A (en) * | 2016-02-22 | 2016-08-24 | 华中农业大学 | Leaching repair system for heavy metal contaminated soil |
CN111816340A (en) * | 2019-04-11 | 2020-10-23 | 北京辐安科技有限公司 | Method for pressing and removing toxic and harmful substances on hard surface |
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2008
- 2008-09-25 JP JP2008245602A patent/JP2010075816A/en active Pending
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN103011369A (en) * | 2013-01-22 | 2013-04-03 | 长沙创享环保科技有限公司 | Device for treating arsenic wastewater |
CN105880272A (en) * | 2016-02-22 | 2016-08-24 | 华中农业大学 | Leaching repair system for heavy metal contaminated soil |
CN111816340A (en) * | 2019-04-11 | 2020-10-23 | 北京辐安科技有限公司 | Method for pressing and removing toxic and harmful substances on hard surface |
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