CN104478158A - Sewage treatment method - Google Patents
Sewage treatment method Download PDFInfo
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- CN104478158A CN104478158A CN201410648456.9A CN201410648456A CN104478158A CN 104478158 A CN104478158 A CN 104478158A CN 201410648456 A CN201410648456 A CN 201410648456A CN 104478158 A CN104478158 A CN 104478158A
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F9/00—Multistage treatment of water, waste water or sewage
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F11/00—Treatment of sludge; Devices therefor
- C02F11/12—Treatment of sludge; Devices therefor by de-watering, drying or thickening
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F11/00—Treatment of sludge; Devices therefor
- C02F11/12—Treatment of sludge; Devices therefor by de-watering, drying or thickening
- C02F11/121—Treatment of sludge; Devices therefor by de-watering, drying or thickening by mechanical de-watering
- C02F11/123—Treatment of sludge; Devices therefor by de-watering, drying or thickening by mechanical de-watering using belt or band filters
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/001—Processes for the treatment of water whereby the filtration technique is of importance
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2301/00—General aspects of water treatment
- C02F2301/08—Multistage treatments, e.g. repetition of the same process step under different conditions
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F3/00—Biological treatment of water, waste water, or sewage
- C02F3/02—Aerobic processes
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F3/00—Biological treatment of water, waste water, or sewage
- C02F3/28—Anaerobic digestion processes
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F3/00—Biological treatment of water, waste water, or sewage
- C02F3/34—Biological treatment of water, waste water, or sewage characterised by the microorganisms used
- C02F3/341—Consortia of bacteria
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Abstract
Description
技术领域technical field
本发明涉及水治理领域,尤其涉及一种污水处理方法。The invention relates to the field of water treatment, in particular to a sewage treatment method.
背景技术Background technique
随着国民经济的迅猛发展,城市规模不断扩大和城镇化的快速发展,城市工业废水和生活污水的排放总量也逐年加大。若未经处理的废水、污水直接排入自然水体,不但会严重污染江、河、湖、库和地下水的水质,而且会大量传播病菌、病毒、有害物质和有害气体,影响人民群众的生活质量和身体健康。With the rapid development of the national economy, the continuous expansion of cities and the rapid development of urbanization, the total discharge of urban industrial wastewater and domestic sewage has also increased year by year. If untreated wastewater and sewage are directly discharged into natural water bodies, it will not only seriously pollute the water quality of rivers, lakes, reservoirs and groundwater, but also spread a large number of germs, viruses, harmful substances and harmful gases, affecting the quality of life of the people and good health.
面对步步紧逼的水危机,我国政府已将城市污水处理及水再生利用技术、工业废水处理及循环利用工业技术、节水技术与装备作为当前国家优先发展的环保产业和重点领域。Facing the pressing water crisis, the Chinese government has made urban sewage treatment and water recycling technology, industrial wastewater treatment and recycling industrial technology, water-saving technology and equipment as the current national priority development of environmental protection industries and key areas.
近年来,全国城市污水处理厂的建设逐步受到重视,污水处理厂已纳入市政基础建设。但建设速度远远赶不上污染防治的需要。In recent years, the construction of urban sewage treatment plants across the country has gradually received attention, and sewage treatment plants have been incorporated into municipal infrastructure. But the speed of construction is far behind the needs of pollution prevention and control.
目前我国污水处理主要采用好氧生物加膜处理技术,即AAOM工艺。由于其建设投资高、施工设备要求高、运行处理成本和管理维修费用高,污泥产量大、处理效率低(俗称“三高一低”工艺)的问题,导致我国污水处理事业步履艰难,甚至出现污水处理厂“建得起、用不起”的尴尬局面。因此迫切需要发展高效、实用、经济适合我国国情的城镇污水处理新技术。At present, my country's sewage treatment mainly adopts aerobic biological membrane treatment technology, that is, AAOM process. Due to its high construction investment, high construction equipment requirements, high operation and treatment costs, management and maintenance costs, large sludge output, and low treatment efficiency (commonly known as the "three highs and one low" process), the sewage treatment industry in my country is struggling, and even There is an embarrassing situation where sewage treatment plants are "affordable to build but unusable". Therefore, there is an urgent need to develop new technologies for urban sewage treatment that are efficient, practical, and economical and suitable for my country's national conditions.
发明内容Contents of the invention
针对上述现有技术中的缺点和不足,本发明的目的在于提供一种投入成本低、污泥产量小且处理效率高的污水处理方法。In view of the shortcomings and deficiencies in the prior art above, the purpose of the present invention is to provide a sewage treatment method with low input cost, low sludge output and high treatment efficiency.
本发明的目的是通过以下技术方案实现的:The purpose of the present invention is achieved through the following technical solutions:
一种污水处理方法,将污水在厂内先经过粗格栅去除大的漂浮物,然后流入集水池;污水经立式污水泵提升至较粗格栅网孔小的组合式旋转细格栅,组合式旋转细格栅把杂物及砂粒从废水中分离出来;经旋转细格栅处理后的出水进入厌氧池,由推进器将进水和厌氧污泥混合进行厌氧处理;经厌氧处理后的污水流入生化池,首次流入时加入以光合菌群、乳酸菌群、酵母菌群、革兰氏阳性放线菌群和发酵的丝状菌群组成的复合菌剂,形成益生菌菌群,利用悬链式曝气器曝气充氧进行好氧处理;处理后的污水,经沉淀后再进行曝气充氧稳定,污水自流入消毒池,消毒后排放。A sewage treatment method, the sewage is passed through the coarse grid to remove large floating objects in the factory, and then flows into the sump; the sewage is lifted by the vertical sewage pump to the combined rotating fine grid with smaller mesh size than the coarse grid, The combined rotating fine grid separates sundries and sand from the wastewater; the effluent treated by the rotating fine grid enters the anaerobic tank, and the propeller mixes the influent and anaerobic sludge for anaerobic treatment; The sewage after oxygen treatment flows into the biochemical tank, and when it flows in for the first time, a composite bacterial agent composed of photosynthetic bacteria, lactic acid bacteria, yeast bacteria, Gram-positive actinomycetes and fermented filamentous bacteria is added to form probiotics The group uses catenary aerator to aerate and oxygenate for aerobic treatment; the treated sewage is aerated and oxygenated after sedimentation to stabilize it, and the sewage flows into the disinfection tank by itself, and is discharged after disinfection.
优选地,沉淀后产生的污泥用污泥泵送入污泥浓缩池,污泥经浓缩后再由螺杆泵送入带式压滤机脱水;污泥浓缩池产生的上清液和压滤机产生的滤液自流入集水池二次处理。Preferably, the sludge generated after sedimentation is sent to the sludge thickening tank with a sludge pump, and the sludge is then sent to a belt filter press for dehydration by a screw pump after being concentrated; The filtrate produced by the machine flows into the sump for secondary treatment.
优选地,在曝气和澄清过程中需要的氧气由风机供给。Preferably, the oxygen required during aeration and clarification is supplied by fans.
与现有技术相比,本发明实施例至少具有以下优点:Compared with the prior art, the embodiments of the present invention have at least the following advantages:
本发明实施例中,本污水处理方法投资低、效率高污泥回流量大、工艺简单,为提高污水处理能力,在运行过程中投加有效微生物菌剂,可以有效的降解各类污染物,除去臭味,减低污染负荷。微生物能在常温、常压下运行,不仅能耗低、出水效果好,且没有二次污染。出水水质达到GB8979-96的二级水标准,进一步处理可考虑回用。In the embodiment of the present invention, this sewage treatment method has low investment, high efficiency, large sludge return flow, and simple process. In order to improve the sewage treatment capacity, effective microbial agents are added during the operation process, which can effectively degrade various pollutants. Remove odor and reduce pollution load. Microorganisms can operate at normal temperature and pressure, not only low energy consumption, good water discharge effect, but also no secondary pollution. The effluent water quality has reached the second-grade water standard of GB8979-96, and further treatment can be considered for reuse.
具体实施方式Detailed ways
下面结合实施例对本发明作进一步详述,以下实施例只是描述性的,不是限定性的,不能以此限定本发明的保护范围。Below in conjunction with embodiment the present invention is described in further detail, following embodiment is only descriptive, not restrictive, can not limit protection scope of the present invention with this.
将污水在厂内先经过粗格栅去除大的漂浮物,然后自流入集水池。污水经立式污水泵提升至组合式旋转细格栅,组合式旋转细格栅可把杂物及砂粒从废水中分离出来,同时可以除掉一部分有机负荷。旋转细格栅处理出水先进入厌氧池,由推进器将进水和厌氧污泥混合进行厌氧处理,然后自流入生化池,初次运行时加入我们开发的有效微生物菌剂(是以光合菌群、乳酸菌群、酵母菌群、革兰氏阳性放线菌群和发酵的丝状菌群等5大类10属80余种微生物组成的复合菌剂,因而形成强大的益生菌菌群,通过氧化、还原、发酵等途径,分解氧化有机物,能有效地降解有机物,抑制、杀灭各种有害细菌,抑制流行病原微生物的传播,消除硫化氢和氨等常见异味,起到改善环境的作用),利用悬链式曝气器曝气充氧进行好氧处理,处理后的污水,经沉淀后再进行曝气充氧稳定,污水自流入消毒池,消毒后排放。沉淀产生的污泥用污泥泵送入污泥浓缩池,污泥经浓缩后再由螺杆泵送人带式压滤机脱水。污泥浓缩池产生的上清液和压滤机产生的滤液自流入集水池二次处理。曝气和澄清过程需要的氧气由风机供给,预处理设施产生的机械杂物外运填埋处置,产生的剩余污泥外运用作农肥。In the factory, the sewage first passes through the coarse grid to remove large floating objects, and then flows into the sump. The sewage is lifted to the combined rotary fine screen by the vertical sewage pump. The combined rotary fine screen can separate sundries and sand particles from the waste water and remove part of the organic load at the same time. The effluent treated by the rotating fine grid first enters the anaerobic tank, and the propeller mixes the influent water and anaerobic sludge for anaerobic treatment, and then flows into the biochemical tank by itself, and the effective microbial agent developed by us (based on photosynthesis) is added to the initial operation. Bacteria, lactic acid bacteria, yeast, gram-positive actinomycetes, and fermented filamentous bacteria, which are composed of more than 80 kinds of microorganisms in 10 genera and 5 categories, thus forming a powerful probiotic flora, Decompose oxidized organic matter through oxidation, reduction, fermentation, etc., which can effectively degrade organic matter, inhibit and kill various harmful bacteria, inhibit the spread of epidemic pathogenic microorganisms, eliminate common odors such as hydrogen sulfide and ammonia, and play a role in improving the environment. ), the catenary aerator is used to aerate and oxygenate for aerobic treatment, and the treated sewage is aerated and oxygenated after sedimentation to stabilize it. The sewage flows into the disinfection tank and is discharged after disinfection. The sludge produced by sedimentation is sent to the sludge thickening tank by the sludge pump, and then the sludge is concentrated and then sent to the belt filter press for dehydration by the screw pump. The supernatant from the sludge thickening tank and the filtrate from the filter press flow into the sump for secondary treatment. The oxygen required for the aeration and clarification process is supplied by the fan, the mechanical debris generated by the pretreatment facility is transported to landfill, and the remaining sludge is used as agricultural fertilizer.
该污水处理方法的工艺特点:The process characteristics of the sewage treatment method:
投资低:由于采用土池加防渗措施,每吨水的建设费用大约在800~1000元左右,而AAOM工艺每吨水的建设费用为3000~3200元左右。所以本发明中的水处理方法所需费用大大低于其他工艺污水处理厂的建设费用。另外还具有占地面积小,因地制宜地布置,不受地形影响。Low investment: Due to the use of earthen ponds and anti-seepage measures, the construction cost per ton of water is about 800-1000 yuan, while the construction cost of AAOM process is about 3000-3200 yuan per ton of water. Therefore, the required cost of the water treatment method in the present invention is much lower than the construction cost of other process sewage treatment plants. In addition, it has a small footprint and is arranged according to local conditions without being affected by terrain.
根据国家环保局1992年《工业废水处理设施的调查与研究》,我国工业废水处理设施资金的54%用于土建工程设施,而只有36%用于设备,造成这种投资分配格局的主要原因是工艺池大都采用价格昂贵的钢筋混凝土池。而龙田污水厂土建工程造价,仅占总投资的20%。大的钢筋混凝土池不仅价格昂贵,而且施工难度大。为了减少投资,本发明中所采用的曝气池首先是使用HDPE防渗膜隔绝污水和地下水,其次是悬挂在浮管上的微孔曝气头避免了在池底池壁穿孔安装。这种敷设HDPE防渗膜的土池不仅易于开挖、投资低廉,而且完全能满足污水处理池功能上的要求,并能因地制宜,极好地适应现场的地形,存某些特殊的地质条件下,如地震多发地区、土质疏松地区,其优点得到更充分的体现。敷设HDPE防渗膜的土池使用寿命远远超过钢筋混凝土池。According to the "Investigation and Research on Industrial Wastewater Treatment Facilities" issued by the National Environmental Protection Agency in 1992, 54% of the funds for industrial wastewater treatment facilities in my country are used for civil engineering facilities, while only 36% are used for equipment. The main reason for this investment allocation pattern is Most of the craft pools use expensive reinforced concrete pools. The civil engineering cost of Longtian Sewage Plant only accounts for 20% of the total investment. Large reinforced concrete pools are not only expensive, but also difficult to construct. In order to reduce investment, the aeration tank adopted in the present invention first uses HDPE anti-seepage membrane to isolate sewage and groundwater, and secondly, the microporous aeration head suspended on the floating pipe avoids perforation installation at the bottom of the tank and the wall. This kind of earth pond with HDPE anti-seepage membrane is not only easy to excavate and low in investment, but also can fully meet the functional requirements of sewage treatment ponds, and can adapt to local conditions and adapt to the terrain of the site. Under certain special geological conditions, Such as earthquake-prone areas and loose soil areas, its advantages are more fully reflected. The service life of the earth pond with HDPE anti-seepage membrane is far longer than that of the reinforced concrete pond.
效率高:利用浮在水面的移动式曝气链系统,底部有微孔曝气头,曝气效率高。曝气机安装在池边,能耗小。能耗仅为传统污水处理的1/2~1/3左右。High efficiency: Using the mobile aeration chain system floating on the water surface, there is a microporous aeration head at the bottom, and the aeration efficiency is high. The aerator is installed beside the pool with low energy consumption. Energy consumption is only about 1/2 to 1/3 of traditional sewage treatment.
传统污水处理很少采用低负荷活性污泥系统,这是因为没有高效,合理的工艺及曝气器。C-BIOLAK曝气器(BIoLAK一FluoX)的发展,为我们早已熟悉的并取得一定效果的这个工艺的运用开辟了更广阔的天地。采用C-BIOLAK曝气器的系统曝气池中混合作用所需的耗能仅为1.5瓦/m3,而一般的传统曝气法中混合作用的耗能为10~15瓦/m3,这无疑是非常有价值的改进。Traditional sewage treatment rarely uses low-load activated sludge systems because there are no efficient and reasonable processes and aerators. The development of C-BIOLAK aerator (BIoLAK-FluoX) has opened up a wider world for the application of this process that we are already familiar with and has achieved certain effects. The energy consumption required for mixing in the system aeration tank using C-BIOLAK aerator is only 1.5 watts/m 3 , while the energy consumption for mixing in the general traditional aeration method is 10-15 watts/m 3 , This is undoubtedly a very valuable improvement.
污泥回流量大:在运行过程中,30~40%的污泥被微生物消耗,另有30~40%的污泥回流处理,剩余污泥是传统工艺的20~30%能长时间存放不腐烂,不产生臭味,经贮存池干化,可做农业肥料。C-BIOLAK工艺污泥回流量大,污泥浓度较高,生物量大,相对曝气时间较长,所以污泥负荷较低。Large sludge return flow: During the operation, 30-40% of the sludge is consumed by microorganisms, and another 30-40% of the sludge is refluxed for treatment. The remaining sludge is 20-30% of the traditional process and can be stored for a long time. It rots, does not produce odor, and can be used as agricultural fertilizer after being dried in the storage pool. The C-BIOLAK process has large sludge return flow, high sludge concentration, large biomass, and relatively long aeration time, so the sludge load is low.
工艺简单:此工艺启动快,操作、管理、维修方便,运行稳定后,每吨污水的运行费用较低,为传统方法的1/3~1/4左右。维修时不需要放空或停产。由于C-BIOLAK微孔曝气器(BloLAK一FluoX)特殊的结构,既使在很复杂的环境里曝气器也不至于阻塞,这意味着曝气装置可运行几年不维修,减少了维修的工作量,所以需维护费用很少。C-BIOLAK工艺通过大量回流污泥,其剩余污泥比传统工艺少许多。在使用污泥以前不再需要任何处理,因此,花在处理污泥上的费用也是很低的。Simple process: This process starts quickly, and is easy to operate, manage, and maintain. After stable operation, the operating cost per ton of sewage is low, which is about 1/3 to 1/4 of the traditional method. There is no need to vent or stop production for repairs. Due to the special structure of the C-BIOLAK microporous aerator (BloLAK-FluoX), the aerator will not be blocked even in a very complicated environment, which means that the aeration device can run for several years without maintenance, reducing maintenance The workload, so the maintenance cost is very little. The C-BIOLAK process uses a large amount of return sludge, and its residual sludge is much less than the traditional process. There is no need for any treatment before using the sludge, so the cost of sludge treatment is also very low.
C-BIOLAK系统没有水下固定部件,维修时不用排干池中的水,而用小船到维修地点将曝气链下的曝气头提起即可。实践表明,曝气头运行几年也不用任何维修,这主要是因为曝气管是由很细的纤维(直径约0.003mm)做成,并用聚合物充填,以达到防水和防脏物的目的。同时,曝气头有大约80%的自由空隙和20%的表面,和传统曝气头刚好相反。因此,微生物可生长的面积很小,并很容易被去除。当曝气头必须维修时,也不影响整个污水处理场的运行。该工艺的移动部件和易老化部件都很少。在选择设备和材料时,都采用了可靠耐用的材料。该工艺无需太多的自动化。它既不需要任何易损的探测器,也不需要任何复杂的控制系统。The C-BIOLAK system has no underwater fixed parts, and there is no need to drain the water in the pool during maintenance, but just use a boat to lift the aeration head under the aeration chain to the maintenance site. Practice shows that the aeration head does not need any maintenance after several years of operation, mainly because the aeration tube is made of very thin fibers (about 0.003mm in diameter) and filled with polymers to achieve the purpose of waterproofing and anti-dirt . At the same time, the aerator head has about 80% free space and 20% surface area, which is just the opposite of the traditional aerator head. As a result, the microbes have a small area to grow and are easily removed. When the aeration head must be maintained, it does not affect the operation of the entire sewage treatment plant. The process has very few moving and aging parts. When selecting equipment and materials, reliable and durable materials are used. The process does not require much automation. It does not require any fragile detectors nor any complex control system.
为提高污水处理能力,在运行过程中投加有效微生物菌剂,可以有效的降解各类污染物,除去臭味,减低污染负荷。微生物能在常温、常压下运行,不仅能耗低、出水效果好,且没有二次污染。出水水质达到GB8979-96的二级水标准,进一步处理可考虑回用。In order to improve the sewage treatment capacity, effective microbial agents are added during operation, which can effectively degrade various pollutants, remove odors, and reduce pollution loads. Microorganisms can operate at normal temperature and pressure, not only low energy consumption, good water discharge effect, but also no secondary pollution. The effluent water quality has reached the second-grade water standard of GB8979-96, and further treatment can be considered for reuse.
以上所述,仅为本发明较佳的具体实施方式,但本发明的保护范围并不局限于此,任何熟悉本技术领域的技术人员在本发明揭露的技术范围内,可轻易想到的变化或替换,都应涵盖在本发明的保护范围之内。因此,本发明的保护范围应该以权利要求书的保护范围为准。The above is only a preferred embodiment of the present invention, but the scope of protection of the present invention is not limited thereto. Any person skilled in the art within the technical scope disclosed in the present invention can easily think of changes or Replacement should be covered within the protection scope of the present invention. Therefore, the protection scope of the present invention should be determined by the protection scope of the claims.
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Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105293765A (en) * | 2015-10-26 | 2016-02-03 | 北京东方协和医药生物技术有限公司 | Domestic wastewater treatment fundamental technology |
| CN105601046A (en) * | 2016-03-10 | 2016-05-25 | 蒋安美 | Domestic sewage treatment method |
| CN106946389A (en) * | 2017-03-31 | 2017-07-14 | 陈来胜 | A kind of sewage-treatment plant |
| CN107777833A (en) * | 2016-08-29 | 2018-03-09 | 江苏众胜灭菌设备科技有限公司 | A kind of sewage water treatment method |
| CN108191190A (en) * | 2017-12-30 | 2018-06-22 | 山东中荣生物科技有限公司 | A kind of sewage treatment plant's biochemical system mud decrement method |
| CN108298681A (en) * | 2018-04-12 | 2018-07-20 | 南京林业大学 | Light intensity energy-saving sewage treating device |
Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| RU2144517C1 (en) * | 1999-05-05 | 2000-01-20 | Камайданов Евгений Николаевич | Method and plant for treatment of sewage |
| CN2737787Y (en) * | 2004-05-24 | 2005-11-02 | 北京科技大学 | Sewage treatment apparatus with swinging aeration head |
| US20110127214A1 (en) * | 2008-02-15 | 2011-06-02 | Rico Martinez Mauricio | Energy optimization in an anaerobic, facultative, anoxic aerobic plant, using fine bubbles, without sludge production |
| CN102173529A (en) * | 2010-11-30 | 2011-09-07 | 福建凤竹纺织科技股份有限公司 | Deodorization method in treatment of printing and dyeing wastewater |
| CN203440210U (en) * | 2013-09-12 | 2014-02-19 | 江苏和顺环保股份有限公司 | Wastewater treatment system for pharmaceutical factory |
-
2014
- 2014-11-17 CN CN201410648456.9A patent/CN104478158A/en active Pending
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| RU2144517C1 (en) * | 1999-05-05 | 2000-01-20 | Камайданов Евгений Николаевич | Method and plant for treatment of sewage |
| CN2737787Y (en) * | 2004-05-24 | 2005-11-02 | 北京科技大学 | Sewage treatment apparatus with swinging aeration head |
| US20110127214A1 (en) * | 2008-02-15 | 2011-06-02 | Rico Martinez Mauricio | Energy optimization in an anaerobic, facultative, anoxic aerobic plant, using fine bubbles, without sludge production |
| CN102173529A (en) * | 2010-11-30 | 2011-09-07 | 福建凤竹纺织科技股份有限公司 | Deodorization method in treatment of printing and dyeing wastewater |
| CN203440210U (en) * | 2013-09-12 | 2014-02-19 | 江苏和顺环保股份有限公司 | Wastewater treatment system for pharmaceutical factory |
Non-Patent Citations (3)
| Title |
|---|
| 何强等: "《细部小城镇污水处理设施建设技术指南》", 30 September 2011 * |
| 李桂平: "某工业园区污水处理厂设计", 《工业水处理》 * |
| 环境保护部污染物排放总量控制司组织编写: "《城镇分散型水污染物减排实用技术汇编》", 31 January 2009 * |
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105293765A (en) * | 2015-10-26 | 2016-02-03 | 北京东方协和医药生物技术有限公司 | Domestic wastewater treatment fundamental technology |
| CN105601046A (en) * | 2016-03-10 | 2016-05-25 | 蒋安美 | Domestic sewage treatment method |
| CN107777833A (en) * | 2016-08-29 | 2018-03-09 | 江苏众胜灭菌设备科技有限公司 | A kind of sewage water treatment method |
| CN106946389A (en) * | 2017-03-31 | 2017-07-14 | 陈来胜 | A kind of sewage-treatment plant |
| CN108191190A (en) * | 2017-12-30 | 2018-06-22 | 山东中荣生物科技有限公司 | A kind of sewage treatment plant's biochemical system mud decrement method |
| CN108298681A (en) * | 2018-04-12 | 2018-07-20 | 南京林业大学 | Light intensity energy-saving sewage treating device |
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