JP2005224654A - Channel water treatment device - Google Patents
Channel water treatment device Download PDFInfo
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- JP2005224654A JP2005224654A JP2004033131A JP2004033131A JP2005224654A JP 2005224654 A JP2005224654 A JP 2005224654A JP 2004033131 A JP2004033131 A JP 2004033131A JP 2004033131 A JP2004033131 A JP 2004033131A JP 2005224654 A JP2005224654 A JP 2005224654A
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- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 18
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims abstract description 51
- 239000011941 photocatalyst Substances 0.000 claims abstract description 24
- GWEVSGVZZGPLCZ-UHFFFAOYSA-N titanium dioxide Inorganic materials O=[Ti]=O GWEVSGVZZGPLCZ-UHFFFAOYSA-N 0.000 claims description 11
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 claims description 9
- OGIDPMRJRNCKJF-UHFFFAOYSA-N titanium oxide Inorganic materials [Ti]=O OGIDPMRJRNCKJF-UHFFFAOYSA-N 0.000 claims description 6
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical class C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 claims description 5
- 238000001179 sorption measurement Methods 0.000 claims description 5
- 229920000049 Carbon (fiber) Polymers 0.000 claims description 3
- 230000002378 acidificating effect Effects 0.000 claims description 3
- 238000004438 BET method Methods 0.000 claims description 2
- 239000000126 substance Substances 0.000 abstract description 13
- 241000195493 Cryptophyta Species 0.000 abstract description 10
- 239000005416 organic matter Substances 0.000 abstract description 8
- 241000233866 Fungi Species 0.000 abstract description 7
- 239000002351 wastewater Substances 0.000 abstract description 7
- 229910052799 carbon Inorganic materials 0.000 abstract description 5
- 230000000694 effects Effects 0.000 abstract description 5
- 239000003463 adsorbent Substances 0.000 abstract description 3
- 239000000598 endocrine disruptor Substances 0.000 abstract description 2
- 238000004065 wastewater treatment Methods 0.000 abstract description 2
- 239000000463 material Substances 0.000 abstract 1
- 239000004744 fabric Substances 0.000 description 9
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 5
- 238000005516 engineering process Methods 0.000 description 5
- 238000000034 method Methods 0.000 description 5
- 229910052760 oxygen Inorganic materials 0.000 description 5
- 239000001301 oxygen Substances 0.000 description 5
- 239000000243 solution Substances 0.000 description 4
- 238000003756 stirring Methods 0.000 description 4
- RBTBFTRPCNLSDE-UHFFFAOYSA-N 3,7-bis(dimethylamino)phenothiazin-5-ium Chemical compound C1=CC(N(C)C)=CC2=[S+]C3=CC(N(C)C)=CC=C3N=C21 RBTBFTRPCNLSDE-UHFFFAOYSA-N 0.000 description 3
- 238000000354 decomposition reaction Methods 0.000 description 3
- 229960000907 methylthioninium chloride Drugs 0.000 description 3
- 230000001954 sterilising effect Effects 0.000 description 3
- 238000004659 sterilization and disinfection Methods 0.000 description 3
- 239000002253 acid Substances 0.000 description 2
- 230000004913 activation Effects 0.000 description 2
- 238000003763 carbonization Methods 0.000 description 2
- 239000003054 catalyst Substances 0.000 description 2
- 239000013078 crystal Substances 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- VUZPPFZMUPKLLV-UHFFFAOYSA-N methane;hydrate Chemical class C.O VUZPPFZMUPKLLV-UHFFFAOYSA-N 0.000 description 2
- 230000008569 process Effects 0.000 description 2
- 238000012360 testing method Methods 0.000 description 2
- 241000252229 Carassius auratus Species 0.000 description 1
- 230000009471 action Effects 0.000 description 1
- 239000003575 carbonaceous material Substances 0.000 description 1
- 125000003178 carboxy group Chemical group [H]OC(*)=O 0.000 description 1
- 238000005119 centrifugation Methods 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000010790 dilution Methods 0.000 description 1
- 239000012895 dilution Substances 0.000 description 1
- 238000006056 electrooxidation reaction Methods 0.000 description 1
- 239000000835 fiber Substances 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 238000010304 firing Methods 0.000 description 1
- 230000002070 germicidal effect Effects 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 125000002887 hydroxy group Chemical group [H]O* 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- QSHDDOUJBYECFT-UHFFFAOYSA-N mercury Chemical compound [Hg] QSHDDOUJBYECFT-UHFFFAOYSA-N 0.000 description 1
- 229910052753 mercury Inorganic materials 0.000 description 1
- 238000002715 modification method Methods 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 238000009832 plasma treatment Methods 0.000 description 1
- 239000011148 porous material Substances 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 230000009257 reactivity Effects 0.000 description 1
- 230000002787 reinforcement Effects 0.000 description 1
- 230000003014 reinforcing effect Effects 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 239000006228 supernatant Substances 0.000 description 1
- 238000010998 test method Methods 0.000 description 1
- 239000010409 thin film Substances 0.000 description 1
- 239000004408 titanium dioxide Substances 0.000 description 1
Images
Classifications
-
- 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
Abstract
Description
本発明は、活性炭吸着材に光触媒を担持した水処理装置に関するものである。 The present invention relates to a water treatment apparatus in which a photocatalyst is supported on an activated carbon adsorbent.
従来、排水中の被処理物質を処理する技術としては濾過、遠心分離などの分離技術が主である。一方、分解技術としては現在多くの要素技術が提案されている。 Conventionally, separation techniques such as filtration and centrifugation are mainly used as techniques for treating a substance to be treated in waste water. On the other hand, many elemental technologies have been proposed as decomposition technologies.
近年、排水中の微量な有害有機物が、環境に排出され問題となっている。現在、これらを分解する要素技術として光触媒が提案されているが、紫外線領域で作動する為・光源のエネルギーが一部しか使用されず効率が悪く、且つ撹絆装置を具備する為コストが高くなり有効な技術は実用化されていない。
例えば振動撹搾翼を使用した排水中の菌類を処理する技術として滅菌用振動撹絆装置があ乱この方法は光源を具備し、光触媒を翼に付着させた振動撹搾装置との組み合わせによる滅菌を目的としている。この装置を菌の滅菌装置として使用した場合、1ppm以上の負荷の排水中では処理が充分ではなく、又光源及び、撹絆に要する動カ費と初期費用が高価になる欠点がある。 For example, as a technique for treating fungi in wastewater using a vibration stirring blade, there is a disturbance of a vibration sterilization device for sterilization. This method is equipped with a light source and sterilized by a combination with a vibration stirring device in which a photocatalyst is attached to the blade. It is an object. When this apparatus is used as a germicidal sterilization apparatus, the treatment is not sufficient in drainage with a load of 1 ppm or more, and there are disadvantages that the light source and the dynamic and initial costs required for stirring are expensive.
本発明の課題は、藻等の菌類及び内分泌撹乱化学物質等の微量有機物を分解する排水処理装置において、光触媒が水路の動圧又は水頭圧によって回転し、排水中の有機物と効果的に接触でき、有機物が高活性な光触媒担持活性炭表面まで送り込まれる事によって吸着・分解され、分解物質は速やかに活性炭表面を離れる事によって表面に蓄積・付着しない。活性炭吸着材の機能を光触媒により回復させ長期間機能を保持でき、5ppmから10ppmの比較的負荷の大きな排水においても効果を発揮でき、且つ光触媒担持活性炭が水路の動圧又は水頭圧によって回転するため、回転駆動装置を必要とせず、可視光と人工光源からの光エネルギーを効果的に吸収できる事を特徴とする水路水処理装置を提供する。 The problem of the present invention is that, in a wastewater treatment apparatus that decomposes trace organic substances such as fungi such as algae and endocrine disrupting chemical substances, the photocatalyst rotates due to the dynamic pressure of the water channel or the head pressure of the water, and can effectively contact the organic matter in the wastewater. The organic matter is adsorbed and decomposed by being sent to the surface of the activated carbon supporting the highly active photocatalyst, and the decomposed substance does not accumulate or adhere to the surface by leaving the activated carbon surface quickly. Because the function of the activated carbon adsorbent is restored by the photocatalyst, the function can be maintained for a long time, and the effect can be exerted even in drainage with a relatively large load of 5 ppm to 10 ppm, and the photocatalyst-supported activated carbon rotates due to the dynamic pressure of the water channel or the head pressure. An aqueduct water treatment device characterized in that it can effectively absorb light energy from visible light and an artificial light source without requiring a rotary drive device.
以下に本発明にかかる課題を解決する為の手段を説明する。 Means for solving the problems according to the present invention will be described below.
水路中に多段に配置され流水の水頭圧差、及び/又は動圧によって回転する補強された枠に貼られた活性炭繊維を担体とする高活性な光触媒と夜間又は光エネルギー不足時に点灯する光源により有機物は光エネルギーが与えられない時間は吸着され、また光エネルギーが与えられた時間は分解が促進される安価な水路水処理装置において、水路堰部の落水によるエネルギー、又は水路の流れによる動圧を利用して回転できる。補強されたプレート状の羽根が複数取付けられ羽根部に活性炭繊維に酸化チタン溶液を塗布し焼成された可視光下で作動する高活性な光触媒担持活性炭繊維布を取リつけた回転体の上部に光触媒を励起する光源を配置し、光源は光触媒を励起するに必要な太陽光エネルギーが存在する時間は消灯され、夜間又は太陽光エネルギーが不足する場合は点灯される機構を持ち、回転体に取付けられた活性炭繊維布が光の届かない水中、又は日陰部に入った時間は有機物が吸着され、光エネルギーを十分受けることができる位置に移動した時には光触媒表面の活性酸素種による酸化還元作用により有機物が分解され、多段に設置された回転体により順次分解が促進され無害化されて排出される。光源は高圧水銀ランプ等の波長350nmで以上のものが良く、350nmから450nmの範囲に多くのエネルギーを放出する物が望ましい。特に熱損失が少なく波長を特定できる発光ダイオードが望ましい。 Organic matter with a highly active photocatalyst using activated carbon fibers supported on a reinforced frame that is arranged in multiple stages in the water channel and rotated by the head pressure difference and / or dynamic pressure of running water and a light source that lights at night or when light energy is insufficient In an inexpensive water treatment system where light energy is adsorbed during the time when light energy is not applied and decomposition is promoted during the time when light energy is applied, the energy due to falling water in the water channel weir or the dynamic pressure due to the flow of the water channel is reduced. Can be rotated using. A plurality of reinforced plate-like blades are attached, and a titanium oxide solution is applied to the activated carbon fibers on the blades and baked. A highly active photocatalyst-supported activated carbon fiber cloth that operates under visible light is attached to the upper part of the rotating body. A light source that excites the photocatalyst is arranged, and the light source is turned off when the solar energy necessary to excite the photocatalyst is present, and is turned on at night or when the solar energy is insufficient, and is attached to the rotating body. When the activated carbon fiber cloth is moved to a position where it can move to a position where it can absorb enough light energy when it enters water or in the shaded area where light does not reach, the organic substance is oxidized by the redox action of the active oxygen species on the surface of the photocatalyst. Are decomposed, and the decomposition is sequentially promoted and made harmless by the rotating bodies installed in multiple stages. The light source is preferably a high pressure mercury lamp or the like having a wavelength of 350 nm or more, and preferably emits a lot of energy in the range of 350 nm to 450 nm. In particular, a light emitting diode that can specify a wavelength with little heat loss is desirable.
光触媒の作成は、活性炭繊維布担体を酸化チタン溶液に5秒から1時間、浸漬する。酸化チタン溶液はサステナブルテクノロジー社製のものを使用した。その後、自然乾燥し真空下において900℃から1300℃の範囲で4.5時間から21時間焼成すると表面に酸化チタンの薄膜が形成される。昇温・降温速度は50℃/時間から200℃/時間の範囲であり、最高温度に達した時点で5分から3時間保持することが望ましい。この製造方法によリ酸化チタン結晶体はルチル型となり繊維状活性炭に担持しやすくなり、また真空で焼成する事により酸素欠陥が生じたと恩われる結晶構造の活性点が、可視光域で活性化する。 For preparation of the photocatalyst, the activated carbon fiber cloth carrier is immersed in the titanium oxide solution for 5 seconds to 1 hour. A titanium oxide solution manufactured by Sustainable Technology was used. Thereafter, it is naturally dried and fired in the range of 900 ° C. to 1300 ° C. for 4.5 hours to 21 hours under vacuum to form a titanium oxide thin film on the surface. The temperature increase / decrease rate is in the range of 50 ° C./hour to 200 ° C./hour, and it is desirable to hold the temperature for 5 minutes to 3 hours when the maximum temperature is reached. With this manufacturing method, the titanium dioxide crystal becomes rutile and can be easily supported on fibrous activated carbon, and the active site of the crystal structure, which is said to have oxygen defects caused by firing in vacuum, is activated in the visible light range. To do.
本発明の活性炭繊維担体は、繊維状活性炭原料編物を350℃以上1300℃以下の温度の不活性雰囲気で炭化し、次いで500℃以上1300℃以下の温度で炭素と反応する水蒸気、酸素、二酸化炭素などを含む活性な雰囲気で賦活し活性炭化したものが好適に利用可能である。又、場合によっては雰囲気条件を制御することにより炭化と賦活を同時に行うことも可能である。尚、賦活処理、すなわち活性炭化を行う際の最高到達温度を1300℃以上にすると重量収率が著しく減少するため、最高到違温度は1300℃以下にすることが好ましい。これにより、比表面積が1000〜3000m2/gである編物状の繊維状活性炭が得られる。該活性炭編物の吸着性能としてはJlSK1477「繊維状活性炭試験方法」の5.7項に記載のトルエン吸着性能で30g/m2以上(25℃、1/10希釈の条件下〕、好ましくは40g/m2以上必要である。この吸着量を下回る場合は、触媒の担持量が不足し、性能を十分発揮できなくなる。BET法による比表面積はトルエン吸着性能と相関があるが、1000〜3000h/g必要である。1000m2/g以下であると、触媒の担持量が不足し、性能を十分発揮できなくなリ、3000m2/g以上であると繊維の比重が著しく低下し、編物の形態を保持できない。 The activated carbon fiber carrier of the present invention carbonizes a fibrous activated carbon raw material knitted fabric in an inert atmosphere at a temperature of 350 ° C. or higher and 1300 ° C. or lower, and then reacts with carbon at a temperature of 500 ° C. or higher and 1300 ° C. or lower. Those activated and carbonized in an active atmosphere containing the above can be suitably used. In some cases, carbonization and activation can be performed simultaneously by controlling the atmospheric conditions. In addition, since the weight yield will be remarkably reduced if the maximum reached temperature in activation treatment, that is, activated carbonization, is 1300 ° C. or higher, it is preferable to set the maximum reaching temperature to 1300 ° C. or lower. Thereby, a knitted fibrous activated carbon having a specific surface area of 1000 to 3000 m 2 / g is obtained. The adsorption performance of the activated carbon knitted fabric is 30 g / m 2 or more (at 25 ° C., 1/10 dilution condition), preferably 40 g / m 2 in terms of the toluene adsorption performance described in paragraph 5.7 of JlSK1477 “Fibrous activated carbon test method”. m is required 2 or more. If below this adsorption amount, the amount of supported catalyst is insufficient, although the specific surface area by the .BET method can not be sufficiently exhibited performance correlates with toluene adsorption performance, 1000~3000h / g If it is 1000 m 2 / g or less, the supported amount of the catalyst is insufficient, and the performance cannot be sufficiently exhibited. If it is 3000 m 2 / g or more, the specific gravity of the fiber is remarkably lowered, and the shape of the knitted fabric is reduced. I can't hold it.
本発明に最適な親水性のある繊維状活性炭素の表面改質方法として、例えば、1×10-2torr以上の酸素分圧を有する酸素雰囲気下で重量収率にして65〜99%の範囲になるように実施する。処理温度は300〜700℃が好ましい。低温では処理する炭素材料の反応性が落ちるため、酸化の効果が得られない。また高温では表面に水酸基やカルボキシル基などの親水基が付与できない。強酸や電気酸化などによる湿式処理、プラズマ処理でも同様な効果を得ることができる。これにより、全酸性基量が0.1meq/g以上である親水性のある繊維状活性炭素を得ることができ、6meq/g以下であることが望ましい。好ましくは全酸性基量0.2meq/g〜3meq/gの範囲である。 As a surface modification method for hydrophilic activated carbon having hydrophilicity suitable for the present invention, for example, a weight yield in the range of 65 to 99% in an oxygen atmosphere having an oxygen partial pressure of 1 × 10 −2 torr or more. We carry out to become. The treatment temperature is preferably 300 to 700 ° C. At low temperatures, the reactivity of the carbon material to be treated falls, so that the oxidation effect cannot be obtained. Further, at high temperatures, hydrophilic groups such as hydroxyl groups and carboxyl groups cannot be imparted to the surface. The same effect can be obtained by wet treatment using strong acid or electro-oxidation, or plasma treatment. As a result, a hydrophilic fibrous activated carbon having a total acidic group amount of 0.1 meq / g or more can be obtained, and is preferably 6 meq / g or less. Preferably, the total acidic group amount is in the range of 0.2 meq / g to 3 meq / g.
以上のように、本発明によれば、可視光下で微量有機物を効果的に吸着分解できるとともに、藻のような菌類を抑制でき,安価に水環境を改善することができる。 As described above, according to the present invention, trace organic substances can be effectively adsorbed and decomposed under visible light, fungi such as algae can be suppressed, and the water environment can be improved at low cost.
以下本発明の実施例を添付の図1に示し説明する。流路4に拡散した濃度10mg/L以下の有機物質や藻等の菌類を分解処理する装置として、水路4に設置された複数の補強枠に取付けられた光触媒担持繊維状活性炭水処理装置1は堰2から溢流する排水の水頭圧及び流路を流れる水の動圧によって中心に通した軸3の廻りを回転する。光触媒担持繊維状活性炭水処理装置1の上部には紫外線を発生する光源3を配置し光源は光触媒が可視光で作動する時間は消灯し、夜間及び光触媒の作動エネルギーが不足する場合は自動的に点灯する装置6を有し、水路を通る排水中の微量有機物は活性炭細孔に吸着されると同時に担持された光触媒によって光触媒表面に発生するヒドロキシラジカルと活性酸素種により、酸化・還元され無害化されて環境へ排出される。
An embodiment of the present invention will be described below with reference to FIG. A photocatalyst-supporting fibrous activated carbon
[実施例1]
図1の装置で、幅5cmの流路に濃度10ppmのメチレンブルー液500mLを入れ、全酸性基量1.0meq/g,1300m2/gの繊維状活性炭編物にルチル型酸化チタンを担持した光触媒を合計表面積約240cm2取付け、可視光下で2時間循環させた結果、メチレンブルー濃度が1/15(6.7%)に減少した。
一方、同じ装置で光触媒を担持しない同一表面積の繊維状活性炭編物によるテストを行った結果、2時間後にメチレンブルー濃度が1/4.0(25%)に減少した。
[実施例2]
図1の装置で、幅5cmの流路に藻が発生した金魚水槽の上澄み液を入れ、実施例1同様の繊維状活性炭編物光触媒を合計表面積約240cm2取付け、2週間循環させた結果、藻は発生しなかった。一方、同じ装置で光触媒を担持しない同一表面積の繊維状活性炭編物によるテストの場合は3日後に藻の発生が見受けられた。
[Example 1]
In the apparatus shown in FIG. 1, 500 mL of methylene blue solution having a concentration of 10 ppm is put into a channel having a width of 5 cm, and a photocatalyst in which rutile titanium oxide is supported on a fibrous activated carbon knitted fabric having total acid group amounts of 1.0 meq / g and 1300 m 2 / g. As a result of attaching a total surface area of about 240 cm 2 and circulating under visible light for 2 hours, the concentration of methylene blue was reduced to 1/15 (6.7%).
On the other hand, as a result of testing with a fibrous activated carbon knitted fabric having the same surface area that does not carry a photocatalyst in the same apparatus, the methylene blue concentration decreased to 1/4 (25%) after 2 hours.
[Example 2]
In the apparatus of FIG. 1, the supernatant of a goldfish tank in which algae was generated was put into a channel having a width of 5 cm, and a fibrous activated carbon knitted photocatalyst similar to Example 1 was attached to a total surface area of about 240 cm 2 and circulated for 2 weeks. Did not occur. On the other hand, in the case of a test using the same surface area fibrous activated carbon knitted fabric that does not carry a photocatalyst in the same apparatus, generation of algae was observed after 3 days.
以上のように、本発明によれば、可視光下で微量有機物を効果的に吸着分解できるとともに、藻のような菌類を抑制でき,安価に水環境を改善することができ工業的に有効に利用可能である。 As described above, according to the present invention, trace organic substances can be effectively adsorbed and decomposed under visible light, fungi such as algae can be suppressed, the water environment can be improved at low cost, and industrially effective. Is available.
1:光触媒担持繊維状活性炭
2:堰
3:光源
4:水路
5:軸
6:自動点灯装置
1: Photocatalyst carrying fibrous activated carbon 2: Weir 3: Light source 4: Water channel 5: Shaft 6: Automatic lighting device
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Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB2445792A (en) * | 2007-01-18 | 2008-07-23 | Malcolm Robert Snowball | Photocatalytic fluid treatment |
CN114314792A (en) * | 2021-11-25 | 2022-04-12 | 合肥供水集团有限公司 | Full-automatic dechlorinating device for high-chlorine-content wastewater treatment |
-
2004
- 2004-02-10 JP JP2004033131A patent/JP2005224654A/en active Pending
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB2445792A (en) * | 2007-01-18 | 2008-07-23 | Malcolm Robert Snowball | Photocatalytic fluid treatment |
CN114314792A (en) * | 2021-11-25 | 2022-04-12 | 合肥供水集团有限公司 | Full-automatic dechlorinating device for high-chlorine-content wastewater treatment |
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