CN209481417U - A farming wastewater treatment system - Google Patents
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- 238000004065 wastewater treatment Methods 0.000 title claims abstract description 28
- 238000009313 farming Methods 0.000 title 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 86
- 239000007788 liquid Substances 0.000 claims abstract description 39
- 239000010802 sludge Substances 0.000 claims abstract description 36
- 238000004062 sedimentation Methods 0.000 claims abstract description 35
- 238000000926 separation method Methods 0.000 claims abstract description 31
- 238000009360 aquaculture Methods 0.000 claims abstract description 23
- 244000144974 aquaculture Species 0.000 claims abstract description 23
- 230000033228 biological regulation Effects 0.000 claims abstract description 15
- 238000009395 breeding Methods 0.000 claims abstract description 11
- 230000001488 breeding effect Effects 0.000 claims abstract description 11
- 230000005484 gravity Effects 0.000 claims abstract description 10
- 239000002699 waste material Substances 0.000 claims abstract description 4
- 239000010865 sewage Substances 0.000 claims description 32
- 230000008719 thickening Effects 0.000 claims description 20
- 238000003756 stirring Methods 0.000 claims description 14
- 238000004659 sterilization and disinfection Methods 0.000 claims description 10
- 230000003139 buffering effect Effects 0.000 claims description 5
- 239000000706 filtrate Substances 0.000 claims description 5
- 230000001105 regulatory effect Effects 0.000 claims description 5
- 239000000645 desinfectant Substances 0.000 claims description 3
- 238000002156 mixing Methods 0.000 claims description 3
- 238000000034 method Methods 0.000 abstract description 26
- 230000008569 process Effects 0.000 abstract description 20
- 239000002351 wastewater Substances 0.000 abstract description 14
- 238000005265 energy consumption Methods 0.000 abstract description 9
- 239000003344 environmental pollutant Substances 0.000 abstract description 9
- 231100000719 pollutant Toxicity 0.000 abstract description 9
- 239000000126 substance Substances 0.000 abstract description 6
- 238000005273 aeration Methods 0.000 description 12
- 244000005700 microbiome Species 0.000 description 7
- 230000000694 effects Effects 0.000 description 6
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 4
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 4
- 210000003608 fece Anatomy 0.000 description 4
- 229910052760 oxygen Inorganic materials 0.000 description 4
- 239000001301 oxygen Substances 0.000 description 4
- 239000002893 slag Substances 0.000 description 4
- XKMRRTOUMJRJIA-UHFFFAOYSA-N ammonia nh3 Chemical compound N.N XKMRRTOUMJRJIA-UHFFFAOYSA-N 0.000 description 3
- 238000001914 filtration Methods 0.000 description 3
- 230000000813 microbial effect Effects 0.000 description 3
- 239000007787 solid Substances 0.000 description 3
- 241001465754 Metazoa Species 0.000 description 2
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 description 2
- 238000009825 accumulation Methods 0.000 description 2
- 230000009471 action Effects 0.000 description 2
- 238000000354 decomposition reaction Methods 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 230000007613 environmental effect Effects 0.000 description 2
- 238000003912 environmental pollution Methods 0.000 description 2
- 238000001125 extrusion Methods 0.000 description 2
- 238000000855 fermentation Methods 0.000 description 2
- 230000004151 fermentation Effects 0.000 description 2
- 239000000945 filler Substances 0.000 description 2
- 230000012010 growth Effects 0.000 description 2
- 238000007689 inspection Methods 0.000 description 2
- 238000012423 maintenance Methods 0.000 description 2
- 230000014759 maintenance of location Effects 0.000 description 2
- 230000010534 mechanism of action Effects 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 229910052757 nitrogen Inorganic materials 0.000 description 2
- 235000015816 nutrient absorption Nutrition 0.000 description 2
- 230000003647 oxidation Effects 0.000 description 2
- 238000007254 oxidation reaction Methods 0.000 description 2
- 229910052698 phosphorus Inorganic materials 0.000 description 2
- 239000011574 phosphorus Substances 0.000 description 2
- 230000008635 plant growth Effects 0.000 description 2
- 238000001556 precipitation Methods 0.000 description 2
- 238000012545 processing Methods 0.000 description 2
- 239000011435 rock Substances 0.000 description 2
- 238000005070 sampling Methods 0.000 description 2
- 239000013049 sediment Substances 0.000 description 2
- 238000012163 sequencing technique Methods 0.000 description 2
- 239000002689 soil Substances 0.000 description 2
- 238000001179 sorption measurement Methods 0.000 description 2
- 239000006228 supernatant Substances 0.000 description 2
- 230000009466 transformation Effects 0.000 description 2
- 230000005068 transpiration Effects 0.000 description 2
- 239000003403 water pollutant Substances 0.000 description 2
- 238000011161 development Methods 0.000 description 1
- 230000000670 limiting effect Effects 0.000 description 1
- 244000144972 livestock Species 0.000 description 1
- 239000005416 organic matter Substances 0.000 description 1
- 244000144977 poultry Species 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
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- Purification Treatments By Anaerobic Or Anaerobic And Aerobic Bacteria Or Animals (AREA)
- Separation Of Suspended Particles By Flocculating Agents (AREA)
- Biological Treatment Of Waste Water (AREA)
Abstract
本实用新型涉及一种养殖废水处理系统,包括依次连接的固液分离设备、沼气利用模块、集水调节模块、沉降处理模块、SBR处理模块、曝气生物滤池和人工湿地模块;其中,所述固液分离设备用于养殖废弃物进行固液分离,所述固液分离设备的出液口与沼气利用模块相连通,所述集水调节模块用于均衡水质水量,至少所述沉降处理模和曝气生物滤池分别与污泥浓缩池相连,并可分别将重力沉积泥和反洗水排入污泥浓缩池,所述污泥浓缩池的上部与所述集水调节模块相连通。本实用新型采用“物理处理+化学处理+生化处理+生物处理”工艺的有机结合,能使废水稳定达标排放,能耗低,运行成本低,对污染物的去除率较高,同时投资成本低。
The utility model relates to a breeding wastewater treatment system, which comprises sequentially connected solid-liquid separation equipment, a biogas utilization module, a water collection adjustment module, a sedimentation treatment module, an SBR treatment module, an aerated biological filter and an artificial wetland module; wherein, the The solid-liquid separation equipment is used for solid-liquid separation of aquaculture waste. The liquid outlet of the solid-liquid separation equipment is connected to the biogas utilization module. The water collection adjustment module is used to balance the water quality and quantity. At least the settlement treatment module The biological aerated filter and the biological aerated filter are respectively connected with the sludge concentration tank, and can respectively discharge the gravity sedimentation sludge and backwash water into the sludge concentration tank, and the upper part of the sludge concentration tank is connected with the water collection regulation module. The utility model adopts the organic combination of "physical treatment + chemical treatment + biochemical treatment + biological treatment" process, which can make the wastewater discharge stably up to the standard, with low energy consumption, low operation cost, high removal rate of pollutants, and low investment cost .
Description
技术领域technical field
本实用新型属于环保处理技术领域,具体涉及一种养殖废水处理系统。The utility model belongs to the technical field of environmental protection treatment, in particular to a breeding wastewater treatment system.
背景技术Background technique
伴随着我国畜禽养殖业的高速发展,养殖废水污染问题也日趋严重,随着我国对环保问题的高度重视,养殖废水的处理迫在眉睫。With the rapid development of my country's livestock and poultry breeding industry, the pollution of breeding wastewater is becoming more and more serious. With my country's emphasis on environmental protection, the treatment of breeding wastewater is imminent.
养殖废水具有典型的“三高”特征,即有机物浓度高,COD高达3000~12000mg/l,氨氮高达800~2200mg/l,悬浮物SS超标数十倍;可生化性一般;臭味大;冲洗排放时间集中,冲击负荷大。Aquaculture wastewater has typical "three highs" characteristics, that is, high organic matter concentration, COD as high as 3000-12000mg/l, ammonia nitrogen as high as 800-2200mg/l, and suspended solids SS exceeding the standard by dozens of times; general biodegradability; strong odor; washing The discharge time is concentrated and the impact load is large.
综上所述,亟需提供一种系统稳定、能耗低,运行成本低,对污染物的去除率较高,同时投资成本低的养殖废水处理系统。To sum up, it is urgent to provide a breeding wastewater treatment system with stable system, low energy consumption, low operating cost, high removal rate of pollutants and low investment cost.
实用新型内容Utility model content
本实用新型的目的的是提供一种系统稳定、能耗低,运行成本低,对污染物的去除率较高,同时投资成本低的养殖废水处理系统。The purpose of the utility model is to provide a breeding wastewater treatment system with stable system, low energy consumption, low operation cost, high removal rate of pollutants and low investment cost.
上述目的是通过如下技术方案实现:一种养殖废水处理系统,包括依次连接的固液分离设备、沼气利用模块、集水调节模块、沉降处理模块、SBR处理模块、曝气生物滤池和人工湿地模块;其中,所述固液分离设备用于养殖废弃物进行固液分离,所述固液分离设备的出液口与沼气利用模块相连通,所述集水调节模块用于均衡水质水量,至少所述沉降处理模和曝气生物滤池分别与污泥浓缩池相连,并可分别将重力沉积泥和反洗水排入污泥浓缩池,所述污泥浓缩池的上部与所述集水调节模块相连通。The above purpose is achieved through the following technical solutions: a breeding wastewater treatment system, including sequentially connected solid-liquid separation equipment, biogas utilization module, water collection regulation module, sedimentation treatment module, SBR treatment module, biological aerated filter and constructed wetland module; wherein, the solid-liquid separation equipment is used for solid-liquid separation of aquaculture waste, the liquid outlet of the solid-liquid separation equipment is connected to the biogas utilization module, and the water collection adjustment module is used to balance the water quality and quantity, at least The sedimentation treatment module and the biological aerated filter are respectively connected with the sludge thickening tank, and can respectively discharge the gravity sedimentation mud and backwash water into the sludge thickening tank, and the upper part of the sludge thickening tank is connected with the water collecting tank. The adjustment modules are connected.
应用时,所述沼气利用模块、集水调节模块、沉降处理模块、SBR处理模块和人工湿地模块分别包括沼气池、集水调节池、沉降池、SBR池和人工湿地。本实用新型具体应用过程中,固液分离设备实现渣水分离,粪渣干化外运处置,废水进入沼气池厌氧处理;沼气池出水进入集水调节池,通过提升泵抽水至沉降池处理,沉降池内底层沉淀物重力自排至污泥浓缩池,上层污水自流入SBR池;SBR池采取进水、曝气、沉淀、排水、闲置于一体的的方法,可利用鼓风机曝气供氧,通过微生物的生长繁殖来降解水中污染物;SBR池通过滗水器滗水至入中间水池缓冲,再泵入至曝气生物滤池,对污水进行深度好氧处理;曝气生物滤池反洗水排入污泥浓缩池,曝气生物滤池出水进入人工湿地,利用植物生长来处理污染物,污泥浓缩池的上清液返流至集水调节池再次处理。本实用新型采用“物理处理+化学处理+生化处理+生物处理”工艺的有机结合,工艺系统稳定运行,能使废水稳定达标排放,能耗低,运行成本低,后续人工湿地处理工艺能美化污水站,且净化污水的同时也净化空气,各工艺有机结合,对污染物的去除率较高,同时投资成本低,处理效果好。In application, the biogas utilization module, water collection regulation module, sedimentation treatment module, SBR treatment module and constructed wetland module respectively include biogas digesters, water collection regulation ponds, sedimentation ponds, SBR ponds and constructed wetlands. In the specific application process of the utility model, the solid-liquid separation equipment realizes the separation of slag and water, the dung is dried and transported outside for disposal, and the waste water enters the biogas tank for anaerobic treatment; the effluent of the biogas tank enters the water collection adjustment tank, and is pumped by the lifting pump to the sedimentation tank for treatment The bottom sediment in the settling tank is self-drained to the sludge thickening tank by gravity, and the upper sewage flows into the SBR tank; the SBR tank adopts the method of water inflow, aeration, sedimentation, drainage, and idleness, and the blower can be used to aerate and supply oxygen. The pollutants in the water are degraded through the growth and reproduction of microorganisms; the SBR tank decants water through a decanter until it enters the intermediate pool for buffering, and then pumps it into the biological aerated filter for deep aerobic treatment of the sewage; the biological aerated filter is backwashed The water is discharged into the sludge thickening tank, the effluent from the biological aerated filter enters the artificial wetland, and the pollutants are treated by plant growth, and the supernatant of the sludge thickening tank is returned to the water collection adjustment tank for further treatment. The utility model adopts the organic combination of "physical treatment + chemical treatment + biochemical treatment + biological treatment" process, the process system runs stably, the waste water can be stably discharged up to the standard, the energy consumption is low, the operation cost is low, and the follow-up artificial wetland treatment process can beautify the sewage Station, and purify the sewage while also purifying the air, the organic combination of various processes, the removal rate of pollutants is high, while the investment cost is low, and the treatment effect is good.
进一步的技术方案是,所述固液分离设备的前段工位设有搅拌模块,所述搅拌模块包括搅拌池、搅拌机以及设置在所述搅拌池内的提升泵,所述提升泵通过管道与所述固液分离设备相连。如此,经厂区的污水收集管网,污水进入搅拌池,通过搅拌机混匀,泵入至固液分离设备实现渣水分离,粪渣干化外运处置。A further technical solution is that the front station of the solid-liquid separation equipment is provided with a stirring module, and the stirring module includes a stirring tank, a stirrer and a lifting pump arranged in the stirring tank, and the lifting pump is connected to the Solid-liquid separation equipment connected. In this way, through the sewage collection pipe network in the factory area, the sewage enters the mixing tank, is mixed by the mixer, and is pumped into the solid-liquid separation equipment to realize the separation of slag and water, and the dung is dried and transported out for disposal.
进一步的技术方案是,所述养殖废水处理系统还包括并列设置的第一鼓风机和第二鼓风机,所述第一鼓风机和第二鼓风机的出风口通过管道与所述SBR处理模块和曝气生物滤池相连。如此,第一鼓风机和第二鼓风机为SBR处理模块和曝气生物滤池提供空气进行曝气,第一鼓风机和第二鼓风机可根据所需要的风量可同时工作或单独工作。A further technical solution is that the aquaculture wastewater treatment system also includes a first blower and a second blower arranged side by side, and the air outlets of the first blower and the second blower are connected to the SBR treatment module and the biological aerated filter through a pipeline. The pool is connected. In this way, the first blower and the second blower provide air for the SBR treatment module and the biological aerated filter for aeration, and the first blower and the second blower can work simultaneously or independently according to the required air volume.
进一步的技术方案是,所述第一鼓风机和第二鼓风机的出风口通过管道与所述沉降处理模块相连。如此,第一鼓风机和第二鼓风机为沉降处理模块提供空气实现吹脱。A further technical solution is that the air outlets of the first blower and the second blower are connected to the sedimentation treatment module through pipelines. In this way, the first air blower and the second air blower provide air for the sedimentation treatment module to realize blow-off.
进一步的技术方案是,所述SBR处理模块和曝气生物滤池之间设有中间池,所述BR处理模块至少包括滗水器,所述滗水器将SBR处理模块内的污水滗水至入中间池缓冲,所述中间池的污水可泵入曝气生物滤池。A further technical solution is that an intermediate tank is provided between the SBR treatment module and the biological aerated filter, and the BR treatment module at least includes a decanter, and the decanter decants the sewage in the SBR treatment module to into the intermediate pool for buffering, and the sewage in the intermediate pool can be pumped into the biological aerated filter.
进一步的技术方案是,所述养殖废水处理系统还包括清水池,经所述人工湿地模块的处理后的处理液流入清水池。如此,可通过清水池监测水质动向,作为取样检查口。A further technical solution is that the aquaculture wastewater treatment system further includes a clear water pool, and the treatment liquid treated by the constructed wetland module flows into the clear water pool. In this way, the water quality trend can be monitored through the clear water pool as a sampling inspection port.
进一步的技术方案是,所述养殖废水处理系统还包括加药消毒机,所述加药消毒机通过在清水池尾水段投加消毒药剂进行灭菌消毒处理。如此,消毒后的水达标排放至河流,这样进一步保证排出的水的水质,减少环境污染。A further technical solution is that the aquaculture wastewater treatment system also includes a dosing and disinfection machine, and the dosing and disinfection machine performs sterilization and disinfection treatment by adding disinfectants to the tail water section of the clear water tank. In this way, the disinfected water meets the standard and is discharged to the river, which further ensures the quality of the discharged water and reduces environmental pollution.
进一步的技术方案是,所述污泥浓缩池的下部通过管道和隔膜泵与过滤设备相连,所述过滤设备的滤液排出口与所述沉降处理模块相连通。污泥浓缩池的污泥通过气动隔膜泵泵入至板框压滤机处理,泥饼消毒外运处置,滤液流至沉降处理模块再次处理。A further technical solution is that the lower part of the sludge thickening tank is connected to the filter equipment through a pipeline and a diaphragm pump, and the filtrate outlet of the filter equipment is connected to the sedimentation treatment module. The sludge in the sludge thickening tank is pumped into the plate and frame filter press for treatment through the pneumatic diaphragm pump, the mud cake is sterilized and transported outside for disposal, and the filtrate flows to the sedimentation treatment module for further treatment.
进一步的技术方案是,所述沼气利用模块、集水调节模块、沉降处理模块、SBR处理模块和人工湿地模块分别包括沼气池、集水调节池、沉降池、SBR池和人工湿地。可采用各池子采用半地埋式,排泥系统采用重力自排,降低能耗。上述各模块的具体作用如下,固液分离机:利用螺旋挤压原理,对高浓度高SS的原始废水进行固液分离,其对SS和COD的去除效率高达70以上;沼气池:黑膜沼气池,在密闭环境下,通过微生物的发酵作用处理污水;集水调节池:均衡水质水量,避免水质和水量波动太大影响污水处理系统;沉降池:为进入SBR池提供有力条件,充分去除SS,采用重力排泥;SBR池:序批式活性污泥法,在运行上的有序和间歇操作,集进水、曝气、沉淀、排水和闲置于一池。曝气阶段利用罗茨鼓风机的供氧,微生物生长繁殖,从而降低了COD且有很好的脱氮除磷效果;曝气生物滤池:进水方式采用下进上出的模式,曝气方式为底部曝气,中间填埋火山岩填料,该池集生物氧化和截留悬浮固体一体,定期反洗曝气生物滤池;人工湿地:污水与污泥在沿一定方向流动的过程中,主要利用土壤、人工介质、植物、微生物的物理、化学、生物三重协同作用,对污水、污泥进行处理的一种技术。其作用机理包括吸附、滞留、过滤、氧化还原、沉淀、微生物分解、转化、植物遮蔽、残留物积累、蒸腾水分和养分吸收及各类动物的作用。A further technical solution is that the biogas utilization module, water collection regulation module, sedimentation treatment module, SBR treatment module and constructed wetland module include biogas digesters, water collection regulation ponds, sedimentation ponds, SBR ponds and constructed wetlands, respectively. Each pool can be semi-buried, and the mud discharge system adopts gravity self-drainage to reduce energy consumption. The specific functions of the above modules are as follows. Solid-liquid separator: use the principle of screw extrusion to separate solid-liquid from raw wastewater with high concentration and high SS, and its removal efficiency for SS and COD is as high as 70% or more; biogas digester: black film biogas Pool, in a closed environment, treats sewage through microbial fermentation; water collection adjustment pool: balance water quality and quantity, avoid too large fluctuations in water quality and water volume from affecting the sewage treatment system; sedimentation tank: provide strong conditions for entering the SBR pool, and fully remove SS , using gravity sludge discharge; SBR pool: Sequencing batch activated sludge method, orderly and intermittent operation in operation, collecting water, aeration, sedimentation, drainage and idle in one pool. In the aeration stage, the roots blower is used to supply oxygen, and the microorganisms grow and multiply, thereby reducing COD and having a good effect of nitrogen and phosphorus removal; biological aerated filter: the water intake mode adopts the mode of bottom in and top out, and the aeration mode Aeration is at the bottom, and volcanic rock filler is buried in the middle. The pool integrates biological oxidation and interception of suspended solids, and regularly backwashes the biological aerated filter; artificial wetland: when sewage and sludge flow in a certain direction, the main use of soil It is a technology for treating sewage and sludge through the triple synergy of physics, chemistry and biology of artificial media, plants and microorganisms. Its mechanism of action includes adsorption, retention, filtration, redox, precipitation, microbial decomposition, transformation, plant shading, residue accumulation, transpiration of water and nutrient absorption, and the action of various animals.
进一步的技术方案是,所述集水调节池和中间池分别设有提升泵,所述提升泵将集水调节池和中间池的污水分别输送至沉降池和曝气生物滤池。A further technical solution is that the water collection adjustment tank and the intermediate tank are respectively provided with lift pumps, and the lift pumps transport the sewage in the water collection adjustment tank and the intermediate tank to the sedimentation tank and the biological aerated filter respectively.
经过本系统处理后的废水,水污染物排放指标如下:1)CODcr:≤100mg/L;2)BOD5:≤30mg/L;3)氨氮:≤80mg/L;4)SS:≤70mg/L。相比于现有技术,本实用新型具有以下优势:1)采用“物理处理+化学处理+生化处理+生物处理”工艺的有机结合,工艺系统稳定运行,能使废水稳定达标排放;2)可实现PLC自动化控制,便于运维管理;3)能耗低,运行成本低;4)后续人工湿地处理工艺能美化污水站,且净化污水的同时也净化空气;5)各工艺有机结合,对污染物的去除率较高;6)投资成本低,处理效果好。The wastewater treated by this system, the discharge indicators of water pollutants are as follows: 1) CODcr: ≤100mg/L; 2) BOD 5 : ≤30mg/L; 3) Ammonia nitrogen: ≤80mg/L; 4) SS: ≤70mg/L L. Compared with the prior art, the utility model has the following advantages: 1) The organic combination of "physical treatment + chemical treatment + biochemical treatment + biological treatment" process is adopted, the process system runs stably, and the wastewater can be discharged stably up to the standard; 2) it can Realize PLC automatic control, which is convenient for operation and maintenance management; 3) Low energy consumption and low operating cost; 4) Subsequent artificial wetland treatment process can beautify the sewage station, and purify the sewage while also purifying the air; 5) The organic combination of various processes reduces pollution 6) Low investment cost and good treatment effect.
附图说明Description of drawings
构成本实用新型的一部分的附图用来提供对本实用新型的进一步理解,本实用新型的示意性实施例及其说明用于解释本实用新型,并不构成对本实用新型的不当限定。The accompanying drawings constituting a part of the utility model are used to provide a further understanding of the utility model, and the schematic embodiments of the utility model and their descriptions are used to explain the utility model, and do not constitute improper limitations to the utility model.
图1为本实用新型一种实施方式所涉及的养殖废水处理系统的布置示意图;Fig. 1 is the layout schematic diagram of the breeding wastewater treatment system involved in an embodiment of the present invention;
图2为本实用新型一种实施方式所涉及的养殖废水处理系统的处理流程示意图。Fig. 2 is a schematic diagram of the treatment process of the aquaculture wastewater treatment system involved in an embodiment of the present invention.
图中:In the picture:
1固液分离设备 2集水调节池 3沼气池 4沉降池1 Solid-liquid separation equipment 2 Water collection and adjustment tank 3 Digester 4 Settling tank
5 SBR池 6人工湿地模块 7曝气生物滤池 8搅拌池5 SBR tank 6 Constructed wetland module 7 Biological aerated filter tank 8 Stirring tank
9搅拌机 10第一鼓风机 11第二鼓风机 12中间池9 mixer 10 first blower 11 second blower 12 intermediate pool
13清水池 14加药消毒机 15污泥浓缩池 16过滤设备13 Clean water pool 14 Dosing and disinfection machine 15 Sludge concentration pool 16 Filtration equipment
17隔膜泵 18滗水器17 diaphragm pump 18 decanter
具体实施方式Detailed ways
下面结合附图对本实用新型进行详细描述,本部分的描述仅是示范性和解释性,不应对本实用新型的保护范围有任何的限制作用。此外,本领域技术人员根据本文件的描述,可以对本文件中实施例中以及不同实施例中的特征进行相应组合。The utility model will be described in detail below in conjunction with the accompanying drawings. The description in this part is only exemplary and explanatory, and should not have any limiting effect on the protection scope of the utility model. In addition, those skilled in the art can make corresponding combinations of features in the embodiments in this document and in different embodiments according to the descriptions in this document.
本实用新型实施例如下,参照图1和图2,一种养殖废水处理系统,包括依次连接的固液分离设备1、沼气利用模块、集水调节模块、沉降处理模块、SBR处理模块、曝气生物滤池7和人工湿地模块6;其中,所述固液分离设备1用于养殖废弃物进行固液分离,所述固液分离设备1的出液口与沼气利用模块相连通,所述集水调节模块用于均衡水质水量,至少所述沉降处理模和曝气生物滤池7分别与污泥浓缩池15相连,并可分别将重力沉积泥和反洗水排入污泥浓缩池15,所述污泥浓缩池15的上部与所述集水调节模块相连通。Embodiments of the present utility model are as follows, referring to Fig. 1 and Fig. 2, a breeding wastewater treatment system, including solid-liquid separation equipment 1 connected in sequence, a biogas utilization module, a water collection regulation module, a sedimentation treatment module, an SBR treatment module, an aeration biological filter 7 and constructed wetland module 6; wherein, the solid-liquid separation device 1 is used for solid-liquid separation of culture waste, and the liquid outlet of the solid-liquid separation device 1 is connected with the biogas utilization module, and the set The water regulation module is used to balance the water quality and quantity. At least the sedimentation treatment module and the biological aerated filter tank 7 are connected to the sludge thickening tank 15 respectively, and the gravity sedimentation mud and backwash water can be discharged into the sludge thickening tank 15 respectively. The upper part of the sludge thickening tank 15 communicates with the water collection regulating module.
应用时,如图1和图2,所述沼气利用模块、集水调节模块、沉降处理模块、SBR处理模块和人工湿地模块6分别包括为沼气池3、集水调节池2、沉降池4、SBR池5和人工湿地。本实用新型具体应用过程中,固液分离设备1实现渣水分离,粪渣干化外运处置,废水进入沼气池3厌氧处理;沼气池3出水进入集水调节池2,通过提升泵抽水至沉降池4处理,沉降池4内底层沉淀物重力自排至污泥浓缩池15,上层污水自流入SBR池5;SBR池5采取进水、曝气、沉淀、排水、闲置于一体的的方法,可利用鼓风机曝气供氧,通过微生物的生长繁殖来降解水中污染物;SBR池5通过滗水器18滗水至入中间水池缓冲,再泵入至曝气生物滤池7,对污水进行深度好氧处理;曝气生物滤池7反洗水排入污泥浓缩池15,曝气生物滤池7出水进入人工湿地,利用植物生长来处理污染物,污泥浓缩池15的上清液返流至集水调节池2再次处理。本实用新型采用“物理处理+化学处理+生化处理+生物处理”工艺的有机结合,工艺系统稳定运行,能使废水稳定达标排放,能耗低,运行成本低,后续人工湿地处理工艺能美化污水站,且净化污水的同时也净化空气,各工艺有机结合,对污染物的去除率较高,同时投资成本低,处理效果好。In application, as shown in Figure 1 and Figure 2, the biogas utilization module, water collection regulation module, sedimentation treatment module, SBR treatment module and constructed wetland module 6 respectively include a biogas digester 3, a water collection regulation pond 2, a settlement pond 4, SBR pool 5 and constructed wetlands. In the specific application process of the utility model, the solid-liquid separation equipment 1 realizes the separation of slag and water, the dung is dried and transported outside for disposal, and the waste water enters the biogas digester 3 for anaerobic treatment; the effluent of the biogas digester 3 enters the water collection adjustment pond 2, and pumps water through the lifting pump To the sedimentation tank 4 for treatment, the bottom sediment in the sedimentation tank 4 is automatically discharged to the sludge thickening tank 15 by gravity, and the upper layer of sewage flows into the SBR tank 5; The method can use the blower to aerate and supply oxygen, and degrade the pollutants in the water through the growth and reproduction of microorganisms; the SBR pool 5 decants the water through the decanter 18 until it enters the intermediate pool for buffering, and then pumps it into the biological aerated filter 7 to treat the sewage Carry out deep aerobic treatment; the backwash water of the biological aerated filter 7 is discharged into the sludge thickening tank 15, and the effluent of the biological aerated filter 7 enters the artificial wetland, and the pollutants are treated by plant growth, and the supernatant of the sludge thickening tank 15 The liquid is returned to the water collection adjustment tank 2 for further processing. The utility model adopts the organic combination of "physical treatment + chemical treatment + biochemical treatment + biological treatment" process, the process system runs stably, the waste water can be stably discharged up to the standard, the energy consumption is low, the operation cost is low, and the follow-up artificial wetland treatment process can beautify the sewage Station, and purify the sewage while also purifying the air, the organic combination of various processes, the removal rate of pollutants is high, while the investment cost is low, and the treatment effect is good.
上述实施例的基础上,本实用新型另一实施例中,如图1,所述固液分离设备1的前段工位设有搅拌模块,所述搅拌模块包括搅拌池8、搅拌机9以及设置在所述搅拌池8内的提升泵,所述提升泵通过管道与所述固液分离设备1相连。如此,经厂区的污水收集管网,污水进入搅拌池8,通过搅拌机9混匀,泵入至固液分离设备1实现渣水分离,粪渣干化外运处置。On the basis of the above-mentioned embodiments, in another embodiment of the present invention, as shown in Figure 1, the front section of the solid-liquid separation device 1 is provided with a stirring module, and the stirring module includes a stirring tank 8, a stirring machine 9 and a The lift pump in the stirring tank 8 is connected to the solid-liquid separation device 1 through a pipeline. In this way, through the sewage collection pipe network in the factory area, the sewage enters the mixing tank 8, is mixed by the mixer 9, and is pumped into the solid-liquid separation equipment 1 to realize the separation of slag and water, and the dung is dried and transported outside for disposal.
上述实施例的基础上,本实用新型另一实施例中,如图1,所述养殖废水处理系统还包括并列设置的第一鼓风机10和第二鼓风机11,所述第一鼓风机10和第二鼓风机11的出风口通过管道与所述SBR处理模块和曝气生物滤池7相连。如此,第一鼓风机10和第二鼓风机11为SBR处理模块和曝气生物滤池7提供空气进行曝气,第一鼓风机10和第二鼓风机11可根据所需要的风量可同时工作或单独工作。On the basis of the above-mentioned embodiments, in another embodiment of the utility model, as shown in Figure 1, the aquaculture wastewater treatment system also includes a first blower 10 and a second blower 11 arranged side by side, and the first blower 10 and the second blower The air outlet of the blower 11 is connected with the SBR treatment module and the biological aerated filter 7 through a pipeline. In this way, the first blower 10 and the second blower 11 provide air for the SBR treatment module and the biological aerated filter 7 for aeration, and the first blower 10 and the second blower 11 can work simultaneously or independently according to the required air volume.
上述实施例的基础上,本实用新型另一实施例中,如图1,所述第一鼓风机10和第二鼓风机11的出风口通过管道与所述沉降处理模块相连。如此,第一鼓风机10和第二鼓风机11为沉降处理模块提供空气实现吹脱。On the basis of the above embodiments, in another embodiment of the present invention, as shown in FIG. 1 , the air outlets of the first blower 10 and the second blower 11 are connected to the sedimentation treatment module through pipes. In this way, the first air blower 10 and the second air blower 11 provide air for the sedimentation treatment module to realize blow-off.
上述实施例的基础上,本实用新型另一实施例中,如图1,所述SBR处理模块和曝气生物滤池7之间设有中间池12,所述BR处理模块至少包括滗水器18,所述滗水器18将SBR处理模块内的污水滗水至入中间池12缓冲,所述中间池12的污水可泵入曝气生物滤池7。On the basis of the above embodiments, in another embodiment of the present invention, as shown in Figure 1, an intermediate pool 12 is provided between the SBR treatment module and the biological aerated filter 7, and the BR treatment module at least includes a decanter 18. The decanter 18 decants the sewage in the SBR treatment module to the intermediate pool 12 for buffering, and the sewage in the intermediate pool 12 can be pumped into the biological aerated filter 7.
上述实施例的基础上,本实用新型另一实施例中,如图1,所述养殖废水处理系统还包括清水池13,经所述人工湿地模块6的处理后的处理液流入清水池13。如此,可通过清水池13监测水质动向,作为取样检查口。On the basis of the above embodiments, in another embodiment of the present invention, as shown in Figure 1, the aquaculture wastewater treatment system further includes a clear water pool 13, and the treated liquid treated by the constructed wetland module 6 flows into the clear water pool 13. In this way, the water quality trend can be monitored through the clear water pool 13 as a sampling inspection port.
上述实施例的基础上,本实用新型另一实施例中,如图1,所述养殖废水处理系统还包括加药消毒机14,所述加药消毒机14通过在清水池13尾水段投加消毒药剂进行灭菌消毒处理。如此,消毒后的水达标排放至河流,这样进一步保证排出的水的水质,减少环境污染。On the basis of the above-described embodiments, in another embodiment of the utility model, as shown in Figure 1, the aquaculture wastewater treatment system also includes a dosing and disinfection machine 14, and the dosing and disinfection machine 14 passes through the 13 tail water sections of the clear water tank. Add disinfectant for sterilization and disinfection. In this way, the disinfected water meets the standard and is discharged to the river, which further ensures the quality of the discharged water and reduces environmental pollution.
上述实施例的基础上,本实用新型另一实施例中,如图1,所述污泥浓缩池15的下部通过管道和隔膜泵17与过滤设备16相连,所述过滤设备16的滤液排出口与所述沉降处理模块相连通。污泥浓缩池15的污泥通过气动隔膜泵17泵入至板框压滤机处理,泥饼消毒外运处置,滤液流至沉降处理模块再次处理。On the basis of the foregoing embodiments, in another embodiment of the utility model, as shown in Figure 1, the bottom of the sludge thickening tank 15 is connected to the filter device 16 through a pipeline and a diaphragm pump 17, and the filtrate outlet of the filter device 16 is It is connected with the settlement processing module. The sludge in the sludge thickening tank 15 is pumped into the plate and frame filter press through the pneumatic diaphragm pump 17 for treatment, the mud cake is sterilized and transported outside for disposal, and the filtrate flows to the sedimentation treatment module for further treatment.
上述实施例的基础上,本实用新型另一实施例中,如图1,所述沼气利用模块、集水调节模块、沉降处理模块、SBR处理模块和人工湿地模块6分别包括沼气池3、集水调节池2、沉降池4、SBR池5和人工湿地。可采用各池子采用半地埋式,排泥系统采用重力自排,降低能耗。上述各模块的具体作用如下,固液分离机:利用螺旋挤压原理,对高浓度高SS的原始废水进行固液分离,其对SS和COD的去除效率高达70以上;沼气池3:黑膜沼气池3,在密闭环境下,通过微生物的发酵作用处理污水;集水调节池2:均衡水质水量,避免水质和水量波动太大影响污水处理系统;沉降池4:为进入SBR池5提供有力条件,充分去除SS,采用重力排泥;SBR池5:序批式活性污泥法,在运行上的有序和间歇操作,集进水、曝气、沉淀、排水和闲置于一池。曝气阶段利用罗茨鼓风机的供氧,微生物生长繁殖,从而降低了COD且有很好的脱氮除磷效果;曝气生物滤池7:进水方式采用下进上出的模式,曝气方式为底部曝气,中间填埋火山岩填料,该池集生物氧化和截留悬浮固体一体,定期反洗曝气生物滤池7;人工湿地:污水与污泥在沿一定方向流动的过程中,主要利用土壤、人工介质、植物、微生物的物理、化学、生物三重协同作用,对污水、污泥进行处理的一种技术。其作用机理包括吸附、滞留、过滤、氧化还原、沉淀、微生物分解、转化、植物遮蔽、残留物积累、蒸腾水分和养分吸收及各类动物的作用。On the basis of the above embodiments, in another embodiment of the utility model, as shown in Figure 1, the biogas utilization module, water collection regulation module, settlement treatment module, SBR treatment module and constructed wetland module 6 respectively include a biogas tank 3, a collection Water regulation pond 2, sedimentation pond 4, SBR pond 5 and constructed wetland. Each pool can be semi-buried, and the mud discharge system adopts gravity self-drainage to reduce energy consumption. The specific functions of the above modules are as follows. Solid-liquid separator: uses the principle of screw extrusion to separate solid-liquid from raw wastewater with high concentration and high SS, and its removal efficiency for SS and COD is as high as 70% or more; biogas tank 3: black film Digester 3, in a closed environment, treats sewage through the fermentation of microorganisms; water collection adjustment tank 2: balances water quality and quantity, and avoids excessive fluctuations in water quality and water volume from affecting the sewage treatment system; settling tank 4: provides powerful water for entering SBR tank 5 Conditions, fully remove SS, adopt gravity sludge discharge; SBR pool 5: sequencing batch activated sludge method, orderly and intermittent operation in operation, collect water, aeration, sedimentation, drainage and idle in one pool. In the aeration stage, the roots blower is used to supply oxygen, and the microorganisms grow and reproduce, thereby reducing COD and having a good effect of nitrogen and phosphorus removal; biological aerated filter 7: the water intake mode adopts the bottom-in and top-out mode, and the aeration The method is aeration at the bottom, and volcanic rock filler is buried in the middle. The pool integrates biological oxidation and interception of suspended solids, and regularly backwashes the biological aerated filter 7; Constructed wetland: when sewage and sludge flow in a certain direction, the main It is a technology to treat sewage and sludge by using the physical, chemical and biological synergy of soil, artificial medium, plants and microorganisms. Its mechanism of action includes adsorption, retention, filtration, redox, precipitation, microbial decomposition, transformation, plant shading, residue accumulation, transpiration of water and nutrient absorption, and the action of various animals.
上述实施例的基础上,本实用新型另一实施例中,如图1,所述集水调节池2和中间池12分别设有提升泵,所述提升泵将集水调节池2和中间池12的污水分别输送至沉降池4和曝气生物滤池7。On the basis of the foregoing embodiments, in another embodiment of the present utility model, as shown in Fig. 1 , the water-collecting regulating pool 2 and the intermediate pool 12 are respectively provided with lift pumps, and the lifting pumps will separate the water-collecting regulating pool 2 and the intermediate pool 12 is transported to the sedimentation tank 4 and the biological aerated filter 7 respectively.
经过本系统处理后的废水,水污染物排放指标如下:1)CODcr:≤100mg/L;2)BOD5:≤30mg/L;3)氨氮:≤80mg/L;4)SS:≤70mg/L。相比于现有技术,本实用新型具有以下优势:1)采用“物理处理+化学处理+生化处理+生物处理”工艺的有机结合,工艺系统稳定运行,能使废水稳定达标排放;2)可实现PLC自动化控制,便于运维管理;3)能耗低,运行成本低;4)后续人工湿地处理工艺能美化污水站,且净化污水的同时也净化空气;5)各工艺有机结合,对污染物的去除率较高;6)投资成本低,处理效果好。The wastewater treated by this system, the discharge indicators of water pollutants are as follows: 1) CODcr: ≤100mg/L; 2) BOD 5 : ≤30mg/L; 3) Ammonia nitrogen: ≤80mg/L; 4) SS: ≤70mg/L L. Compared with the prior art, the utility model has the following advantages: 1) The organic combination of "physical treatment + chemical treatment + biochemical treatment + biological treatment" process is adopted, the process system runs stably, and the wastewater can be discharged stably up to the standard; 2) it can Realize PLC automatic control, which is convenient for operation and maintenance management; 3) Low energy consumption and low operating cost; 4) Subsequent artificial wetland treatment process can beautify the sewage station, and purify the sewage while also purifying the air; 5) The organic combination of various processes reduces pollution 6) Low investment cost and good treatment effect.
对于本技术领域的普通技术人员来说,在不脱离本实用新型原理的前提下,还可以做出若干改进和润饰,这些改进和润饰也应视为本实用新型的保护范围。For those of ordinary skill in the art, without departing from the principle of the utility model, some improvements and modifications can also be made, and these improvements and modifications should also be regarded as the protection scope of the utility model.
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