CN105000729A - Comprehensive wastewater purification system - Google Patents
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Abstract
本发明公开了一种综合废水净化系统,包括净化塔、雾化器、臭氧机,净化塔上部侧壁设有废水入口,内部从上到下依次设有缓流层、导流层以及吸附层;缓流层为单层平板结构,位于废水入口下方;单层平板结构上远离废水入口的一端设有多个通孔;导流层由多层斜面导流板组成;导流板表面设有光栅结构;光栅结构表面设有多孔膜;雾化器的喷嘴位于净化塔内,位于导流层下方;吸附层由两层石英砂过滤网组成;两层石英砂过滤网之间设有与臭氧机相连的臭氧入口;净化塔底端设有流体出口。本发明提供的综合废水净化系统可及时准确的处理废水,达到排放要求,保护环境,也为企业造福;装置组成合理,维护容易。
The invention discloses a comprehensive wastewater purification system, which comprises a purification tower, an atomizer, and an ozone machine. The upper side wall of the purification tower is provided with a wastewater inlet, and the interior is sequentially provided with a slow flow layer, a diversion layer and an adsorption layer from top to bottom. ; The slow flow layer is a single-layer flat structure, located below the waste water inlet; the end of the single-layer flat plate structure away from the waste water inlet is provided with a plurality of through holes; the diversion layer is composed of multi-layer inclined deflectors; Grating structure; there is a porous film on the surface of the grating structure; the nozzle of the atomizer is located in the purification tower and below the diversion layer; the adsorption layer is composed of two layers of quartz sand filters; between the two layers of quartz sand filters is a The ozone inlet connected to the machine; there is a fluid outlet at the bottom of the purification tower. The comprehensive waste water purification system provided by the invention can timely and accurately treat waste water, meet discharge requirements, protect the environment, and benefit enterprises; the device has reasonable composition and is easy to maintain.
Description
技术领域 technical field
本发明涉及一种废水处装置,具体涉及一种综合废水净化系统,用于废水的高效处理。 The invention relates to a waste water treatment device, in particular to a comprehensive waste water purification system for high-efficiency waste water treatment.
背景技术 Background technique
废水是指居民活动过程中排出的水及径流雨水的总称,它包括生活污水、工业废水和初雨径流入排水管渠等其它无用水。电镀是当今全球三大污染行业之一。电镀废水,尤其是综合电镀废水具有污染物种类多、成分复杂、毒性大以及危害严重的特点,其主要污染物是多种重金属离子、氰化物、废酸和废碱等。电镀工厂排出的废水和废液,如镀件漂洗水、废槽液、设备冷却水和冲洗地面水等,其水质因生产工艺而异,往往含油多种金属离子,一般来说,常含有Cr6+、Cd2+、Ni2+、Cu2+、Zn2+、Fe2+等重金属;电镀废水有毒,危害大。如氰可引起人畜急性中毒,致死,低浓度长期作用也能造成慢性中毒。镉可使肾脏发生病变,并会引起痛痛病。六价铬可引起肺癌、肠胃道疾病和贫血,并会在骨、脾和肝脏内蓄积。因此,电镀废水必须严格控制,妥善处理。 Wastewater refers to the general term for water discharged during residents' activities and runoff rainwater. It includes domestic sewage, industrial wastewater, and other useless water such as primary rain runoff into drainage pipes and ditches. Electroplating is one of the three major polluting industries in the world today. Electroplating wastewater, especially comprehensive electroplating wastewater, has the characteristics of many types of pollutants, complex components, high toxicity and serious hazards. The main pollutants are various heavy metal ions, cyanide, waste acid and waste alkali, etc. Wastewater and waste liquid discharged from electroplating factories, such as rinsing water of plating parts, waste bath liquid, equipment cooling water and flushing ground water, etc., the water quality varies with the production process, and often contains oil and various metal ions. Generally speaking, it often contains Cr 6+ , Cd 2+ , Ni 2+ , Cu 2+ , Zn 2+ , Fe 2+ and other heavy metals; electroplating wastewater is toxic and harmful. For example, cyanide can cause acute poisoning of humans and animals and cause death, and long-term effects of low concentrations can also cause chronic poisoning. Cadmium can cause pathological changes in the kidneys and cause itai disease. Hexavalent chromium can cause lung cancer, gastrointestinal disorders, and anemia, and can accumulate in bones, spleen, and liver. Therefore, electroplating wastewater must be strictly controlled and properly disposed of.
在生活污水、食品加工和造纸等工业废水中,含有碳水化合物、蛋白质、油脂、木质素等有机物质。这些物质以悬浮或溶解状态存在于污水中,可通过微生物的生物化学作用而分解。在其分解过程中需要消耗氧气,因而被称为耗氧污染物。这种污染物可造成水中溶解氧减少,影响鱼类和其他水生生物的生长。水中溶解氧耗尽后,有机物进行厌氧分解,产生硫化氢、氨和硫醇等难闻气味,使水质恶化。水体中有机物成分非常复杂,耗氧有机物浓度常用单位体积水中耗氧物质生化分解过程中所消耗的氧量表示。 Industrial wastewater such as domestic sewage, food processing, and papermaking contains organic substances such as carbohydrates, proteins, oils, and lignin. These substances exist in the sewage in a suspended or dissolved state and can be decomposed by the biochemical action of microorganisms. Oxygen-depleting pollutants are called oxygen-depleting pollutants because they consume oxygen during their decomposition. This pollutant can reduce dissolved oxygen in the water, affecting the growth of fish and other aquatic organisms. After the dissolved oxygen in the water is exhausted, the organic matter undergoes anaerobic decomposition, producing unpleasant odors such as hydrogen sulfide, ammonia and mercaptans, which deteriorate the water quality. The composition of organic matter in water is very complex, and the concentration of oxygen-consuming organic matter is usually expressed by the amount of oxygen consumed during the biochemical decomposition of oxygen-consuming substances in a unit volume of water.
现有的废水的处理方法为:直接对工厂排出的废水通过重金属离子去除装置去除重金属离子,然后通过污水管网排到污水处理厂进行氨氮和有机物的处理。具体水处理工艺很多,包括树脂交换、电解法、化学法与气浮等。现有的废水处理方法存在电解法能耗高,电耗和铁耗均高,对高浓度含铬废水产生污泥量太多,不适应,同时对含氰废水处理不理想;化学药剂和气浮法采用化学药品氧化还原中和,用气浮上浮方法进行泥水分离,因电镀污泥比重大,并且废水中含有多种有机添加剂,实际使用时气浮分离不彻底,并且运行管理不便的不足 The existing wastewater treatment method is: directly remove heavy metal ions from the wastewater discharged from the factory through a heavy metal ion removal device, and then discharge it to a sewage treatment plant through a sewage pipe network for treatment of ammonia nitrogen and organic matter. There are many specific water treatment processes, including resin exchange, electrolysis, chemical method and air flotation. Existing wastewater treatment methods have high energy consumption, high power consumption and iron consumption by electrolysis, too much sludge generated for high-concentration chromium-containing wastewater, which is not suitable, and it is not ideal for cyanide-containing wastewater; chemical agents and air flotation The method uses chemical redox neutralization, and uses air flotation to separate mud and water. Because the electroplating sludge has a large proportion and the wastewater contains a variety of organic additives, the air flotation separation is not complete in actual use, and the operation and management are inconvenient.
所以,为了实现综合废水的真正有效处理,需要研发一种综合废水净化系统,其能够用于废水的高效处理。 Therefore, in order to realize the truly effective treatment of comprehensive wastewater, it is necessary to develop a comprehensive wastewater purification system that can be used for efficient treatment of wastewater.
发明内容 Contents of the invention
本发明的发明目的是提供一种综合废水净化系统,可以有效地去除废水中的金属离子和有机物。 The purpose of the present invention is to provide a comprehensive wastewater purification system that can effectively remove metal ions and organic matter in wastewater.
为达到上述发明目的,本发明采用的技术方案是: In order to achieve the above-mentioned purpose of the invention, the technical scheme adopted in the present invention is:
一种综合废水净化系统,包括净化塔、雾化器、臭氧机,所述净化塔上部侧壁设有废水入口,内部从上到下依次设有缓流层、导流层以及吸附层;所述缓流层为单层平板结构,位于废水入口下方;所述单层平板结构上远离废水入口的一端设有多个通孔;所述导流层由多层斜面导流板组成;所述导流板表面设有光栅结构;所述光栅结构表面设有多孔膜;所述雾化器的喷嘴位于净化塔内,位于导流层下方;所述吸附层由两层石英砂过滤网组成;所述两层石英砂过滤网之间设有与臭氧机相连的臭氧入口;所述净化塔底端设有流体出口。 A comprehensive wastewater purification system, including a purification tower, an atomizer, and an ozone machine. The upper side wall of the purification tower is provided with a wastewater inlet, and the interior is sequentially provided with a slow flow layer, a diversion layer and an adsorption layer from top to bottom; The slow flow layer is a single-layer plate structure, located below the waste water inlet; the end of the single-layer plate structure away from the waste water inlet is provided with a plurality of through holes; the guide layer is composed of multi-layer inclined guide plates; The surface of the guide plate is provided with a grating structure; the surface of the grating structure is provided with a porous film; the nozzle of the atomizer is located in the purification tower and below the guide layer; the adsorption layer is composed of two layers of quartz sand filters; An ozone inlet connected with an ozone machine is arranged between the two layers of quartz sand filter screens; a fluid outlet is arranged at the bottom of the purification tower.
本发明中,单层平板结构上,设有多个通孔的区域的面积为整个单层平板面积的20-25%。可以减缓流速,增加过滤、吸附效果,同时通过设置的孔,不会阻碍废水的处理效率增加废水与导流板的接触时间,提高过滤效果,不会使得水流速下降厉害,避免流速下降导致的颗粒过滤效果差的缺陷。 In the present invention, on the single-layer plate structure, the area provided with a plurality of through holes accounts for 20-25% of the area of the entire single-layer plate. It can slow down the flow rate, increase the filtration and adsorption effect, and at the same time pass through the set holes, which will not hinder the treatment efficiency of wastewater. Increase the contact time between wastewater and the deflector, improve the filtration effect, and will not cause the water flow rate to drop sharply, avoiding the drop caused by the flow rate. The defect of poor particle filtering effect.
本发明中,斜面导流板与水平面的夹角为10-15度。导流板斜向设置,引导废水的流向以及在引导过程中很好的去除废水中的有机物,现有的去除有机物的方式大都为在静止水池中加入微生物或者物理吸附,本发明首次在废水流动过程中,有效的去除水中有机物,既提高效率又精简设备。可以根据需要设置导流板与塔壁之间的间隙,流体从间隙中流到下一个导流板上,本发明的斜面导流板优选为五层。 In the present invention, the included angle between the inclined guide plate and the horizontal plane is 10-15 degrees. The deflector is arranged obliquely to guide the flow of waste water and remove organic matter in the waste water during the guiding process. Most of the existing methods of removing organic matter are adding microorganisms or physical adsorption in a still pool. This invention is the first time in the flow of waste water During the process, the organic matter in the water is effectively removed, which not only improves the efficiency but also simplifies the equipment. The gap between the deflector and the tower wall can be set as required, and the fluid flows from the gap to the next deflector. The slope deflector of the present invention preferably has five layers.
有机物去除是微观处理效应,与过滤颗粒物等大杂质不同,采用由纤维状高分子吸附材料编织得到的多孔膜可以有效去除有机物;多孔膜的厚度为0.4-0.8mm;多孔膜的孔隙率为60-65%。 The removal of organic matter is a microscopic treatment effect. Unlike filtering large impurities such as particulate matter, the porous membrane woven from fibrous polymer adsorption materials can effectively remove organic matter; the thickness of the porous membrane is 0.4-0.8mm; the porosity of the porous membrane is 60 -65%.
本发明首次利用光栅结构形成有机物去除场所,光栅结构的厚度为2.5-3毫米,占空比为0.46-0.52。可以有效增加废水与多孔膜的接触,在每一个光栅结构的凹槽中,废水有极短暂的停顿,增加有机物去除率。 The present invention utilizes the grating structure for the first time to form an organic matter removal place, the thickness of the grating structure is 2.5-3 mm, and the duty ratio is 0.46-0.52. It can effectively increase the contact between the wastewater and the porous membrane. In each groove of the grating structure, the wastewater has a very short pause to increase the removal rate of organic matter.
优选的,雾化器的喷嘴为两个,且两个喷嘴关于净化塔的轴线对称分布。雾化器中放置的是可以是金属络合成固体物的试剂,试剂经雾化器雾化后由雾化喷嘴进入塔内与废水混合,雾化物可以增加混合均匀度,设置两个相互对称的雾化喷嘴,使得废水与试剂的混合无死角。 Preferably, there are two nozzles of the atomizer, and the two nozzles are distributed symmetrically about the axis of the purification tower. The reagents that can be metal complexed into solids are placed in the atomizer. After the reagents are atomized by the atomizer, they enter the tower from the atomization nozzle and mix with the waste water. The atomized materials can increase the mixing uniformity. Two mutually symmetrical Advanced atomizing nozzles make the mixing of wastewater and reagents without dead ends.
石英砂过滤网一方面去除废水中的颗粒物,更关键的是形成的回流通道,增加水与臭氧的接触,进一步去除有害物质;两层石英砂过滤网的过滤精度不同。 On the one hand, the quartz sand filter removes the particulate matter in the wastewater, and more importantly, the formed backflow channel increases the contact between water and ozone, and further removes harmful substances; the filtration accuracy of the two layers of quartz sand filters is different.
本发明的纤维状高分子吸附材料具有一定的强度,具有多孔结构,有效增加比表面积,亲油基团不仅存在于纤维表面,也大量存在微孔中,加快纤维吸附速度并进一步提高吸附容量。 The fibrous polymer adsorption material of the present invention has a certain strength, has a porous structure, and effectively increases the specific surface area. The lipophilic groups not only exist on the surface of the fiber, but also exist in a large number of micropores, which accelerates the fiber adsorption speed and further increases the adsorption capacity.
吸附技术是通过吸附材料捕集排入环境中的有害物达到处理的目的,可避免对环境的破坏,其核心在于吸附材料,以活性炭为代表的传统吸附材料以及相关吸附技术在吸附效果和工艺操作方面存在的缺陷,无法达到工业化的治理要求,尤其是颗粒状活性炭用于废水有机物污染事故处置时,根本无法实现对水面漂浮有毒有机污染物的清理回收,本发明首次利用高分子吸附材料,有效的解决了废水中的有机污染物,又避免了现有化学处理、生物处理方法带来的副作用。 Adsorption technology is to capture harmful substances discharged into the environment through adsorption materials to achieve the purpose of treatment, which can avoid damage to the environment. Its core lies in adsorption materials. The defects in the operation cannot meet the requirements of industrialized treatment, especially when the granular activated carbon is used for the disposal of wastewater organic pollution accidents, it is impossible to clean and recover the toxic organic pollutants floating on the water surface. The present invention uses polymer adsorption materials for the first time. It effectively solves the organic pollutants in the wastewater, and avoids the side effects caused by the existing chemical treatment and biological treatment methods.
由于上述技术方案运用,本发明与现有技术相比具有下列优点: Due to the use of the above-mentioned technical solutions, the present invention has the following advantages compared with the prior art:
1.本发明首次在废水流动过程中,有效的去除水中有机物,既提高效率又精简设备,利用光栅结构形成有机物去除场所,可以有效增加废水与多孔膜的接触,在每一个光栅结构的凹槽中,废水有极短暂的停顿,增加有机物去除率。 1. For the first time, the present invention effectively removes organic matter in water during the flow of waste water, which not only improves efficiency but also simplifies equipment. The grating structure is used to form an organic matter removal site, which can effectively increase the contact between waste water and porous membrane. In the groove of each grating structure, Wastewater has a very short pause, which increases the removal rate of organic matter.
2.本发明提供的综合废水净化系统为一体装置,可及时准确的处理综合废水,达到排放要求,保护环境,也为企业造福;装置组成合理,维护容易,适用于废水处理。 2. The comprehensive wastewater purification system provided by the invention is an integrated device, which can timely and accurately process comprehensive wastewater, meet discharge requirements, protect the environment, and benefit enterprises; the device has reasonable composition, easy maintenance, and is suitable for wastewater treatment.
附图说明 Description of drawings
图1为实施例中综合废水净化系统结构示意图; Fig. 1 is the structural representation of integrated waste water purification system in the embodiment;
图2为单层平板结构示意图; Fig. 2 is a schematic diagram of a single-layer plate structure;
图3为光栅结构示意图; Fig. 3 is a schematic diagram of grating structure;
其中,净化塔1、废水入口2、单层平板结构3、通孔31、斜面导流板4、光栅结构41、石英砂过滤网5、石英砂过滤网6、雾化器7、臭氧机8、喷嘴71、喷嘴72、臭氧入口81。 Among them, purification tower 1, waste water inlet 2, single-layer plate structure 3, through hole 31, inclined deflector 4, grating structure 41, quartz sand filter 5, quartz sand filter 6, atomizer 7, ozone machine 8 , Nozzle 71, nozzle 72, ozone inlet 81.
具体实施方式 Detailed ways
下面结合附图及实施例对本发明作进一步描述: The present invention will be further described below in conjunction with accompanying drawing and embodiment:
实施例一: Embodiment one:
见附图1,一种综合废水净化系统,包括净化塔1,其上部侧壁设有废水入口2、底端设有流体出口,为了更好流出,底部可以设置一定的倾斜,水入口下方设有单层平板结构3,单层平板结构上设有多个通孔31;单层平板结构下方五层斜面导流板4,斜面导流板与水平面的夹角为10-15度;导流板表面设有光栅结构41;光栅结构表面设有多孔膜;导流板下方设有两层石英砂过滤网5、6。 See accompanying drawing 1, a kind of comprehensive waste water purification system comprises a purification tower 1, and its upper side wall is provided with waste water inlet 2, and the bottom end is provided with fluid outlet, and in order to flow out better, the bottom can be provided with a certain inclination, and water inlet is provided below. There is a single-layer plate structure 3, and a plurality of through holes 31 are arranged on the single-layer plate structure; there are five layers of slope deflectors 4 under the single-layer plate structure, and the angle between the slope deflectors and the horizontal plane is 10-15 degrees; A grating structure 41 is provided on the surface of the plate; a porous film is provided on the surface of the grating structure; two layers of quartz sand filter screens 5 and 6 are provided under the guide plate.
还包括雾化器7、臭氧机8;雾化器的两个喷嘴71、72位于净化塔内,位于导流层下方;与臭氧机相连的臭氧入口81在两层石英砂过滤网之间。 It also includes an atomizer 7 and an ozone machine 8; the two nozzles 71 and 72 of the atomizer are located in the purification tower and below the diversion layer; the ozone inlet 81 connected with the ozone machine is between two layers of quartz sand filter screens.
上述多孔膜由纤维状高分子吸附材料编织得到,厚度为0.4-0.8mm,多孔膜的孔隙率为60-65%。 The above porous membrane is obtained by weaving fibrous polymer adsorption material, the thickness is 0.4-0.8mm, and the porosity of the porous membrane is 60-65%.
参见附图2,为单层平板结构示意图,设有多个通孔的区域的面积为整个单层平板面积的20%。 Referring to accompanying drawing 2, it is a schematic diagram of the structure of a single-layer plate, and the area of the area provided with multiple through holes is 20% of the area of the entire single-layer plate.
参见附图3,为光栅结构示意图,其厚度为2.5毫米,占空比为0.5。 Referring to accompanying drawing 3, it is a schematic diagram of a grating structure, its thickness is 2.5 millimeters, and its duty ratio is 0.5.
实施例二 Embodiment two
一种综合废水净化系统,与实施例一主体近似,其中斜面导流板为四层,最下方的导流板底部设有通孔;单层平板结构中,设有多个通孔的区域的面积为整个单层平板面积的25%;光栅结构的厚度为3毫米,占空比为0.5。 A comprehensive wastewater purification system, similar to the main body of Embodiment 1, wherein the inclined deflector has four layers, and the bottom of the bottom deflector is provided with through holes; in the single-layer flat plate structure, the area with multiple through holes The area is 25% of the entire single-layer flat plate; the thickness of the grating structure is 3 mm, and the duty ratio is 0.5.
实施例三 Embodiment three
实际处理时,废水由入口进入塔内,经由单层平板的孔流到导流板,有机物被去除;然后废水与试剂混合,形成金属固体物,流经石英砂过滤网过滤固体颗粒,同时臭氧进一步去除水中有害物,出水即可完成废水处理。 During the actual treatment, the wastewater enters the tower from the inlet, and flows to the deflector through the holes of the single-layer plate, and the organic matter is removed; then the wastewater is mixed with the reagent to form a metal solid, which flows through the quartz sand filter to filter the solid particles, and at the same time, the ozone Harmful substances in the water are further removed, and the wastewater treatment can be completed when the water is discharged.
表1为废水处理前后各物质含量,可以看出,本发明的装置有效的将废水处理为符合排放标准的水体。 Table 1 shows the content of each substance before and after the wastewater treatment. It can be seen that the device of the present invention effectively treats the wastewater into a water body that meets the discharge standard.
表1 电镀废水处理前后各物质含量(mg/L)
Claims (10)
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| CN201510406600.2A Pending CN105000729A (en) | 2015-07-13 | 2015-07-13 | Comprehensive wastewater purification system |
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107601762A (en) * | 2017-09-28 | 2018-01-19 | 佛山汇众森泰科技有限公司 | A kind of environment-friendly type phenol wastewater sorbing material processing unit (plant) and preparation method |
| CN108715503A (en) * | 2018-06-12 | 2018-10-30 | 北京濮源新材料技术研究院(普通合伙) | New process for treating waste water in a kind of bisphenol A production process |
| CN114259858A (en) * | 2021-12-18 | 2022-04-01 | 上海艾尔天合环境科技有限公司 | Aeration deodorizing device |
Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN201372224Y (en) * | 2009-02-16 | 2009-12-30 | 中国石化集团石油工程西南有限公司油田工程服务分公司 | Waste water oxidation treatment unit for oil and gas fields |
| CN201762179U (en) * | 2010-03-31 | 2011-03-16 | 长江大学 | Rural domestic sewage treatment unit |
| CN103058315A (en) * | 2013-01-29 | 2013-04-24 | 南京大学 | Tower-type adsorption reactor and system and method thereof for removing heavy metal ions in water |
| CN203428997U (en) * | 2013-08-29 | 2014-02-12 | 山东翔宇化纤有限公司 | Waste collection device in nylon 6 production |
| KR101488136B1 (en) * | 2014-06-17 | 2015-01-29 | 유한회사 도건엔지니어링 | Nonpoint pollution decrease apparatus |
| CN103693732B (en) * | 2013-12-09 | 2015-04-22 | 衢州绿都环保工程有限公司 | Sewage tank for ozone disinfection |
-
2015
- 2015-07-13 CN CN201510406600.2A patent/CN105000729A/en active Pending
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN201372224Y (en) * | 2009-02-16 | 2009-12-30 | 中国石化集团石油工程西南有限公司油田工程服务分公司 | Waste water oxidation treatment unit for oil and gas fields |
| CN201762179U (en) * | 2010-03-31 | 2011-03-16 | 长江大学 | Rural domestic sewage treatment unit |
| CN103058315A (en) * | 2013-01-29 | 2013-04-24 | 南京大学 | Tower-type adsorption reactor and system and method thereof for removing heavy metal ions in water |
| CN203428997U (en) * | 2013-08-29 | 2014-02-12 | 山东翔宇化纤有限公司 | Waste collection device in nylon 6 production |
| CN103693732B (en) * | 2013-12-09 | 2015-04-22 | 衢州绿都环保工程有限公司 | Sewage tank for ozone disinfection |
| KR101488136B1 (en) * | 2014-06-17 | 2015-01-29 | 유한회사 도건엔지니어링 | Nonpoint pollution decrease apparatus |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107601762A (en) * | 2017-09-28 | 2018-01-19 | 佛山汇众森泰科技有限公司 | A kind of environment-friendly type phenol wastewater sorbing material processing unit (plant) and preparation method |
| CN108715503A (en) * | 2018-06-12 | 2018-10-30 | 北京濮源新材料技术研究院(普通合伙) | New process for treating waste water in a kind of bisphenol A production process |
| CN114259858A (en) * | 2021-12-18 | 2022-04-01 | 上海艾尔天合环境科技有限公司 | Aeration deodorizing device |
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