CN116282529A - Post sulfur autotrophic nitrogen removal integrated domestic sewage treatment equipment - Google Patents

Post sulfur autotrophic nitrogen removal integrated domestic sewage treatment equipment Download PDF

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CN116282529A
CN116282529A CN202211596219.3A CN202211596219A CN116282529A CN 116282529 A CN116282529 A CN 116282529A CN 202211596219 A CN202211596219 A CN 202211596219A CN 116282529 A CN116282529 A CN 116282529A
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周磊
吕海东
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SHANDONG DAYU WATER TREATMENT CO Ltd
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    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
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Abstract

The invention relates to a post-sulfur autotrophic nitrogen removal integrated domestic sewage treatment device which consists of a hydrolysis acidification area, a contact oxidation area, a high-efficiency sedimentation area, a post-sulfur autotrophic nitrogen removal filter tank and other units, and is supplemented with an aeration device, MBBR biological filler, sulfur autotrophic filter tank biological filler, a filter tank supporting layer, a backwashing back-flushing system, a high-efficiency inclined pipe filler and the like, wherein the high-efficiency sedimentation area is used for performing mud-water separation, and the post-sulfur autotrophic nitrogen removal filter tank is used for removing total nitrogen, so that an additional carbon source is not needed, and the device is high in efficiency, energy-saving and environment-friendly, simple to manufacture, convenient to install and small in occupied area; the method is suitable for treating domestic sewage with lower C/N ratio, has stable denitrification effect, avoids the dependence of a denitrification system on an external carbon source, can stably discharge the treated sewage up to the standard, and can also be reused for greening irrigation and the like.

Description

一种后置硫自养脱氮一体化生活污水处理设备A post-installed sulfur autotrophic denitrification integrated domestic sewage treatment equipment

技术领域technical field

本发明涉及生活污水处理技术领域,特别涉及一种后置硫自养脱氮一体化生活污水处理设备。The invention relates to the technical field of domestic sewage treatment, in particular to a post-installed sulfur autotrophic denitrification integrated domestic sewage treatment equipment.

背景技术Background technique

生物脱氮技术是通过反硝化反应,即硝态氮和亚硝态氮在反硝化菌的作用下,被还原成气态氮的过程,可分为异养反硝化和自养反硝化两种。对一些低C/N比废水如地下水、城市污水厂二级出水、酸洗清洗废水等,有机碳源不足,需要投加碳源(甲醇、葡萄糖、乙酸钠等)为异养反硝化提供电子供体及能量。其缺点是:增加了碳源池,其成本高、脱氮效率低。当前大多生活污水都经过化粪池处理,部分BOD会被消解,造成污水的C/N(即碳氮比)比较低,目前市场上一体化污水处理设备主要采用传统设备,比如A/O、A2/O等工艺及其变型工艺等等,均采用异养反硝化技术。此类工艺在小规模污水处理工况下,脱氮的弊端就显现出来。Biological denitrification technology is a process in which nitrate nitrogen and nitrite nitrogen are reduced to gaseous nitrogen under the action of denitrifying bacteria through denitrification reaction, which can be divided into heterotrophic denitrification and autotrophic denitrification. For some waste water with low C/N ratio, such as groundwater, secondary effluent of urban sewage plants, pickling cleaning waste water, etc., the organic carbon source is insufficient, and it is necessary to add carbon source (methanol, glucose, sodium acetate, etc.) to provide electrons for heterotrophic denitrification. donor and energy. Its disadvantages are: the carbon source pool is increased, its cost is high, and the denitrification efficiency is low. At present, most domestic sewage is treated by septic tanks, and part of BOD will be digested, resulting in relatively low C/N (i.e. carbon-to-nitrogen ratio) of sewage. Currently, integrated sewage treatment equipment on the market mainly adopts traditional equipment, such as A/O, Processes such as A 2 /O and its variant processes, etc., all use heterotrophic denitrification technology. The disadvantages of denitrification of this kind of process appear in the case of small-scale sewage treatment.

主要缺陷为:第一,一体化设备的特点是集成性,设备小巧,但是在脱氮处理时需要大量的硝化液回流,需要保证污水处理的停留时间,因此需要保证设备容积达到设计参数,两者在实际情况存在较大的矛盾;第二,为保证C/N达到4:1以上,需要外加碳源,需要附设碳源投加设备,一方面电能、药剂等用量增高,另一方面需要精确核算投加量,才能保证C/N达到设定范围,市场上大部分一体化设备的脱氮效果不稳定,效率较低。The main defects are as follows: First, the integrated equipment is characterized by integration and compact equipment, but it requires a large amount of nitrifying liquid to return during denitrification treatment, and it is necessary to ensure the residence time of sewage treatment, so it is necessary to ensure that the volume of the equipment reaches the design parameters. The latter has a big contradiction in the actual situation; second, in order to ensure that the C/N ratio reaches more than 4:1, an external carbon source is required, and additional carbon source dosing equipment is required. Accurate calculation of the dosage can ensure that the C/N reaches the set range. The denitrification effect of most integrated equipment on the market is unstable and the efficiency is low.

本发明为一种采用自养反硝化技术脱氮的一体化设备,脱氮效率高、运行成本低。The invention is an integrated equipment for denitrification using autotrophic denitrification technology, which has high denitrification efficiency and low operation cost.

发明内容Contents of the invention

为了解决上述技术问题,本发明为一种后置硫自养脱氮一体化生活污水处理设备,其技术方案为:In order to solve the above-mentioned technical problems, the present invention is a post-installed sulfur autotrophic denitrification integrated domestic sewage treatment equipment, and its technical solution is:

包括水解酸化区、接触氧化区、高效沉淀区和后置硫自养脱氮滤池,污水通过进水口依次经过水解酸化区、接触氧化区、高效沉淀区和后置硫自养脱氮滤池,水解酸化区和接触氧化区之间通过隔板隔开,且其底部相通,接触氧化区的出液口设置在接触氧化区的右侧上部,并与中心导流筒的入液口相连,中心导流筒的出液口竖直向下;Including hydrolytic acidification zone, contact oxidation zone, high-efficiency precipitation zone and post-installed sulfur autotrophic denitrification filter, the sewage passes through the water inlet in sequence through hydrolytic acidification zone, contact oxidation zone, high-efficiency precipitation zone and post-installed sulfur autotrophic denitrification filter , the hydrolytic acidification zone and the contact oxidation zone are separated by a partition, and their bottoms are connected. The liquid outlet of the contact oxidation zone is set on the upper right side of the contact oxidation zone, and is connected with the liquid inlet of the central guide tube. The liquid outlet of the central guide tube is vertically downward;

高效沉淀区与后置硫自养脱氮滤池之间的入液口设置在高效沉淀区右侧上部,入液口与滤池V形布水槽相连;在高效沉淀区底部设有污泥回流管路回连至水解酸化区;The liquid inlet between the high-efficiency sedimentation area and the rear sulfur autotrophic denitrification filter is set on the upper right side of the high-efficiency sedimentation area, and the liquid inlet is connected to the V-shaped distribution tank of the filter; there is a sludge return at the bottom of the high-efficiency sedimentation area The pipeline is connected back to the hydrolytic acidification area;

在后置硫自养脱氮滤池中,从上至下依次为滤池反洗集水槽、滤池V形布水槽、硫自养滤池生物填料和滤池承托层;在滤池反洗集水槽右侧设有回流管路回连至水解酸化区;In the rear sulfur autotrophic denitrification filter, from top to bottom are filter backwash sump, filter V-shaped distribution tank, sulfur autotrophic filter biological filler and filter support layer; On the right side of the washing sump, there is a return pipeline connected to the hydrolytic acidification area;

在后置硫自养脱氮滤池内底部设有反洗水入口和空气入口,空气输送管路分别与接触氧化区底部的空气入口和后置硫自养脱氮滤池的空气入口相连;A backwash water inlet and an air inlet are provided at the inner bottom of the rear sulfur autotrophic denitrification filter, and the air delivery pipeline is respectively connected with the air inlet at the bottom of the contact oxidation zone and the air inlet of the rear sulfur autotrophic denitrification filter;

在水解酸化区、接触氧化区、高效沉淀区和后置硫自养脱氮滤池内分别填充生物填料。Biological fillers are respectively filled in the hydrolytic acidification zone, contact oxidation zone, high-efficiency precipitation zone and post sulfur autotrophic denitrification filter.

进一步地,在后置硫自养脱氮滤池下部右侧设有出水口。Further, a water outlet is provided on the right side of the lower part of the rear sulfur autotrophic denitrification filter.

进一步地,所述高效沉淀区内底部为污泥斗,污泥斗底部为漏斗式排污口,中心导流筒的顶部固定在设备内顶部,中心导流筒筒体竖直向下,且一侧开口与接触氧化区出液口相连,筒体底部开口向下,从接触氧化区至中心导流筒内物质从污泥斗流出;在高效沉淀区内中部还设有斜管填料。Further, the bottom of the high-efficiency sedimentation zone is a sludge hopper, and the bottom of the sludge hopper is a funnel-type sewage outlet. The top of the central guide tube is fixed on the top of the equipment, and the center guide tube is vertically downward, and a The side opening is connected to the liquid outlet of the contact oxidation zone, and the bottom opening of the cylinder is downward, from the contact oxidation zone to the central guide tube, the material in the guide tube flows out from the sludge hopper; in the middle of the high-efficiency sedimentation zone, there is also an inclined tube filler.

进一步地,在接触氧化区内底部设有曝气装置。Further, an aeration device is provided at the bottom of the contact oxidation zone.

进一步地,接触氧化区与高效沉淀区之间、高效沉淀区与后置硫自养脱氮滤池之间分别通过隔板隔开,且其上部分别相通。Further, the contact oxidation zone and the high-efficiency precipitation zone, and the high-efficiency precipitation zone and the post-installed sulfur autotrophic denitrification filter are respectively separated by partitions, and the upper parts thereof communicate with each other.

进一步地,所述水解酸化区为缺氧区。Further, the hydrolytic acidification zone is an anoxic zone.

本发明的有益效果为:本发明为一种后置硫自养脱氮一体化生活污水处理设备,由水解酸化区、接触氧化区、高效沉淀区和后置硫自养脱氮滤池等单元组成,辅以曝气装置、MBBR生物填料、硫自养滤池生物填料、滤池承托层以及反洗反吹系统和高效斜管填料等,高效沉淀区进行泥水分离,采用后置硫自养脱氮滤池进行总氮的脱除,无需外加碳源,效率高,节能,环保,本发明具有制作简单、安装方便、占地面积小;适合C/N比较低生活污水的处理,脱氮效果稳定,避免脱氮系统对外加碳源的依赖,处理后的污水可以稳定达标排放,也可回用于绿化灌溉等。The beneficial effects of the present invention are: the present invention is a post-installed sulfur autotrophic denitrification integrated domestic sewage treatment equipment, which consists of hydrolysis acidification area, contact oxidation area, high-efficiency precipitation area and post-installed sulfur autotrophic denitrification filter. Composition, supplemented by aeration device, MBBR biological filler, sulfur autotrophic filter biological filler, filter support layer, backwashing and blowing system and high-efficiency inclined tube filler, etc., the high-efficiency sedimentation zone is used for mud-water separation, and the post-set sulfur autotrophic filter is used The denitrification filter is used for the removal of total nitrogen without additional carbon source, high efficiency, energy saving, and environmental protection. The nitrogen effect is stable, avoiding the dependence of the denitrification system on external carbon sources, and the treated sewage can be stably discharged up to the standard, and can also be reused for green irrigation.

附图说明Description of drawings

图1为本发明结构示意图;Fig. 1 is a structural representation of the present invention;

如图所示,1进水口,2水解酸化区,3接触氧化区,4高效沉淀区,5后置硫自养脱氮滤池,6斜管填料,7中心导流筒,8曝气装置,9MBBR生物填料,10硫自养滤池生物填料,11滤池承托层,12滤池V形布水槽,13滤池反洗集水槽,14出水口,15反洗进水,16空气输送管路,17 滤池反洗水回流管路,18 污泥回流管路,19污泥回流泵,20进气泵,21内回流泵。As shown in the figure, 1 water inlet, 2 hydrolytic acidification zone, 3 contact oxidation zone, 4 high-efficiency sedimentation zone, 5 rear sulfur autotrophic denitrification filter, 6 inclined tube packing, 7 central guide tube, 8 aeration device , 9MBBR biological filler, 10 sulfur autotrophic filter biological filler, 11 filter support layer, 12 filter V-shaped cloth sink, 13 filter backwash sump, 14 water outlet, 15 backwash water inlet, 16 air delivery Pipeline, 17 filter tank backwash water return pipeline, 18 sludge return pipeline, 19 sludge return pump, 20 intake pump, 21 internal return pump.

具体实施方式Detailed ways

如图所示,本发明为一种后置硫自养脱氮一体化生活污水处理设备,包括水解酸化区2(即为缺氧区)、接触氧化区3、高效沉淀区4和后置硫自养脱氮滤池5,污水通过进水口依次经过水解酸化区、接触氧化区、高效沉淀区和后置硫自养脱氮滤池,水解酸化区和接触氧化区均采用MBBR生物填料9替代传统的弹性填料、组合填料等,其比表面积大、亲水性好、生物活性高、挂膜快、处理效果好、使用寿命长,较小的曝气或搅拌即可实现流化。载体内部不断形成连续梯度溶氧梯度,实现同步硝化反硝化,及短程反硝化。As shown in the figure, the present invention is a post-installed sulfur autotrophic denitrification integrated domestic sewage treatment equipment, including hydrolytic acidification zone 2 (that is, anoxic zone), contact oxidation zone 3, high-efficiency precipitation zone 4 and post-sulfurization zone Autotrophic denitrification filter 5, the sewage passes through the water inlet successively through the hydrolytic acidification zone, contact oxidation zone, high-efficiency sedimentation zone and post-installed sulfur autotrophic denitrification filter. Both the hydrolysis acidification zone and the contact oxidation zone are replaced by MBBR biological filler 9 Traditional elastic fillers, combined fillers, etc. have large specific surface area, good hydrophilicity, high biological activity, fast film formation, good treatment effect, long service life, and fluidization can be achieved with small aeration or stirring. A continuous gradient dissolved oxygen gradient is continuously formed inside the carrier to realize synchronous nitrification and denitrification and short-range denitrification.

水解酸化区和接触氧化区之间通过隔板隔开,且其底部相通。在接触氧化区内底部设有曝气装置,曝气头采用旋混曝气器,通过多层螺旋切割的形式进行充氧曝气,气流多层切割,形成微气泡,提高了氧的利用率,具有曝气均匀,充氧效率高的特点。The hydrolytic acidification zone and the contact oxidation zone are separated by a partition, and their bottoms are connected. There is an aeration device at the bottom of the contact oxidation zone. The aeration head adopts a rotary aerator, which performs oxygenation and aeration in the form of multi-layer spiral cutting. The air flow is cut in multiple layers to form micro-bubbles and improve the utilization rate of oxygen. , has the characteristics of uniform aeration and high oxygenation efficiency.

接触氧化区与高效沉淀区之间、高效沉淀区与后置硫自养脱氮滤池之间分别通过隔板隔开,且其上部分别通过管路相通。The contact oxidation zone and the high-efficiency precipitation zone, and the high-efficiency precipitation zone and the post-installed sulfur autotrophic denitrification filter are respectively separated by partitions, and the upper parts thereof are communicated with each other through pipelines.

高效沉淀区内底部为污泥斗,污泥斗底部为漏斗式排污口,排污口处设有污泥回流管路18,该管路上安装污泥回流泵19,污泥回流管路回连至水解酸化区入口。高效沉淀区的顶部纵向布置中心导流筒7,中心导流筒的一侧与接触氧化区出液口相连,中心导流筒的顶部固定在设备内顶部,中心导流筒的底部开口,该开口与污泥斗相通,从接触氧化区流入中心导流筒内物质从污泥斗排污口流至污泥回流管路,至水解酸化区;高效沉淀池内中部布置斜管填料6,污泥斗的上方0.6-1米处,斜管填料的高度约0.88米,用于过滤。采用竖流沉淀池的中心筒布水方式以及泥斗设计结合斜管沉淀池的蜂窝状斜管填料,类似简化版的高密度沉淀池,能够大幅提高沉淀池表面负荷,降低沉淀池容积,从而实现整体设备体积减低,降低制造成本。The bottom of the high-efficiency sedimentation area is a sludge hopper, and the bottom of the sludge hopper is a funnel-type sewage outlet. A sludge return pipeline 18 is arranged at the sewage outlet. A sludge return pump 19 is installed on the pipeline, and the sludge return pipeline is connected to Entrance to the hydrolytic acidification zone. The top of the high-efficiency sedimentation zone is longitudinally arranged with a center guide cylinder 7, one side of the center guide cylinder is connected to the liquid outlet of the contact oxidation zone, the top of the center guide cylinder is fixed on the top of the equipment, and the bottom of the center guide cylinder is open. The opening communicates with the sludge hopper, and the material flowing into the central guide tube from the contact oxidation zone flows from the sludge hopper sewage outlet to the sludge return pipeline to the hydrolysis and acidification zone; the inclined pipe filler 6 is arranged in the middle of the high-efficiency sedimentation tank, and the sludge hopper 0.6-1 meter above the top, the height of the inclined tube packing is about 0.88 meters, which is used for filtration. The central tube water distribution method of the vertical flow sedimentation tank and the design of the mud bucket combined with the honeycomb inclined tube filler of the inclined tube sedimentation tank are similar to the simplified version of the high-density sedimentation tank, which can greatly increase the surface load of the sedimentation tank and reduce the volume of the sedimentation tank, thereby Realize the volume reduction of the overall equipment and reduce the manufacturing cost.

在后置硫自养脱氮滤池上方设有回流管路17,回流管路的入口与后置硫自养脱氮滤池相连,出口与水解酸化区相连;该管路上设有内回流泵21。在后置硫自养脱氮滤池内从上至下依次布置滤池反洗集水槽、滤池V形布水槽、硫自养滤池生物填料和滤池承托层。A return pipeline 17 is arranged above the rear sulfur autotrophic denitrification filter, the inlet of the return pipeline is connected with the rear sulfur autotrophic denitrification filter, and the outlet is connected with the hydrolytic acidification area; an internal return pump is provided on the pipeline twenty one. In the rear sulfur autotrophic denitrification filter, the filter backwash sump, the filter V-shaped distribution tank, the sulfur autotrophic filter biological filler and the filter supporting layer are arranged in sequence from top to bottom.

硫自养滤池生物填料安装在承托层以上,填料高度约1.2米;采用S/Fe硫自养生物填料;水力负荷设计值取0.5-3m3/m2·h;控制pH在7-8;溶解氧小于0.5mg/L。硫自养滤池生物填料10上面依次布置滤池V形滤水槽10和滤池反洗集水槽13,硫自养滤池生物填料内含有S 2 - 、Fe、Fe 2+等元素,N与该部分元素进行化学反应,N被有效还原,适合C/N比较低生活污水的处理,脱氮效果稳定,避免脱氮系统对外加碳源的依赖,处理后的污水可以稳定达标排放,也可回用于绿化灌溉等。在后置硫自养脱氮滤池下部一侧设有出水口14,出水口上面横向铺设滤池承托层11,该层上布置有滤板和滤头等,用于将填料拦住,滤池承托层拦住填料,液体从滤池承托层向下渗出。The sulfur autotrophic filter biological filler is installed above the supporting layer, and the filler height is about 1.2 meters; S/Fe sulfur autotrophic biological filler is used; the hydraulic load design value is 0.5-3m3/m2 h; the pH is controlled at 7-8; Dissolved oxygen is less than 0.5mg/L. The V-shaped filter water tank 10 of the filter and the filter backwash sump 13 are sequentially arranged on the biofiller 10 of the sulfur autotrophic filter. This part of the elements reacts chemically, and N is effectively reduced. It is suitable for the treatment of domestic sewage with low C/N ratio. The denitrification effect is stable, and the denitrification system is avoided. Reuse for green irrigation, etc. A water outlet 14 is provided on the lower side of the rear sulfur autotrophic denitrification filter, and a filter supporting layer 11 is laid horizontally above the water outlet, and filter plates and filter heads are arranged on this layer to block the filler, and the filter The support layer holds the packing, and the liquid seeps downward from the filter support layer.

在后置硫自养脱氮滤池内底部设有反洗水入口和空气入口,空气输送管路16分别与接触氧化区底部的空气入口和后置硫自养脱氮滤池的空气入口相连,反洗进水与反洗水入口相连。后置硫自养脱氮滤池滤料采用专用滤料,其所含所含的物质,如S 2 - 、Fe、Fe 2+等,作为硝酸盐还原的电子供体,被自养反硝化菌利用而最终转化成气态氮,从而实现总氮的脱除;该自养反硝化过程无需外加有机碳源。A backwash water inlet and an air inlet are provided at the inner bottom of the rear sulfur autotrophic denitrification filter, and the air delivery pipeline 16 is respectively connected with the air inlet at the bottom of the contact oxidation zone and the air inlet of the rear sulfur autotrophic denitrification filter , the backwash inlet water is connected with the backwash water inlet. The post-installed sulfur autotrophic denitrification filter uses a special filter material, and the substances contained in it, such as S 2 - , Fe, Fe 2+ , etc., are used as electron donors for nitrate reduction and are denitrified by autotrophic denitrification Bacteria use and finally converted into gaseous nitrogen, so as to achieve the removal of total nitrogen; the autotrophic denitrification process does not require additional organic carbon sources.

本发明采用PLC自动化控制,各液位、流量传感器通过4-20mA信号传输,在预设的PLC程序下,自动控制进水泵、曝气系统、回流泵、污泥泵、硫自养滤池的反洗进出水、空气反洗等个动力单元及自动阀门的启停。实现全程自动控制操作,自动化程度高,同时设有移动物联网网关,实现远程操控、数据传输等。The invention adopts PLC automatic control, and each liquid level and flow sensor transmits 4-20mA signals, and automatically controls the water inlet pump, aeration system, return pump, sludge pump, and sulfur autotrophic filter under the preset PLC program. Start and stop of power units such as backwashing water in and out, air backwashing, and automatic valves. Realize the whole process of automatic control operation, with a high degree of automation. At the same time, it is equipped with a mobile Internet of Things gateway to realize remote control and data transmission.

本发明工作过程:Working process of the present invention:

污水由进水口(1-进水口)进入一体化反应装置,分别通过2-水解酸化区(控制溶解氧浓度接近于0mg/L)、3-接触氧化区(控制溶解氧浓度2-3mg/L)进行第一级生化反应,在4-高效沉淀区进行泥水分离(控制污泥回流比50%-100%),出水自流经过12-滤池V形布水槽进入5-后置硫自养脱氮滤池,滤池的自养反硝化菌利用10-硫自养滤池生物填料中所含的物质,如S 2 - 、Fe、Fe 2+等,作为硝酸盐还原的电子供体,最终转化成气态氮,从而实现总氮的脱除;该自养反硝化过程无需外加有机碳源;5-后置硫自养脱氮滤池出水进入清水池;反洗时反洗水、空气分别由15-反洗进水、16-空气输送管路按照PLC设定的程序进行,反洗出水由13-滤池反洗集水槽收集,经17 滤池反洗水回流管路回流至2-水解酸化区。The sewage enters the integrated reaction device from the water inlet (1-water inlet), and passes through the 2-hydrolysis acidification zone (control the dissolved oxygen concentration close to 0mg/L), and the 3-contact oxidation zone (control the dissolved oxygen concentration 2-3mg/L ) to carry out the first-stage biochemical reaction, and carry out mud-water separation in the 4-high-efficiency sedimentation zone (control the sludge return ratio of 50%-100%), and the effluent flows through the 12-filter V-shaped distribution tank into the 5-post autotrophic desulfurization Nitrogen filter, the autotrophic denitrifying bacteria in the filter use the substances contained in the biological filler of the 10-sulfur autotrophic filter, such as S 2 - , Fe, Fe 2+ , etc., as electron donors for nitrate reduction, and finally converted into gaseous nitrogen, thereby realizing the removal of total nitrogen; the autotrophic denitrification process does not require additional organic carbon sources; The 15-backwash water inlet and 16-air delivery pipeline are carried out according to the program set by the PLC, and the backwash effluent is collected by the 13-filter backwash sump, and returned to 2- through the 17-filter backwash water return pipeline Hydrolytic acidification zone.

本发明为一种后置硫自养脱氮一体化生活污水处理设备,整体采用碳钢制作,撬装式安装,设备制作简单、占地面积小、安装使用简捷、对总氮的脱除效果稳定、高效。各部件之间都是连通的,只是各部件之间用钢板隔开,污水由前一个装置自流进入下一个装置。本发明由水解酸化区、接触氧化区、高效沉淀区和后置硫自养脱氮滤池等单元组成,辅以曝气装置、MBBR生物填料、硫自养滤池生物填料、滤池承托层以及反洗反吹系统和高效斜管填料等,采用后置反硝化,取消前置反硝化,不单独设置硝化液回流装置,提高系统停留时间。后置反硝化采用硫自养脱氮滤池进行总氮的脱除,无需外加碳源,效率高,节能,环保,高效沉淀区进行泥水分离,本发明具有制作简单、安装方便、占地面积小;适合C/N比较低生活污水的处理,脱氮效果稳定,避免脱氮系统对外加碳源的依赖,处理后的污水可以稳定达标排放,也可回用于绿化灌溉等。The invention is a post-installed sulfur autotrophic denitrification integrated domestic sewage treatment equipment, which is made of carbon steel as a whole and installed in a skid-mounted manner. The equipment is simple to manufacture, occupies a small area, is simple to install and use, and has a good removal effect on total nitrogen. Stable and efficient. The components are all connected, but the components are separated by steel plates, and the sewage flows from the previous device to the next device. The invention is composed of hydrolysis acidification zone, contact oxidation zone, high-efficiency sedimentation zone and rear sulfur autotrophic denitrification filter, supplemented by aeration device, MBBR biological filler, sulfur autotrophic filter biological filler, filter support Layer, backwashing and blowing system and high-efficiency inclined tube packing, etc., adopt post-denitrification, cancel pre-denitrification, and do not set up a nitrifying liquid return device separately to increase the system residence time. Post-denitrification adopts sulfur autotrophic denitrification filter to remove total nitrogen, no need to add carbon source, high efficiency, energy saving, environmental protection, high-efficiency sedimentation zone for mud-water separation, the present invention has the advantages of simple manufacture, convenient installation, and small footprint Small; suitable for the treatment of domestic sewage with low C/N ratio, the denitrification effect is stable, avoiding the dependence of the denitrification system on external carbon sources, and the treated sewage can be stably discharged up to the standard, and can also be reused for green irrigation.

以上所述只是本发明的较佳实施方式,但本发明并不限于上述实施例,只要其以任何相同或相似手段达到本发明的技术效果,都应落入本发明的保护范围之内。The above description is only a preferred embodiment of the present invention, but the present invention is not limited to the above examples, as long as it achieves the technical effect of the present invention by any same or similar means, it should fall within the protection scope of the present invention.

Claims (6)

1. The integrated domestic sewage treatment equipment for the rear-mounted sulfur autotrophic nitrogen removal comprises a hydrolysis acidification area, a contact oxidation area, a high-efficiency sedimentation area and a rear-mounted sulfur autotrophic nitrogen removal filter tank, wherein sewage sequentially passes through the hydrolysis acidification area, the contact oxidation area, the high-efficiency sedimentation area and the rear-mounted sulfur autotrophic nitrogen removal filter tank through a water inlet, the hydrolysis acidification area and the contact oxidation area are separated by a partition plate, and the bottoms of the hydrolysis acidification area and the contact oxidation area are communicated, and the integrated domestic sewage treatment equipment is characterized in that a liquid outlet of the contact oxidation area is arranged at the upper right side of the contact oxidation area and is connected with a liquid inlet of a central guide cylinder, and a liquid outlet of the central guide cylinder is vertically downward;
a liquid inlet between the high-efficiency sedimentation area and the rear sulfur autotrophic denitrification filter is arranged at the upper right side of the high-efficiency sedimentation area, and is connected with a V-shaped water distribution groove of the filter; a sludge return pipeline is arranged at the bottom of the efficient sedimentation zone and is connected back to the hydrolysis acidification zone;
in the postpositive sulfur autotrophic denitrification filter, a filter backwash water collecting tank, a filter V-shaped water distribution tank, a sulfur autotrophic filter biological filler and a filter supporting layer are sequentially arranged from top to bottom; a return pipeline is arranged on the right side of the backwash water collecting tank of the filter tank and is connected back to the hydrolysis acidification area;
the bottom in the post sulfur autotrophic nitrogen removal filter is provided with a backwash water inlet and an air inlet, and an air conveying pipeline is respectively connected with the air inlet at the bottom of the contact oxidation zone and the air inlet of the post sulfur autotrophic nitrogen removal filter;
biological fillers are respectively filled in the hydrolysis acidification area, the contact oxidation area, the high-efficiency sedimentation area and the post sulfur autotrophic denitrification filter.
2. The post-sulfur autotrophic nitrogen removal integrated domestic sewage treatment device according to claim 1, wherein a water outlet is arranged on the right side of the lower part of the post-sulfur autotrophic nitrogen removal filter tank.
3. The post-sulfur autotrophic nitrogen removal integrated domestic sewage treatment device according to claim 1, wherein the bottom in the efficient sedimentation area is a sludge hopper, the bottom of the sludge hopper is a funnel-shaped sewage outlet, the top of the central guide cylinder is fixed at the inner top of the device, the cylinder body of the central guide cylinder is vertically downward, one side of the cylinder body is connected with the liquid outlet of the contact oxidation area, the opening at the bottom of the cylinder body is downward, and substances in the cylinder body from the contact oxidation area to the central guide cylinder flow out of the sludge hopper; and the middle part in the efficient sedimentation zone is also provided with a pipe chute filler.
4. The post-sulfur autotrophic nitrogen-removing integrated domestic sewage treatment apparatus according to claim 1, wherein an aeration device is provided at the bottom in the contact oxidation zone.
5. The post-sulfur autotrophic nitrogen removal integrated domestic sewage treatment device according to claim 1, wherein the contact oxidation area and the high-efficiency sedimentation area, the high-efficiency sedimentation area and the post-sulfur autotrophic nitrogen removal filter are respectively separated by a partition plate, and the upper parts of the contact oxidation area and the high-efficiency sedimentation area are respectively communicated.
6. The post sulfur autotrophic nitrogen removal integrated domestic sewage treatment apparatus of claim 1, wherein said hydrolytic acidification zone is an anoxic zone.
CN202211596219.3A 2022-12-12 2022-12-12 Post sulfur autotrophic nitrogen removal integrated domestic sewage treatment equipment Pending CN116282529A (en)

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Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN202089872U (en) * 2011-06-13 2011-12-28 苏州微体电子科技有限公司 Comprehensive waste water purifying apparatus
WO2018107740A1 (en) * 2016-12-14 2018-06-21 江南大学 Wastewater nitrogen and phosphorus removal device and application thereof
CN111422984A (en) * 2020-03-16 2020-07-17 四川省科学城天人环保有限公司 An IFAS-AOAS integrated sewage treatment device and its process
CN215049474U (en) * 2021-01-26 2021-12-07 中持水务股份有限公司 Centralized sewage treatment facility
WO2022160563A1 (en) * 2021-01-28 2022-08-04 北京坦思环保科技有限公司 Apparatus and method for deep removal of nitrogen from industrial wastewater by means of anaerobic ammonium oxidation

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN202089872U (en) * 2011-06-13 2011-12-28 苏州微体电子科技有限公司 Comprehensive waste water purifying apparatus
WO2018107740A1 (en) * 2016-12-14 2018-06-21 江南大学 Wastewater nitrogen and phosphorus removal device and application thereof
CN111422984A (en) * 2020-03-16 2020-07-17 四川省科学城天人环保有限公司 An IFAS-AOAS integrated sewage treatment device and its process
CN215049474U (en) * 2021-01-26 2021-12-07 中持水务股份有限公司 Centralized sewage treatment facility
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