CN108911123B - Anaerobic purification tank - Google Patents
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- 238000000746 purification Methods 0.000 title claims abstract description 25
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 72
- 239000010865 sewage Substances 0.000 claims abstract description 29
- 239000002893 slag Substances 0.000 claims abstract description 15
- 238000000926 separation method Methods 0.000 claims description 35
- 230000008676 import Effects 0.000 claims 1
- 239000010802 sludge Substances 0.000 abstract 1
- 239000007788 liquid Substances 0.000 description 9
- 238000000034 method Methods 0.000 description 7
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 6
- 241000196324 Embryophyta Species 0.000 description 5
- 238000005516 engineering process Methods 0.000 description 5
- 239000007789 gas Substances 0.000 description 5
- 239000007787 solid Substances 0.000 description 4
- 239000003344 environmental pollutant Substances 0.000 description 3
- 239000000945 filler Substances 0.000 description 3
- 231100000719 pollutant Toxicity 0.000 description 3
- 239000004576 sand Substances 0.000 description 3
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 description 2
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 229910052760 oxygen Inorganic materials 0.000 description 2
- 239000001301 oxygen Substances 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 229910052698 phosphorus Inorganic materials 0.000 description 2
- 239000011574 phosphorus Substances 0.000 description 2
- 238000001556 precipitation Methods 0.000 description 2
- 244000205574 Acorus calamus Species 0.000 description 1
- 235000011996 Calamus deerratus Nutrition 0.000 description 1
- 235000005273 Canna coccinea Nutrition 0.000 description 1
- 240000008555 Canna flaccida Species 0.000 description 1
- 241001633663 Iris pseudacorus Species 0.000 description 1
- 240000007313 Tilia cordata Species 0.000 description 1
- 230000004888 barrier function Effects 0.000 description 1
- 239000000969 carrier Substances 0.000 description 1
- 230000015556 catabolic process Effects 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 238000006731 degradation reaction Methods 0.000 description 1
- 238000012938 design process Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000012010 growth Effects 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 239000011159 matrix material Substances 0.000 description 1
- 244000005700 microbiome Species 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 238000005325 percolation Methods 0.000 description 1
- 238000005191 phase separation Methods 0.000 description 1
- 239000008213 purified water Substances 0.000 description 1
- 230000033458 reproduction Effects 0.000 description 1
- 238000004062 sedimentation Methods 0.000 description 1
- 238000009423 ventilation Methods 0.000 description 1
Classifications
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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
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E50/00—Technologies for the production of fuel of non-fossil origin
- Y02E50/30—Fuel from waste, e.g. synthetic alcohol or diesel
-
- 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
- Y02W10/10—Biological treatment of water, waste water, or sewage
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- Biological Treatment Of Waste Water (AREA)
- Purification Treatments By Anaerobic Or Anaerobic And Aerobic Bacteria Or Animals (AREA)
Abstract
Description
本申请是申请号为“201510704399.6”、发明名称为“集成化人工湿地污水处理系统”的发明的分案申请。This application is a divisional application of the invention with the application number “201510704399.6” and the invention title “Integrated Constructed Wetland Sewage Treatment System”.
技术领域Technical field
本发明涉及水处理技术,特别是涉及一种集成化人工湿地污水处理系统的技术。The present invention relates to water treatment technology, and in particular to an integrated constructed wetland sewage treatment system technology.
背景技术Background technique
人工湿地作为一种新兴的污水处理工艺,兴起于70年代的德国、美国、丹麦等国家。在我国由于中小城镇众多,人口密集,资金及技术有限,发展大型的污水处理厂由很大的困难性,因此建造和运转费用低、维护简单、效果良好人工湿地技术在我国有着广阔的应用前景。As an emerging sewage treatment process, constructed wetlands emerged in Germany, the United States, Denmark and other countries in the 1970s. In our country, due to the large number of small and medium-sized towns, dense population, limited funds and technology, it is very difficult to develop large-scale sewage treatment plants. Therefore, the construction and operation cost is low, the maintenance is simple, and the effect is good. Constructed wetland technology has broad application prospects in our country. .
目前的人工湿地污水处理技术中,污水中污染物的去除主要是依靠湿地主体,污水处理效率往往不高,造成这种情况是因为在湿地设计过程中,湿地进水一般只经过简单沉淀或格栅除渣,湿地进水污染物浓度过高。而且目前的人工湿地对土地需求量相对于处理水量来说一般偏多,造成这种情况的原因是许多人工湿地水力负荷低,即单位面积湿地能处理污水量低。而且现有的人工湿地在运行过程中往往容易堵塞,堵塞的原因有湿地进水水质难以控制悬浮物浓度太高、处理水量控制不稳定、布水不均匀、湿地主体填充物质渗水效果差。In the current constructed wetland sewage treatment technology, the removal of pollutants in sewage mainly relies on the main body of the wetland, and the sewage treatment efficiency is often not high. This is because during the wetland design process, the wetland water generally only undergoes simple sedimentation or gridding. Screen slag removal, the concentration of pollutants in the wetland water is too high. Moreover, current constructed wetlands generally require more land than the amount of water they can process. The reason for this is that many constructed wetlands have low hydraulic loads, that is, the amount of sewage that wetlands can process per unit area is low. Moreover, existing constructed wetlands are often prone to clogging during operation. The reasons for clogging include difficulty in controlling the wetland water quality and high concentration of suspended solids, unstable control of the treated water volume, uneven water distribution, and poor water seepage effect of the filling material in the main body of the wetland.
发明内容Contents of the invention
对上述现有技术中存在的缺陷,本发明所要解决的技术问题是提供一种污水处理效率高,且占地面积小、水力负荷大、运行稳定不易堵塞的集成化人工湿地污水处理系统。In view of the above-mentioned defects in the prior art, the technical problem to be solved by the present invention is to provide an integrated artificial wetland sewage treatment system with high sewage treatment efficiency, small footprint, large hydraulic load, stable operation and not easy to be blocked.
为了解决上述技术问题,本发明所提供的一种集成化人工湿地污水处理系统,包括用于净化水体的人工湿地床,其特征在于:还包括厌氧净化池、提升泵;In order to solve the above technical problems, the present invention provides an integrated artificial wetland sewage treatment system, which includes an artificial wetland bed for purifying water bodies, and is characterized by: also including an anaerobic purification tank and a lifting pump;
所述人工湿地床的上方平铺有用于向其布水的布水器,人工湿地床的底部平铺有用于汇集水体的集水器;A water distributor for distributing water to the artificial wetland bed is laid flat on the top, and a water collector for collecting water is laid flat on the bottom of the artificial wetland bed;
所述厌氧净化池内固定有三相分离器,该三相分离器将厌氧净化池的池腔分隔成上下各一个腔室,其中的上腔室内固定有出水堰,及包围住出水堰的挡渣板,下腔室的腔壁上开设有污水进口,且在下腔室的腔底开设有排泥口;A three-phase separator is fixed in the anaerobic purification tank. The three-phase separator divides the tank cavity of the anaerobic purification tank into an upper and lower chamber. The upper chamber is fixed with a water outlet weir and a barrier surrounding the water outlet weir. The slag board has a sewage inlet on the wall of the lower chamber and a mud discharge port on the bottom of the lower chamber;
所述三相分离器由第一分离罩、第二分离罩构成,第一分离罩是一个上下两端开放的倒锥台形的罩体,第二分离罩是一个向下单向开放的一个锥体形罩体,第二分离罩固定在第一分离罩内,第二分离罩的下沿与第一分离罩的内壁接合,且在第二分离罩的下边缘开设有多个过流孔,各过流孔沿第二分离罩的下边缘均匀分布,第二分离罩的顶部开设有一排气口,该排气口经一排气管接引至厌氧净化池外部;The three-phase separator is composed of a first separation cover and a second separation cover. The first separation cover is an inverted frustum-shaped cover body with upper and lower ends open. The second separation cover is a cone that is open in one direction downward. Body-shaped cover body, the second separation cover is fixed in the first separation cover, the lower edge of the second separation cover is joined with the inner wall of the first separation cover, and a plurality of overflow holes are opened on the lower edge of the second separation cover, each The overflow holes are evenly distributed along the lower edge of the second separation hood, and an exhaust port is provided on the top of the second separation hood. The exhaust port is led to the outside of the anaerobic purification tank through an exhaust pipe;
所述挡渣板高于三相分离器,挡渣板与出水堰之间具有空隙,出水堰的进水口高于挡渣板的底边;The slag retaining plate is higher than the three-phase separator, there is a gap between the slag retaining plate and the water outlet weir, and the water inlet of the water outlet weir is higher than the bottom edge of the slag retaining plate;
所述提升泵的进水口经管件接到出水堰的出水口,提升泵的泵水口接到布水器。The water inlet of the lift pump is connected to the water outlet of the water outlet weir through the pipe fitting, and the pump water port of the lift pump is connected to the water distributor.
进一步的,所述厌氧净化池的顶部由一盖板封闭,所述人工湿地床安装在盖板上。Further, the top of the anaerobic purification tank is closed by a cover plate, and the artificial wetland bed is installed on the cover plate.
进一步的,所述出水堰内装有液位开关,该液位开关接到提升泵的启停控制端。Further, a liquid level switch is installed in the water outlet weir, and the liquid level switch is connected to the start and stop control end of the lift pump.
进一步的,所述人工湿地床上种植有湿地植物。Further, wetland plants are planted on the artificial wetland bed.
进一步的,所述人工湿地床由多个介质层从上至下依次层叠而成,所述介质层包括活性炭粒层、陶粒层、塑料填料层、细砂层、碎石子层。Further, the artificial wetland bed is composed of multiple media layers stacked in sequence from top to bottom. The media layers include an activated carbon particle layer, a ceramsite layer, a plastic filler layer, a fine sand layer, and a gravel sub-layer.
进一步的,所述介质层的厚度为15~30cm。Further, the thickness of the dielectric layer is 15-30 cm.
本发明提供的集成化人工湿地污水处理系统,利用三相分离器对污水进行三相分离,污水经厌氧净化池处理后,水中污染物浓度降低,使人工湿地床能在相同时间内处理更大水量的污水,具有污水处理效率高的特点,而且水力负荷大、运行稳定不易堵塞;另外,将人工湿地床直接安装在厌氧净化池顶部,还能减少占地面积。The integrated constructed wetland sewage treatment system provided by the present invention uses a three-phase separator to perform three-phase separation of sewage. After the sewage is treated by an anaerobic purification tank, the concentration of pollutants in the water is reduced, allowing the constructed wetland bed to process more water in the same time. Large amounts of sewage have the characteristics of high sewage treatment efficiency, large hydraulic load, stable operation and not easy to be blocked; in addition, installing the artificial wetland bed directly on the top of the anaerobic purification tank can also reduce the area occupied.
附图说明Description of the drawings
图1是本发明实施例的集成化人工湿地污水处理系统的结构示意图;Figure 1 is a schematic structural diagram of an integrated constructed wetland sewage treatment system according to an embodiment of the present invention;
图2是本发明实施例的集成化人工湿地污水处理系统中的三相分离器的俯视图。Figure 2 is a top view of the three-phase separator in the integrated constructed wetland sewage treatment system according to the embodiment of the present invention.
具体实施方式Detailed ways
以下结合附图说明对本发明的实施例作进一步详细描述,但本实施例并不用于限制本发明,凡是采用本发明的相似结构及其相似变化,均应列入本发明的保护范围,本发明中的顿号均表示和的关系。The embodiments of the present invention will be described in further detail below with reference to the accompanying drawings. However, these embodiments are not intended to limit the present invention. Any similar structures and similar changes using the present invention should be included in the protection scope of the present invention. The spaces in all indicate the relationship between and.
如图1-图2所示,本发明实施例所提供的一种集成化人工湿地污水处理系统,包括用于净化水体的人工湿地床1,其特征在于:还包括厌氧净化池2、提升泵6;As shown in Figures 1 and 2, an integrated constructed wetland sewage treatment system provided by an embodiment of the present invention includes a constructed wetland bed 1 for purifying water bodies. It is characterized by: also including an anaerobic purification tank 2, a lifting Pump 6;
所述人工湿地床1的上方平铺有用于向其布水的布水器7,人工湿地床1的底部平铺有用于汇集水体的集水器8;A water distributor 7 for distributing water to the artificial wetland bed 1 is laid flat on the top, and a water collector 8 for collecting water is laid flat on the bottom of the artificial wetland bed 1;
所述厌氧净化池2内固定有三相分离器,该三相分离器将厌氧净化池的池腔分隔成上下各一个腔室,其中的上腔室内固定有出水堰4,及包围住出水堰4的挡渣板5,下腔室的腔壁上开设有污水进口21,且在下腔室的腔底开设有排泥口22;A three-phase separator is fixed in the anaerobic purification tank 2. The three-phase separator divides the tank cavity of the anaerobic purification tank into an upper and lower chamber. An outlet weir 4 is fixed in the upper chamber and surrounds the outlet water. The slag retaining plate 5 of the weir 4 is provided with a sewage inlet 21 on the wall of the lower chamber, and a mud discharge port 22 is provided at the bottom of the lower chamber;
所述三相分离器由第一分离罩31、第二分离罩32构成,第一分离罩31是一个上下两端开放的倒锥台形的罩体,第二分离罩32是一个向下单向开放的一个锥体形罩体,第二分离罩32固定在第一分离罩31内,第二分离罩32的下沿与第一分离罩31的内壁接合,且在第二分离罩32的下边缘开设有多个过流孔321,各过流孔321沿第二分离罩32的下边缘均匀分布,第二分离罩32的顶部开设有一排气口,该排气口经一排气管322接引至厌氧净化池2外部;The three-phase separator is composed of a first separation cover 31 and a second separation cover 32. The first separation cover 31 is an inverted frustum-shaped cover with open upper and lower ends, and the second separation cover 32 is a downward one-way cover. An open cone-shaped cover, the second separation cover 32 is fixed in the first separation cover 31, the lower edge of the second separation cover 32 is joined with the inner wall of the first separation cover 31, and at the lower edge of the second separation cover 32 A plurality of overflow holes 321 are provided, and each overflow hole 321 is evenly distributed along the lower edge of the second separation cover 32. An exhaust port is provided on the top of the second separation cover 32, and the exhaust port is connected through an exhaust pipe 322. Lead to the outside of the anaerobic purification tank 2;
所述挡渣板5高于三相分离器,挡渣板5与出水堰4之间具有空隙,出水堰4的进水口高于挡渣板5的底边;The slag retaining plate 5 is higher than the three-phase separator, there is a gap between the slag retaining plate 5 and the outlet weir 4, and the water inlet of the outlet weir 4 is higher than the bottom edge of the slag retaining plate 5;
所述提升泵6的进水口经管件接到出水堰4的出水口,提升泵6的泵水口接到布水器7。The water inlet of the lift pump 6 is connected to the water outlet of the water outlet weir 4 through pipe fittings, and the pump water port of the lift pump 6 is connected to the water distributor 7 .
本发明实施例中,所述厌氧净化池2的顶部由一盖板20封闭,所述人工湿地床1安装在盖板20上。In the embodiment of the present invention, the top of the anaerobic purification tank 2 is closed by a cover plate 20, and the artificial wetland bed 1 is installed on the cover plate 20.
本发明实施例中,所述出水堰4内装有液位开关(图中未示),该液位开关接到提升泵6的启停控制端。In the embodiment of the present invention, the water outlet weir 4 is equipped with a liquid level switch (not shown in the figure), and the liquid level switch is connected to the start and stop control end of the lift pump 6 .
本发明实施例中,所述人工湿地床1上种植有湿地植物9,湿地植物可以选取美人蕉、凤眼莲、菩提子、黄色鸢尾、石菖蒲、空心莲子草等植物,这些植物不但能输送氧气到根区,提供根区微生物生长、繁殖和降解对氧的需求,同时也能维持和加强人工湿地系统内的水力传导力,还能对富营养水体中氮、磷有明显去除。In the embodiment of the present invention, wetland plants 9 are planted on the artificial wetland bed 1. The wetland plants can be selected from canna, hyacinthia, linden seed, yellow iris, calamus, hollywort and other plants. These plants can not only transport oxygen To the root zone, it provides the oxygen demand for the growth, reproduction and degradation of microorganisms in the root zone. It can also maintain and enhance the hydraulic conductivity in the artificial wetland system, and can also significantly remove nitrogen and phosphorus in eutrophic water bodies.
本发明实施例中,所述布水器7是均布有多个布水头的水管,所述集水器8是均布有多个向上开放的集水口的水管。In the embodiment of the present invention, the water distributor 7 is a water pipe with a plurality of water distribution heads uniformly distributed, and the water collector 8 is a water pipe with a plurality of upwardly open water collection ports uniformly distributed.
本发明实施例中,所述人工湿地床1由多个介质层从上至下依次层叠而成,各介质层由上到下依次为活性炭粒层、陶粒层、塑料填料层、细砂层、碎石子层,每个介质层的厚度约为15~30cm,活性炭粒用于吸附水中的磷,陶粒用于加强基质通气和加快渗水,塑料填料作为生物膜载体,细砂、碎石子用于填充床体。In the embodiment of the present invention, the artificial wetland bed 1 is composed of multiple media layers stacked in sequence from top to bottom. Each media layer is an activated carbon granular layer, a ceramsite layer, a plastic filler layer, and a fine sand layer from top to bottom. , gravel sub-layer, the thickness of each medium layer is about 15-30cm, activated carbon particles are used to absorb phosphorus in the water, ceramsite is used to strengthen matrix ventilation and accelerate water seepage, plastic fillers are used as biofilm carriers, fine sand, gravel used to fill the bed.
本发明实施例适用于污水处理,具体处理方法如下:The embodiments of the present invention are suitable for sewage treatment. The specific treatment methods are as follows:
污水通过污水进口21进入厌氧净化池2,进行沉淀及厌氧反应,沉淀及反应一段时间后,固、液、气三相混合物就会在厌氧净化池内上升,三相混合物上升至三相分离器处时,在三相分离器的拦截下进行固、液、气三相分离,大部分的固体被拦截在厌氧净化池的下腔室内逐渐沉淀,最后通过排泥口22排出,大部分的气体则聚积在第二分离罩32的顶部,并通过排气管322排出(排出的气体通常富含沼气,可以当燃气使用),水体则通过第二分离罩32下边缘的各个过流孔321流入厌氧净化池的上腔室,然后再经挡渣板5拦截掉液面的渣质后流入出水堰4,出水堰4内的水位到达设定值时,出水堰4内的液位开关闭合,从而控制提升泵6启动,使得出水堰4内的水体在提升泵6的作用下进入布水器7,由布水器7喷洒在人工湿地床1的表层,然后在人工湿地床1内向下渗滤,并在向下渗滤过程中被人工湿地床净化,净化后的水体由集水器8汇集后排出;当出水堰4内的水位低于设定值时,出水堰4内的液位开关断开,从而控制提升泵6停止运行。The sewage enters the anaerobic purification tank 2 through the sewage inlet 21 and undergoes precipitation and anaerobic reaction. After precipitation and reaction for a period of time, the three-phase mixture of solid, liquid and gas will rise in the anaerobic purification tank, and the three-phase mixture will rise to the three-phase At the separator, solid, liquid and gas are separated into three phases under the interception of the three-phase separator. Most of the solids are intercepted and gradually settle in the lower chamber of the anaerobic purification tank, and are finally discharged through the mud discharge port 22. Part of the gas accumulates on the top of the second separation cover 32 and is discharged through the exhaust pipe 322 (the exhausted gas is usually rich in biogas and can be used as gas), and the water passes through the various overflows on the lower edge of the second separation cover 32 The hole 321 flows into the upper chamber of the anaerobic purification tank, and then intercepts the slag on the liquid level through the slag baffle 5 and then flows into the outlet weir 4. When the water level in the outlet weir 4 reaches the set value, the liquid in the outlet weir 4 The position switch is closed, thereby controlling the start of the lift pump 6, so that the water in the outlet weir 4 enters the water distributor 7 under the action of the lift pump 6, and is sprayed by the water distributor 7 on the surface of the constructed wetland bed 1, and then in the constructed wetland bed 1 It percolates downward and is purified by the artificial wetland bed during the downward percolation process. The purified water body is collected by the water collector 8 and then discharged; when the water level in the outlet weir 4 is lower than the set value, the water in the outlet weir 4 The liquid level switch is disconnected, thereby controlling the lifting pump 6 to stop running.
Claims (4)
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CN202465382U (en) * | 2012-02-29 | 2012-10-03 | 中国石油化工股份有限公司 | Three-phase separator and cylindrical anaerobic reactor |
CN203582580U (en) * | 2013-09-27 | 2014-05-07 | 广西博世科环保科技股份有限公司 | Multi-stage treatment anaerobic reactor capable of separating inorganic sludge |
CN103880178A (en) * | 2014-03-07 | 2014-06-25 | 许中华 | Multistage gas stripping and separating integrated anaerobic treatment device |
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CN101318756A (en) * | 2008-06-07 | 2008-12-10 | 湖南鸿达环保设备制造有限公司 | Tridimensional oligodynamic wastewater treatment facilities |
CN101774688A (en) * | 2009-01-09 | 2010-07-14 | 上海博丹环境工程技术有限公司 | Anaerobic reactor for treating high-concentration chemical industry sewage |
CN204058202U (en) * | 2014-10-13 | 2014-12-31 | 杜丹 | A kind of unpowered domestic sewage processing system |
CN205151908U (en) * | 2015-10-27 | 2016-04-13 | 浙江达人环保科技股份有限公司 | Constructed wetland sewage treatment system integrates |
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EP0493727A1 (en) * | 1990-12-29 | 1992-07-08 | PWA INDUSTRIEPAPIER GmbH | Reactor and process for the continuous mechanical and anaerobic biological purification of waste water containing solids |
CN202465382U (en) * | 2012-02-29 | 2012-10-03 | 中国石油化工股份有限公司 | Three-phase separator and cylindrical anaerobic reactor |
CN203582580U (en) * | 2013-09-27 | 2014-05-07 | 广西博世科环保科技股份有限公司 | Multi-stage treatment anaerobic reactor capable of separating inorganic sludge |
CN103880178A (en) * | 2014-03-07 | 2014-06-25 | 许中华 | Multistage gas stripping and separating integrated anaerobic treatment device |
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Denomination of invention: Anaerobic purification tank Granted publication date: 20230908 Pledgee: Zhejiang Zhoushan Dinghai Ocean Rural Commercial Bank Co.,Ltd. Pledgor: ZHEJIANG DAREN ENVIRONMENTAL PROTECTION TECHNOLOGY Co.,Ltd. Registration number: Y2024330002080 |