JPH047090A - Apparatus for simultaneous sterilizing, degassing and adsorbing/filtering treatments of water - Google Patents
Apparatus for simultaneous sterilizing, degassing and adsorbing/filtering treatments of waterInfo
- Publication number
- JPH047090A JPH047090A JP2107079A JP10707990A JPH047090A JP H047090 A JPH047090 A JP H047090A JP 2107079 A JP2107079 A JP 2107079A JP 10707990 A JP10707990 A JP 10707990A JP H047090 A JPH047090 A JP H047090A
- Authority
- JP
- Japan
- Prior art keywords
- water
- degassing
- treatment
- gas
- ozone
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 38
- 238000007872 degassing Methods 0.000 title claims abstract description 29
- 238000011282 treatment Methods 0.000 title claims abstract description 22
- 238000001914 filtration Methods 0.000 title claims abstract description 17
- 230000001954 sterilising effect Effects 0.000 title claims abstract description 15
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 claims abstract description 29
- 239000007789 gas Substances 0.000 claims abstract description 21
- 238000000354 decomposition reaction Methods 0.000 claims abstract description 11
- 238000006864 oxidative decomposition reaction Methods 0.000 claims abstract description 11
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 claims abstract description 10
- 239000000460 chlorine Substances 0.000 claims abstract description 10
- 229910052801 chlorine Inorganic materials 0.000 claims abstract description 10
- 238000001179 sorption measurement Methods 0.000 claims description 16
- 239000003960 organic solvent Substances 0.000 claims description 12
- 239000000126 substance Substances 0.000 claims description 11
- 238000004659 sterilization and disinfection Methods 0.000 claims description 10
- 230000003647 oxidation Effects 0.000 claims description 6
- 238000007254 oxidation reaction Methods 0.000 claims description 6
- 239000005416 organic matter Substances 0.000 claims description 5
- 235000019645 odor Nutrition 0.000 claims description 4
- 239000012528 membrane Substances 0.000 claims description 3
- 239000000203 mixture Substances 0.000 claims description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims 2
- MYMOFIZGZYHOMD-UHFFFAOYSA-N Dioxygen Chemical compound O=O MYMOFIZGZYHOMD-UHFFFAOYSA-N 0.000 claims 2
- 229910001882 dioxygen Inorganic materials 0.000 claims 2
- KZBUYRJDOAKODT-UHFFFAOYSA-N Chlorine Chemical compound ClCl KZBUYRJDOAKODT-UHFFFAOYSA-N 0.000 claims 1
- 230000003197 catalytic effect Effects 0.000 claims 1
- 238000001704 evaporation Methods 0.000 claims 1
- JEIPFZHSYJVQDO-UHFFFAOYSA-N iron(III) oxide Inorganic materials O=[Fe]O[Fe]=O JEIPFZHSYJVQDO-UHFFFAOYSA-N 0.000 abstract description 5
- 238000002347 injection Methods 0.000 abstract description 3
- 239000007924 injection Substances 0.000 abstract description 3
- 238000007539 photo-oxidation reaction Methods 0.000 abstract description 2
- 230000000274 adsorptive effect Effects 0.000 abstract 2
- 239000002131 composite material Substances 0.000 abstract 1
- 238000013329 compounding Methods 0.000 abstract 1
- 238000004134 energy conservation Methods 0.000 abstract 1
- 239000002904 solvent Substances 0.000 abstract 1
- 238000000746 purification Methods 0.000 description 6
- 238000000034 method Methods 0.000 description 4
- 230000002265 prevention Effects 0.000 description 4
- 238000001816 cooling Methods 0.000 description 3
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 238000012423 maintenance Methods 0.000 description 2
- 238000003756 stirring Methods 0.000 description 2
- 241000195493 Cryptophyta Species 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 239000000498 cooling water Substances 0.000 description 1
- 238000005536 corrosion prevention Methods 0.000 description 1
- 239000002173 cutting fluid Substances 0.000 description 1
- 238000005520 cutting process Methods 0.000 description 1
- 238000004332 deodorization Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000035622 drinking Effects 0.000 description 1
- 239000003651 drinking water Substances 0.000 description 1
- 235000020188 drinking water Nutrition 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000000284 extract Substances 0.000 description 1
- 239000010800 human waste Substances 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- 230000001678 irradiating effect Effects 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 238000000465 moulding Methods 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 230000001737 promoting effect Effects 0.000 description 1
- 235000014214 soft drink Nutrition 0.000 description 1
- 231100000331 toxic Toxicity 0.000 description 1
- 230000002588 toxic effect Effects 0.000 description 1
- 238000009849 vacuum degassing Methods 0.000 description 1
Landscapes
- Physical Water Treatments (AREA)
- Treatment Of Water By Oxidation Or Reduction (AREA)
- Water Treatment By Sorption (AREA)
Abstract
Description
【発明の詳細な説明】
[産業上の利用分野]
本発明は、水中の有機物、遊離塩素、有機溶剤、等の異
物を、殺菌、酸化、分解、脱臭、種々の脱ガス、吸着濾
過、等を複合同時処理する装置で、ボイラー用水の防錆
・スケールの除去・浄化、クーリングタワー用冷却循環
水の殺菌・防錆・防藻・浄化、受水槽・高置水槽におけ
る飲料用水の殺菌浄化と配管系統の防錆・スケールの除
去、金属切削油の防腐・浄化等に関するものである。[Detailed Description of the Invention] [Industrial Application Field] The present invention removes foreign substances such as organic substances, free chlorine, and organic solvents from water by sterilization, oxidation, decomposition, deodorization, various degassing, adsorption filtration, etc. It is a device that performs multiple simultaneous treatments for rust prevention, scale removal, and purification of boiler water, sterilization, rust prevention, algae prevention, and purification of cooling circulating water for cooling towers, sterilization and purification of drinking water in water receiving tanks and elevated water tanks, and piping. Concerns rust prevention and scale removal from systems, corrosion prevention and purification of metal cutting fluids, etc.
[従来の技術]
用水の殺菌・脱ガス・濾過等の浄化装置は種々開発され
てきているが、各々の処理機能が独立した装置で、別々
に処理するため、処理工程が繁雑で、取扱い、保守に苦
慮していた。[Prior Art] Various purification devices for water sterilization, degassing, filtration, etc. have been developed, but each treatment function is an independent device and is processed separately, making the treatment process complicated and difficult to handle. Maintenance was a concern.
なかでも、有機物、遊離塩素等、異物の酸化分解は、高
度処理と称してオゾン酸化だけで解決しようとしている
ため膨大なオゾン量を必要とし、余剰オゾンは毒性なの
で廃棄方法が聞届となっている、また脱ガス技術に関し
ては、機能膜を使って真空ポンプで脱ガスする装置は、
機能膜の目詰まりをおこし保守が大変、又は吸い込み力
の強いポンプを使っての単純脱ガス装置、は脱ガス速度
が遅く、単位エネルギー当たりの脱ガス量が少なすぎる
、等難問題ばかりである。Among these, the oxidative decomposition of foreign substances such as organic matter and free chlorine is attempted to be solved by ozone oxidation alone, which is called advanced treatment, so a huge amount of ozone is required, and the surplus ozone is toxic, so the disposal method is unknown. Regarding degassing technology, there is a device that uses a functional membrane to degas with a vacuum pump.
Simple degassing devices that use pumps with strong suction force have many problems, such as clogging of the functional membrane, which makes maintenance difficult, and simple degassing devices using pumps with strong suction power, which have a slow degassing rate and too little amount of degassing per unit energy.
[発明が解決しようする課題]
本発明は以上の事項に鑑み開発したもので、用水中の有
機物、遊離塩素、有機溶剤等の異物とオゾンを撹拌反応
させたうえ、紫外線を照射することにより、強制的に酸
化分解反応を促進させ、つぎに高真空容器内で高速酸化
分解と脱ガス、吸着濾過を複合同時処理することにより
、有機物、遊離塩素、有機溶剤等の分解能力と脱ガス量
を倍増する、また取扱いが簡単、装置がコンパクト化さ
れ、省スペース、省工効率の高い複合処理装置を提供す
ることを目的としたものである。[Problems to be Solved by the Invention] The present invention was developed in view of the above-mentioned matters, and by stirring and reacting ozone with foreign substances such as organic substances, free chlorine, and organic solvents in water, and then irradiating it with ultraviolet rays, By forcibly promoting the oxidative decomposition reaction, and then performing a combined simultaneous process of high-speed oxidative decomposition, degassing, and adsorption filtration in a high-vacuum container, the decomposition ability and degassing amount of organic substances, free chlorine, organic solvents, etc. can be improved. The purpose of the present invention is to provide a multi-processing device that is easy to handle, compact, space-saving, and has high labor-saving efficiency.
[課題を解決するための手段]
本発明の構成について図面に基づいて説明すると、第1
図において、紫外線ランプ4、またはオゾン発生装置1
4で発生させたオゾンと処理用水を撹拌混合し、4の紫
外線ランプで紫外線照射し、真空性の高い脱ガス吸着濾
過槽1に用水を吸引導入、オゾンと用水中の何機物、遊
離塩素、有機溶剤等を高真空中で強制酸化分解反応をさ
せる、と同時に用水中の種々の溶解性ガスを真空ポンプ
7で抜き取る高速酸化分解反応脱ガス装置、と吸着濾過
フィルター2を同一槽内に、それぞれ、高速オゾン紫外
線照射酸化分解反応処理、脱ガス処理、吸着濾過処理、
を殆ど同時に行えるように直列に、同一装置内に収納し
てなるものである。[Means for Solving the Problems] The configuration of the present invention will be explained based on the drawings.
In the figure, an ultraviolet lamp 4 or an ozone generator 1
Stir and mix the ozone generated in step 4 and the treatment water, irradiate it with ultraviolet light using the ultraviolet lamp in step 4, and suck and introduce the water into the highly vacuum degassing adsorption filter tank 1. , a high-speed oxidation decomposition reaction degassing device that performs a forced oxidation decomposition reaction of organic solvents etc. in a high vacuum and at the same time extracts various soluble gases from the water using a vacuum pump 7, and an adsorption filtration filter 2 in the same tank. , high-speed ozone ultraviolet irradiation oxidation decomposition reaction treatment, degassing treatment, adsorption filtration treatment, respectively.
They are housed in series in the same device so that they can be performed almost simultaneously.
[作用]
本発明は以上のような構成で、これが使用に際しては、
用水中の有機物、遊離塩素、有機溶剤等、異物の酸化分
解を段階別に複合同時処理することにより、酸化分解能
力が大になった、オゾンガスを第1図に指定する位置か
ら注入することにより、脱ガス、特に溶存酸素量の除去
が第2図のグラフに示すごとく迅速化した、また第1処
理と第2処理、第3処理の脱ガス複合同時処理により第
1図、2の吸着濾過フィルターの寿命が数倍延長された
ため、ランニングコストの低減、装置そのものを小さく
することが出来、設置スペースが激減、そのうえオゾン
混合・脱ガスによる殺菌、と紫外線殺菌の同時処理によ
り、殺菌効果が強力でかつ有効に作用する。[Function] The present invention has the above configuration, and when it is used,
By injecting ozone gas from the position specified in Figure 1, the oxidative decomposition capacity has been increased by performing multiple simultaneous oxidative decomposition processes for foreign substances such as organic matter, free chlorine, and organic solvents in water. Degassing, especially removal of dissolved oxygen amount, has been accelerated as shown in the graph in Figure 2, and the adsorption filtration filter shown in Figures 1 and 2 has been improved by the combined simultaneous degassing treatment of the 1st, 2nd, and 3rd treatments. The lifespan of the product has been extended several times, reducing running costs, making the device itself smaller, and drastically reducing the installation space.Furthermore, the simultaneous sterilization by ozone mixing/degassing and ultraviolet sterilization has a strong sterilizing effect. and works effectively.
[実施例]
次に本発明の実施例について、第1図に基づいて説明す
る。[Example] Next, an example of the present invention will be described based on FIG.
4の紫外線ランプ又は14のオゾン発生装置で発生させ
たオゾンガスを、3のオゾン注入装置で混合吸引、6の
用水中の有機物、遊離塩素、有機溶剤等と、紫外線照射
部5で高速殺菌光酸化分解反応をさせ、脱ガス吸着濾過
槽1 (真空度60Torr〜20Torr)に吸引導
入、減圧下で有機物の酸化分解を行い、同時に種々の溶
解性ガスを真空ポンプ7で脱ガス除去、2の成型された
濾過吸着フィルタで、分解有機物、臭気等を吸着濾過し
、11のラインポンプをへて、lOに至る。また9の水
位は8のポールタップで調節する。The ozone gas generated by the ultraviolet lamp (4) or the ozone generator (14) is mixed and sucked by the ozone injection device (3), and the organic matter, free chlorine, organic solvent, etc. in the water (6) is subjected to high-speed sterilization photooxidation in the ultraviolet irradiation unit 5. A decomposition reaction is carried out, and the degassing is introduced into a degassing adsorption filtration tank 1 (vacuum level 60 Torr to 20 Torr), oxidative decomposition of organic matter is carried out under reduced pressure, various soluble gases are simultaneously degassed and removed by a vacuum pump 7, and the molding of 2 is carried out. Decomposed organic substances, odors, etc. are adsorbed and filtered by the filtration/adsorption filter, which passes through line pump 11 and reaches lO. Also, the water level at 9 is adjusted using the pole tap at 8.
以」二のように6から入った用水はオゾンと紫外線によ
る殺菌光酸化分解、脱ガス、濾過吸着、を瞬時に行い1
0に至る。As shown in 2 above, the water entering from 6 is instantly subjected to sterilization, photooxidative decomposition, degassing, filtration and adsorption using ozone and ultraviolet rays.
It reaches 0.
[発明の効果1
本発明は、以上のような構成であるから、俗に言う高度
処理殺菌浄化と、脱ガス装置、等を複合化したことによ
り用水配管ラインのスケール付着、赤錆発生の防止装置
となり、ビル、マン/フン等の受水槽、高置水槽に、ボ
イラー用水に、クーリングタワー用冷却水に、飲料用地
下水の鉄分・有機溶剤等の除去、清涼飲料水用の原料水
製造、機械切削用液、等利用分野はかなり広い。[Effects of the Invention 1] Since the present invention has the above-described configuration, it is a device for preventing scale adhesion and red rust on water piping lines by combining what is commonly called advanced treatment sterilization and purification, a degassing device, etc. It is used for water tanks for buildings, people/human waste, etc., elevated water tanks, water for boilers, cooling water for cooling towers, removal of iron and organic solvents from drinking underground water, production of raw water for soft drinks, and mechanical cutting. It can be used in a wide range of fields such as liquids, etc.
第1図、は本発明の1実施例の使用状況を示す説明的フ
ロー図。
1・脱ガス吸着濾過槽2・吸着濾過フィルター3・オゾ
ン注入装置 4・紫外線ランプ5・紫外線照射筒 6
・用液槽
7・真空ポンプ 8・ボールタ、フ9・水位
IO・処理水
11・ラインポンプ 12−水・排オゾン吸着筒1
3・用水補充 14・オゾン発生装置第2図、は
オゾンガス注入した場合とオゾンガスを注入しない場合
との脱ガス速度差グラフ。
l・オゾンガス注入した時の脱ガス速度グラフ2・オゾ
ンガス注入しなかった時の脱ガス速度グラフFIG. 1 is an explanatory flow diagram illustrating the use of one embodiment of the present invention. 1. Degassing adsorption filtration tank 2. Adsorption filtration filter 3. Ozone injection device 4. Ultraviolet lamp 5. Ultraviolet irradiation tube 6
・Liquid tank 7・Vacuum pump 8・Vaulter, fan 9・Water level
IO/treated water 11/line pump 12-water/exhaust ozone adsorption cylinder 1
3. Water replenishment 14. Ozone generator Figure 2 is a graph of the difference in degassing speed between when ozone gas is injected and when ozone gas is not injected. l・Degassing speed graph when ozone gas is injected 2・Degassing speed graph when ozone gas is not injected
Claims (1)
し、用水中の有機物、遊離塩素、有機溶剤等と接触酸化
分解反応をさせる。 第2処理、第1処理した用水中の有機物、遊離塩素、有
機溶剤、等とオゾンガスの混合物に紫外線を照射するこ
とにより、強制殺菌光酸化分解反応を向上させる。 第3処理、減圧容器内(真空度60Torr〜20To
rr)に、第2処理した用水を吸引導入し酸化分解反応
を完全にならしめ、高真空ポンプで、連続して水中の分
解有機物ガス、塩素ガス、有機溶剤ガス、酸素ガス、等
種々の脱ガスを行う、特に遊離塩素量を半減させる。 第4処理、成型された適宜の吸着濾過フィルターを装着
し分解残留物(有機溶剤等の異物)、臭気等を吸着濾過
する。 第1処理から第4処理までの処理工程を同一装置内に収
納、併設複合同時処理することを特徴とする、高速殺菌
有機物酸化分解・脱ガス・吸着濾過・同時処理装置。 2)オゾンガスを第1図に示す位置から紫外線照射筒を
へて、減圧容器内に吸引注入することにより脱ガス(特
に脱酸素)能力を倍増させることを特徴とする請求項1
記載の装置。 3)減圧容器内で蒸発する蒸気、残留しているオゾンガ
ス、分解有機物ガス、酸素ガス、有機溶剤ガス、臭気等
を高真空ポンプで吸引排気する際、高真空ポンプに至る
手前で、外皮にガスは通すが用水は通さない機能膜で、
蒸気、用水、の排出阻止をはかり、内側には適宜に成型
された活性炭フィルターを装着することにより、オゾン
ガスの吸着、臭気の吸着、を一挙に処理することを特徴
とする請求項1記載の装置。[Claims] 1) First treatment: A predetermined amount of ozone gas is injected and stirred into the service water to cause a catalytic oxidative decomposition reaction with organic substances, free chlorine, organic solvents, etc. in the service water. In the second treatment, the mixture of organic matter, free chlorine, organic solvent, etc. and ozone gas in the first treated water is irradiated with ultraviolet rays to improve the forced sterilization photooxidative decomposition reaction. Third treatment, inside the vacuum container (vacuum degree 60 Torr ~ 20To
rr), the second treated water is suctioned into the water to complete the oxidative decomposition reaction, and a high vacuum pump is used to continuously remove various decomposed organic gases, chlorine gas, organic solvent gas, oxygen gas, etc. from the water. Gas, especially to reduce the amount of free chlorine by half. Fourth treatment: A suitable molded adsorption filtration filter is attached to adsorb and filter decomposition residues (foreign substances such as organic solvents), odors, and the like. A high-speed sterilizing organic substance oxidation decomposition/degassing/adsorption filtration/simultaneous processing device characterized by storing the processing steps from the first treatment to the fourth treatment in the same device and performing combined simultaneous processing. 2) Claim 1 characterized in that the degassing (especially deoxidizing) ability is doubled by suctioning and injecting ozone gas from the position shown in FIG. 1 through the ultraviolet irradiation tube into the reduced pressure container.
The device described. 3) When evaporating steam, residual ozone gas, decomposed organic gas, oxygen gas, organic solvent gas, odor, etc. in the vacuum container is sucked and exhausted with a high vacuum pump, the gas is removed from the outer skin before reaching the high vacuum pump. A functional membrane that allows water to pass through but not water.
2. The apparatus according to claim 1, wherein the apparatus prevents the discharge of steam and water, and is equipped with an appropriately molded activated carbon filter on the inside, thereby simultaneously treating ozone gas adsorption and odor adsorption. .
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2107079A JPH047090A (en) | 1990-04-23 | 1990-04-23 | Apparatus for simultaneous sterilizing, degassing and adsorbing/filtering treatments of water |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2107079A JPH047090A (en) | 1990-04-23 | 1990-04-23 | Apparatus for simultaneous sterilizing, degassing and adsorbing/filtering treatments of water |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH047090A true JPH047090A (en) | 1992-01-10 |
Family
ID=14449949
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP2107079A Pending JPH047090A (en) | 1990-04-23 | 1990-04-23 | Apparatus for simultaneous sterilizing, degassing and adsorbing/filtering treatments of water |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH047090A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR100802158B1 (en) * | 2007-02-16 | 2008-02-13 | 하순식 | The fire-fighting coupling and fire-fighting system using it |
US7531096B2 (en) * | 2005-12-07 | 2009-05-12 | Arizona Public Service Company | System and method of reducing organic contaminants in feed water |
-
1990
- 1990-04-23 JP JP2107079A patent/JPH047090A/en active Pending
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US7531096B2 (en) * | 2005-12-07 | 2009-05-12 | Arizona Public Service Company | System and method of reducing organic contaminants in feed water |
KR100802158B1 (en) * | 2007-02-16 | 2008-02-13 | 하순식 | The fire-fighting coupling and fire-fighting system using it |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US7462288B2 (en) | Ozone/UV combination for the decomposition of endocrine substances | |
JP3440313B2 (en) | Method and apparatus for treating contaminated water | |
CN101386461A (en) | Processing system for implementing coking waste water reuse and processing method | |
CN104649491A (en) | Process and equipment for catalytic oxidation of industrial wastewater | |
CN108434958A (en) | A kind of sludge workshop foul gas advanced treatment device and its treatment process | |
CN101638263A (en) | High-efficiency ozone sewage sterilization system | |
JPH047090A (en) | Apparatus for simultaneous sterilizing, degassing and adsorbing/filtering treatments of water | |
CN209307099U (en) | A kind of Medical Wastewater Disposal System | |
CN103214133B (en) | Graphene sewage purification combined device and sewage purification method thereof | |
NL2026394B1 (en) | Wastewater ozone treatment | |
CN103951141A (en) | Garbage leachate treatment process and device | |
CN210683408U (en) | Chemical sewage and waste gas purification treatment device | |
JPH03143584A (en) | Simultaneously treating device for deaeration, filtration, adsorption and sterilization of water | |
CN221370910U (en) | Corrosion-resistant chemical wastewater treatment tank | |
CN219259774U (en) | Sewage treatment recycling equipment | |
JP3941293B2 (en) | Method and apparatus for treating harmful substances in sewage | |
CN217188510U (en) | VOC organic waste gas treatment device | |
CN221732885U (en) | Kitchen garbage treatment deodorizing device | |
CN210163287U (en) | Medical wastewater treatment device based on vortex injection aeration technology | |
CN213085719U (en) | Chemical production sewage treatment device | |
CN219630243U (en) | Drinking water deodorization and deodorization reaction tank | |
KR102138176B1 (en) | Wastewater pre-processing system with OH reaction agitation tank | |
CN214862438U (en) | Multistage absorbing device for toxic and harmful gases in industrial wastewater | |
JPH09299753A (en) | Organic chlorine compound photolysis device | |
CN211644977U (en) | Membrane biological reaction tank applied to industrial sewage treatment |