CN110386739A - A kind of aquaculture sewage sludge modularized treatment system and its treatment process - Google Patents
A kind of aquaculture sewage sludge modularized treatment system and its treatment process Download PDFInfo
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- 238000000034 method Methods 0.000 title claims abstract description 27
- 238000009360 aquaculture Methods 0.000 title claims abstract description 24
- 244000144974 aquaculture Species 0.000 title claims abstract description 24
- 239000010801 sewage sludge Substances 0.000 title claims abstract description 22
- 239000010802 sludge Substances 0.000 claims abstract description 86
- 238000001035 drying Methods 0.000 claims abstract description 44
- 238000005273 aeration Methods 0.000 claims abstract description 41
- 238000006243 chemical reaction Methods 0.000 claims abstract description 41
- 230000020477 pH reduction Effects 0.000 claims abstract description 25
- 239000000126 substance Substances 0.000 claims abstract description 25
- 238000005188 flotation Methods 0.000 claims abstract description 22
- 230000003301 hydrolyzing effect Effects 0.000 claims abstract description 22
- 238000004062 sedimentation Methods 0.000 claims abstract description 22
- 230000008719 thickening Effects 0.000 claims abstract description 21
- 239000002002 slurry Substances 0.000 claims abstract description 18
- 239000007789 gas Substances 0.000 claims abstract description 10
- 238000004064 recycling Methods 0.000 claims abstract description 4
- 239000010865 sewage Substances 0.000 claims description 30
- 238000002485 combustion reaction Methods 0.000 claims description 18
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 15
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims description 13
- 239000001301 oxygen Substances 0.000 claims description 13
- 229910052760 oxygen Inorganic materials 0.000 claims description 13
- 230000014759 maintenance of location Effects 0.000 claims description 9
- 239000007788 liquid Substances 0.000 claims description 8
- 239000002994 raw material Substances 0.000 claims description 6
- 238000012546 transfer Methods 0.000 claims description 6
- 208000005156 Dehydration Diseases 0.000 claims description 5
- 238000006297 dehydration reaction Methods 0.000 claims description 5
- 238000005406 washing Methods 0.000 claims description 5
- 230000018044 dehydration Effects 0.000 claims description 4
- 239000003337 fertilizer Substances 0.000 claims description 4
- 238000007667 floating Methods 0.000 claims description 4
- 238000000926 separation method Methods 0.000 claims description 4
- 238000010248 power generation Methods 0.000 claims description 3
- 230000001105 regulatory effect Effects 0.000 claims description 3
- 238000012423 maintenance Methods 0.000 abstract description 6
- 239000002351 wastewater Substances 0.000 abstract description 5
- 230000007613 environmental effect Effects 0.000 abstract description 4
- 238000009434 installation Methods 0.000 abstract description 3
- 238000009395 breeding Methods 0.000 abstract description 2
- 230000001488 breeding effect Effects 0.000 abstract description 2
- 244000144972 livestock Species 0.000 description 4
- 239000007787 solid Substances 0.000 description 4
- 239000011449 brick Substances 0.000 description 3
- 230000003111 delayed effect Effects 0.000 description 3
- 238000011010 flushing procedure Methods 0.000 description 3
- 230000007062 hydrolysis Effects 0.000 description 3
- 238000006460 hydrolysis reaction Methods 0.000 description 3
- 238000012545 processing Methods 0.000 description 3
- 238000004065 wastewater treatment Methods 0.000 description 3
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 description 2
- 239000000446 fuel Substances 0.000 description 2
- 239000003895 organic fertilizer Substances 0.000 description 2
- 229910052698 phosphorus Inorganic materials 0.000 description 2
- 239000011574 phosphorus Substances 0.000 description 2
- 244000144977 poultry Species 0.000 description 2
- 238000006722 reduction reaction Methods 0.000 description 2
- 241000894006 Bacteria Species 0.000 description 1
- XKMRRTOUMJRJIA-UHFFFAOYSA-N ammonia nh3 Chemical compound N.N XKMRRTOUMJRJIA-UHFFFAOYSA-N 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 235000015895 biscuits Nutrition 0.000 description 1
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- 238000010586 diagram Methods 0.000 description 1
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- 230000003670 easy-to-clean Effects 0.000 description 1
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- 238000005516 engineering process Methods 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
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- 230000002349 favourable effect Effects 0.000 description 1
- 210000003608 fece Anatomy 0.000 description 1
- 239000000383 hazardous chemical Substances 0.000 description 1
- 239000010871 livestock manure Substances 0.000 description 1
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- 230000000813 microbial effect Effects 0.000 description 1
- 238000006386 neutralization reaction Methods 0.000 description 1
- 239000005416 organic matter Substances 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
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- 238000012795 verification Methods 0.000 description 1
Classifications
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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
-
- 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
- C02F11/122—Treatment of sludge; Devices therefor by de-watering, drying or thickening by mechanical de-watering using filter presses
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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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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G7/00—Incinerators or other apparatus for consuming industrial waste, e.g. chemicals
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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
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/24—Treatment of water, waste water, or sewage by flotation
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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
- C02F2001/007—Processes including a sedimentation step
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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
- C02F2103/00—Nature of the water, waste water, sewage or sludge to be treated
- C02F2103/20—Nature of the water, waste water, sewage or sludge to be treated from animal husbandry
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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
- C02F3/30—Aerobic and anaerobic processes
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- Environmental & Geological Engineering (AREA)
- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Water Supply & Treatment (AREA)
- Chemical & Material Sciences (AREA)
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- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
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Abstract
本发明涉及污水污泥处理技术领域,公开了一种养殖业污水污泥模块化处理系统,包括物化处理模块、生物处理模块、沼气利用模块和污泥干化模块,物化处理模块包括格栅调节池、物化池和沉淀池,生物处理模块包括水解酸化反应池、IC反应池、BAF曝气池和气浮机,沼气利用模块包括沼气脱硫器、沼气发电机、沼气燃烧炉和沼液收集箱,污泥干化模块包括污泥浓缩池、压滤机、干燥间和污泥焚烧炉;本发明还公开了一种养殖业污水污泥模块化处理系统的处理工艺。本发明占地面积小,方便安装维护,费用低,可根据实际需要删减组件进行选择性的组装,实现了资源化循环利用,效率高,节能环保,大幅减少了污染性气体的排放,对废水进行了回收利用。
The invention relates to the technical field of sewage sludge treatment, and discloses a modular treatment system for aquaculture sewage sludge, including a physical and chemical treatment module, a biological treatment module, a biogas utilization module and a sludge drying module. The physical and chemical treatment module includes a grid adjustment module pool, physicochemical tank and sedimentation tank, biological treatment module includes hydrolytic acidification reaction tank, IC reaction tank, BAF aeration tank and air flotation machine, biogas utilization module includes biogas desulfurizer, biogas generator, biogas burner and biogas slurry collection box, The sludge drying module includes a sludge thickening tank, a filter press, a drying room and a sludge incinerator; the invention also discloses a treatment process of a breeding industry sewage sludge modular treatment system. The invention occupies a small area, is convenient for installation and maintenance, and has low cost. It can selectively assemble components according to actual needs, realize resource recycling, high efficiency, energy saving and environmental protection, and greatly reduce the emission of polluting gases. Waste water was recycled.
Description
技术领域technical field
本发明涉及污水污泥处理技术领域,具体涉及一种养殖业污水污泥模块化处理系统及其处理工艺。The invention relates to the technical field of sewage sludge treatment, in particular to a modular treatment system for aquaculture sewage sludge and a treatment process thereof.
背景技术Background technique
养殖业污泥污水对城市发展来说,既是污染同时也是可以被我们利用起来的资源。养殖污水具有典型的“三高”特征,即有机物浓度高,其中的CODcr(化学耗氧量)高达3000-12000mg/l,氨氮高达800-2200mg/l,SS(悬浮物)超标数十倍,且色度深,含有大量的细菌,有机磷含量也很高。若直接排放到农田湖泊中会造成严重的污染,目前的畜禽养殖污染已经成为我国环境治理的一个重大问题。Aquaculture sludge is not only pollution but also a resource that we can use for urban development. Aquaculture sewage has typical "three highs" characteristics, that is, the concentration of organic matter is high, among which CODcr (chemical oxygen demand) is as high as 3000-12000 mg/l, ammonia nitrogen is as high as 800-2200 mg/l, and SS (suspended solids) exceeds the standard by dozens of times. And the color is deep, contains a large number of bacteria, and the content of organic phosphorus is also high. If it is directly discharged into farmland and lakes, it will cause serious pollution. The current livestock and poultry breeding pollution has become a major problem in my country's environmental governance.
目前国内外的污水处理技术主要是物理处理法、生物处理法和化学处理法。物理处理法包括格栅和固液分离,生物处理法包括水解酸化、厌氧、好氧处理以及气浮处理,而化学处理则是在各个处理过程中加入化学物质,使化学物质与污水中的有害物质发生化学反应而被转化,包括中和、氧化、还原、分解、混凝和化学沉淀等,以达到加快处理速度的目的。对于污泥处理,一般使用浓缩-脱水(真空、加压、带式)-干燥(直接、间接)处理流程,处理后的泥块用于燃烧、填埋和制砖等用途。At present, domestic and foreign sewage treatment technologies are mainly physical treatment, biological treatment and chemical treatment. The physical treatment method includes grid and solid-liquid separation, the biological treatment method includes hydrolytic acidification, anaerobic, aerobic treatment and air flotation treatment, and the chemical treatment is to add chemical substances in each treatment process to make the chemical substances and sewage Hazardous substances undergo chemical reactions and are transformed, including neutralization, oxidation, reduction, decomposition, coagulation and chemical precipitation, etc., in order to speed up the processing speed. For sludge treatment, concentration-dehydration (vacuum, pressurization, belt)-drying (direct, indirect) treatment process is generally used, and the treated mud is used for combustion, landfill and brick making.
目前国内废水处理现状较为混乱,还没有规范化的处理方法。国内的畜禽粪便无害化处理方法单一,设施投入过大,运转费用过高。沼气化工程治污虽然能达到生态化和减量化的要求,但尚未能达到无害化的目标,并且沼液和沼渣处理不当,还会引起二次污染。因此研发一种方便处理,维护费用低,可全方位资源化循环利用的养殖废水处理模式和工艺成为了当务之急,也极具工程实践价值。At present, the status quo of domestic wastewater treatment is relatively chaotic, and there is no standardized treatment method. Domestic livestock and poultry manure has a single harmless treatment method, and the investment in facilities is too large, and the operating cost is too high. Although the pollution control of the biogasification project can meet the requirements of ecologicalization and reduction, it has not yet achieved the goal of harmlessness, and improper treatment of biogas slurry and biogas residue will cause secondary pollution. Therefore, it has become a top priority to develop a farming wastewater treatment mode and process that is convenient to handle, low in maintenance costs, and can be recycled and utilized in an all-round way, and it is also of great engineering practice value.
发明内容Contents of the invention
基于以上问题,本发明提供一种养殖业污水污泥模块化处理系统及其处理工艺,本发明可实现养殖场污水污泥的模块化处理,可对处理过程中的污泥污水进行资源化循环利用,处理效率高,节能环保,大幅减少了污染性气体的排放,方便安装,方便维护,维护费用低。Based on the above problems, the present invention provides a modular treatment system for aquaculture sewage sludge and its treatment process. The present invention can realize the modular treatment of sewage sludge in aquaculture farms, and can recycle the sludge and sewage in the treatment process. Utilization, high processing efficiency, energy saving and environmental protection, greatly reducing the emission of polluting gases, easy installation, easy maintenance, and low maintenance costs.
为解决以上技术问题,本发明提供了一种养殖业污水污泥模块化处理系统,包括物化处理模块、生物处理模块、沼气利用模块和污泥干化模块;所述物化处理模块包括通过管路依次连通的格栅调节池、物化池和沉淀池,所述生物处理模块包括通过管路依次连通的水解酸化反应池、IC反应池、BAF曝气池和气浮机,所述水解酸化反应池与沉淀池通过管路连通;所述沼气利用模块包括沼气脱硫器、沼气发电机、沼气燃烧炉和沼液收集箱,所述沼气脱硫器的进气口和沼液收集箱的进液口均与IC反应池通过管路连通,所述沼气发电机和沼气燃烧炉的进气口均与沼气脱硫器的出气口通过管路连通;所述污泥干化模块包括依次连通的污泥浓缩池、压滤机、干燥间和污泥焚烧炉,所述污泥浓缩池的滤渣进口与格栅调节池、物化池、沉淀池、IC反应池、BAF曝气池和气浮机的滤渣排出口均通过管路相连通,所述污泥焚烧炉分别与污泥浓缩池和干燥间通过传输热量的管路相连通,所述污泥浓缩池和干燥间还分别与沼气燃烧炉通过传输热量的管路相连通。In order to solve the above technical problems, the present invention provides a modular treatment system for aquaculture sewage sludge, including a physical and chemical treatment module, a biological treatment module, a biogas utilization module and a sludge drying module; the physical and chemical treatment module includes The grid adjustment tank, the materialization tank and the sedimentation tank connected in sequence, the biological treatment module includes the hydrolytic acidification reaction tank, the IC reaction tank, the BAF aeration tank and the air flotation machine connected in sequence through the pipeline, and the hydrolytic acidification reaction tank and the The sedimentation tank is communicated through pipelines; the biogas utilization module includes a biogas desulfurizer, a biogas generator, a biogas burner and a biogas slurry collection box, and the inlet of the biogas desulfurizer and the liquid inlet of the biogas slurry collection box are connected to the The IC reaction pool is connected through pipelines, and the gas inlets of the biogas generator and the biogas burner are connected with the gas outlet of the biogas desulfurizer through pipelines; the sludge drying module includes sludge thickening tanks, Filter press, drying room and sludge incinerator, the filter residue inlet of the sludge thickening tank and the filter residue outlet of the grid adjustment tank, physical and chemical tank, sedimentation tank, IC reaction tank, BAF aeration tank and air flotation machine all pass through The pipelines are connected, and the sludge incinerator is respectively connected with the sludge thickening tank and the drying room through the pipeline for transferring heat, and the sludge thickening tank and the drying room are respectively connected with the biogas combustion furnace through the pipeline for transferring heat connected.
进一步的,所述格栅调节池中的格栅采用上流式格栅。Further, the grills in the grill adjustment pool adopt upflow grills.
进一步的,还包括回水池,所述气浮机和干燥间均与回水池通过管路连通。Further, a return pool is also included, and both the air flotation machine and the drying room are connected with the return pool through pipelines.
为解决以上技术问题,本发明还提供了一种养殖业污水污泥模块化处理系统的处理工艺,首先将养殖污水加入到格栅调节池中以去除污水中的漂浮物和悬浮物,随后将污水从格栅调节池依次排入物化池和沉淀池进行固液分离、水解酸化反应池进行水解酸化处理、IC反应池进行厌氧处理、BAF曝气池进行好氧处理和气浮机进行气浮处理,并对经以上处理之后的污水进行回收再利用;将从上述格栅调节池、物化池、沉淀池、IC反应池、BAF曝气池和气浮机中排出的滤渣均排入污泥浓缩池中进行污泥初步脱水处理,污泥浓缩池的热量由污泥焚烧炉和沼气燃烧炉提供,将经污泥浓缩池处理之后的污泥运送入压滤机中制作泥饼后运送入干燥间进行干燥处理,干燥间的热量由沼气燃烧炉和污泥焚烧炉提供,将经干燥间处理之后的泥饼运送入污泥焚烧炉中进行焚烧产生热量,将经干燥间处理之后产生的污水通过管路运输至回水池中回收利用;另外,将IC反应池中产生的沼气运送入沼气脱硫器中经高压水洗工艺脱硫后再分别运送入沼气发电机进行发电和沼气燃烧炉进行燃烧,同时将IC反应池中的沼液排入沼液收集箱内用作有机化肥料的原料。In order to solve the above technical problems, the present invention also provides a treatment process of a modular sewage sludge treatment system in the aquaculture industry. First, the aquaculture sewage is added to the grid adjustment tank to remove floating and suspended solids in the sewage, and then the Sewage is discharged from the grid adjustment tank into the materialization tank and sedimentation tank in sequence for solid-liquid separation, hydrolysis and acidification reaction tank for hydrolysis and acidification treatment, IC reaction tank for anaerobic treatment, BAF aeration tank for aerobic treatment and air flotation machine for air flotation treatment, and recycle and reuse the sewage after the above treatment; discharge the filter residue discharged from the above-mentioned grid adjustment tank, physical and chemical tank, sedimentation tank, IC reaction tank, BAF aeration tank and air flotation machine into the sludge concentration The preliminary sludge dehydration treatment is carried out in the pool. The heat of the sludge thickening tank is provided by the sludge incinerator and the biogas combustion furnace. The heat in the drying room is provided by the biogas combustion furnace and the sludge incinerator. The mud cake after being treated in the drying room is transported into the sludge incinerator for incineration to generate heat, and the sewage generated after being treated in the drying room is It is transported to the backwater pool for recycling through pipelines; in addition, the biogas generated in the IC reaction pool is transported into the biogas desulfurizer, desulfurized by high-pressure water washing process, and then transported to the biogas generator for power generation and biogas combustion furnace for combustion. The biogas slurry in the IC reaction tank is discharged into the biogas slurry collection box to be used as raw material for organic fertilizer.
进一步的,所述BAF曝气池采用延时曝气工艺控制溶解氧,曝气池内的溶解氧浓度高于3-5mg/L,曝气池出口处溶解氧浓度控制在2mg/l。Further, the BAF aeration tank adopts a delayed aeration process to control dissolved oxygen, the dissolved oxygen concentration in the aeration tank is higher than 3-5 mg/L, and the dissolved oxygen concentration at the outlet of the aeration tank is controlled at 2 mg/l.
进一步的,曝气池内的溶解氧浓度控制在5-10mg/L。Further, the dissolved oxygen concentration in the aeration tank is controlled at 5-10 mg/L.
进一步的,在BAF曝气池对污水进行处理时向BAF曝气池中加入脱水活性污泥,脱水活性污泥的加入量为曝气池蓄水量的0.5%—0.8%。Further, when the BAF aeration tank treats the sewage, add dewatered activated sludge into the BAF aeration tank, and the amount of dehydrated activated sludge added is 0.5%-0.8% of the water storage capacity of the aeration tank.
进一步的,水解酸化池的水力停留时间为8-10小时。Further, the hydraulic retention time of the hydrolytic acidification tank is 8-10 hours.
进一步的,水解酸化池的水力停留时间为10小时。Further, the hydraulic retention time of the hydrolytic acidification tank is 10 hours.
与现有技术相比,本发明的有益效果是:本发明占地面积小,方便安装和维护,维护费用低,可根据实际污泥污水处理的复杂程度进行组件选择性的组装;本发明可实现养殖场污水污泥的模块化处理,可对处理过程中的污泥污水进行资源化循环利用,处理效率高,节能环保,大幅减少了污染性气体的排放,对废水进行了回收利用;本发明在厌氧处理阶段产生的沼气,既可以作为污泥干化时所需高温蒸汽的能量来源,同时在经本系统提供的高压水洗工艺脱硫提纯后,也可作为厌氧阶段的燃料使用,同时可为本系统的所有用电设备提供电能;另外,污泥干化模块使用压滤机与干化脱水处理,将污泥的含水量控制在了40%以下,更易燃烧,保证了干化泥饼的顺利焚烧,干化泥饼还可作为肥料、燃料或制备烧结砖的原料使用,处理完毕的废水也可作为冲洗用水和景观水使用。Compared with the prior art, the beneficial effects of the present invention are: the present invention occupies a small area, is convenient for installation and maintenance, and has low maintenance costs, and can selectively assemble components according to the complexity of actual sludge and sewage treatment; the present invention can Realize the modular treatment of farm sewage sludge, which can recycle the sludge and sewage in the process of treatment, with high treatment efficiency, energy saving and environmental protection, greatly reducing the emission of polluting gases, and recycling waste water; The biogas produced in the anaerobic treatment stage can be used as the energy source of high-temperature steam required for sludge drying, and can also be used as fuel in the anaerobic stage after being desulfurized and purified by the high-pressure water washing process provided by this system. At the same time, it can provide electric energy for all electrical equipment in this system; in addition, the sludge drying module uses a filter press and drying dehydration treatment to control the water content of the sludge below 40%, which is easier to burn and ensures drying The mud cake is incinerated smoothly, and the dried mud cake can also be used as fertilizer, fuel or raw material for preparing sintered bricks, and the treated wastewater can also be used as flushing water and landscape water.
附图说明Description of drawings
图1为本发明的实施例提供的处理系统的原理框架图。FIG. 1 is a schematic frame diagram of a processing system provided by an embodiment of the present invention.
具体实施方式Detailed ways
为使本发明的目的、技术方案和优点更加清楚明白,下面结合实施例和附图,对本发明作进一步的详细说明,本发明的示意性实施方式及其说明仅用于解释本发明,并不作为对本发明的限定。In order to make the purpose, technical solutions and advantages of the present invention clearer, the present invention will be further described in detail below in conjunction with the examples and accompanying drawings. As a limitation of the present invention.
实施例:Example:
参见图1,一种养殖业污水污泥模块化处理系统,本处理系统包括物化处理模块、生物处理模块、沼气利用模块、污泥干化模块和回水池。Referring to Figure 1, a modular treatment system for aquaculture sewage sludge, the treatment system includes a physical and chemical treatment module, a biological treatment module, a biogas utilization module, a sludge drying module and a return pond.
物化处理模块包括通过管路依次连通的格栅调节池、物化池和沉淀池,养殖污水依次流入格栅调节池、物化池和沉淀池,格栅调节池中的格栅采用上流式格栅,可达到不易堵塞和易于清污的目的,格栅调节池用于去除污泥污水中的漂浮物和悬浮物,物化池和沉淀池用于对污水中的固液进行分离。The physical and chemical treatment module includes a grid regulating tank, a physical and chemical tank and a sedimentation tank that are connected in sequence through pipelines. The aquaculture sewage flows into the grid regulating tank, physical and chemical tank and sedimentation tank in sequence. It can achieve the purpose of not easy to block and easy to clean. The grid adjustment tank is used to remove floating and suspended solids in sludge sewage, and the physical and chemical tank and sedimentation tank are used to separate solid and liquid in sewage.
生物处理模块包括通过管路依次连通的水解酸化反应池、IC反应池、BAF曝气池和气浮机,水解酸化反应池与沉淀池通过管路连通,沉淀池中的污泥污水可从沉淀池流入水解酸化反应池中,随后从水解酸化反应池依次流入IC反应池、BAF曝气池和气浮机中进行相应的处理;气浮机与回水池通过排水管路相连,气浮机处理之后且达到标准的废水可作为回用水冲洗畜舍或作为景观水使用。The biological treatment module includes a hydrolytic acidification reaction tank, an IC reaction tank, a BAF aeration tank and an air flotation machine connected in sequence through pipelines. The hydrolytic acidification reaction tank and the sedimentation tank are connected through pipelines, and the sludge and sewage in the sedimentation tank can be collected from the sedimentation tank. It flows into the hydrolytic acidification reaction tank, and then flows into the IC reaction tank, BAF aeration tank and air flotation machine from the hydrolytic acidification reaction tank for corresponding treatment; The wastewater that reaches the standard can be used as reused water for flushing livestock houses or as landscape water.
沼气利用模块包括沼气脱硫器、沼气发电机、沼气燃烧炉和沼液收集箱,沼气脱硫器的进气口和沼液收集箱的进液口均与IC反应池通过管路连通,沼气发电机的进气口和沼气燃烧炉的进气口均与沼气脱硫器的出气口通过管路连通;IC反应池中产生的沼气进入沼气脱硫器中经过高压水洗工艺脱硫处理后,分别进入沼气发电机和沼气燃烧炉,沼气发电机利用沼气产生电能为本处理系统供电,沼气燃烧炉通过燃烧沼气而产生热能供污泥干化模块使用;另外,沼液收集箱收集IC反应池中的沼液,沼液可作为有机化肥料的原料。The biogas utilization module includes a biogas desulfurizer, a biogas generator, a biogas burner and a biogas slurry collection box. Both the gas inlet of the biogas desulfurizer and the liquid inlet of the biogas slurry collection box are connected to the IC reaction pool through pipelines, and the biogas generator The air inlet of the biogas burner and the air inlet of the biogas burner are connected with the gas outlet of the biogas desulfurizer through pipelines; the biogas generated in the IC reaction tank enters the biogas desulfurizer and is desulfurized by high-pressure water washing process, and then enters the biogas generator respectively. And the biogas combustion furnace, the biogas generator uses biogas to generate electricity to power the treatment system, and the biogas combustion furnace generates heat energy for the sludge drying module by burning biogas; in addition, the biogas slurry collection box collects the biogas slurry in the IC reaction tank, Biogas slurry can be used as a raw material for organic fertilizers.
污泥干化模块包括依次连通的污泥浓缩池、压滤机、干燥间和污泥焚烧炉,污泥浓缩池的滤渣进口与格栅调节池、物化池、沉淀池、IC反应池、BAF曝气池和气浮机的滤渣排出口均通过管路相连通,污泥焚烧炉分别与污泥浓缩池和干燥间通过传输热量的管路相连通,污泥浓缩池和干燥间还分别与沼气燃烧炉通过传输热量的管路相连通,干燥间与回水池通过排水管路相连;从格栅调节池、物化池、沉淀池、IC反应池、BAF曝气池和气浮机中排出的滤渣均进入污泥浓缩池,沼气燃烧炉和污泥焚烧炉中的热气通过传输热量的管路进入污泥浓缩池内,对污泥浓缩池内的污泥进行加热,以降低污泥浓缩池中的污泥的含水量,以便于后期压滤机处理;通过压滤机对从污泥浓缩池中排出的污泥进行处理而得到泥饼,部分泥饼可运出去进行好氧堆肥处理用于还田,部分泥饼打孔后进入干燥间,沼气燃烧炉和污泥焚烧炉中的热气通过传输热量的管路进入干燥间内,对干燥间内的泥饼进行加热后使泥饼干化,干化后的泥饼可作为制砖和肥料的原料使用,同时可将部分干化后的泥饼投入污泥焚烧炉中进行焚烧以产生热量供污泥浓缩池和干燥间使用;污泥干化后得到的不含污染性物质的污水,可回流至回水池中作为回用水冲洗畜舍。The sludge drying module includes a sludge thickening tank, a filter press, a drying room and a sludge incinerator connected in sequence, the filter residue inlet of the sludge thickening tank and the grid adjustment tank, a physicochemical tank, a sedimentation tank, an IC reaction tank, and a BAF The filter residue outlets of the aeration tank and the air flotation machine are connected through pipelines, and the sludge incinerator is respectively connected with the sludge thickening tank and the drying room through heat transfer pipelines, and the sludge thickening tank and the drying room are also connected with the biogas The combustion furnace is connected through the heat transfer pipeline, and the drying room is connected with the return pool through the drainage pipeline; the filter residue discharged from the grid adjustment tank, the physical and chemical tank, the sedimentation tank, the IC reaction tank, the BAF aeration tank and the air flotation machine are all Entering the sludge concentration tank, the hot gas in the biogas burner and sludge incinerator enters the sludge concentration tank through the heat transfer pipeline, and heats the sludge in the sludge concentration tank to reduce the sludge concentration in the sludge concentration tank. water content, so as to facilitate the later treatment of the filter press; the sludge discharged from the sludge thickening tank is processed by the filter press to obtain mud cakes, and part of the mud cakes can be transported out for aerobic composting treatment for returning to the field. Part of the mud cake enters the drying room after being perforated, and the hot gas in the biogas incinerator and sludge incinerator enters the drying room through the heat transfer pipeline, and the mud cake in the drying room is heated to make the mud biscuit, and after drying The mud cake can be used as a raw material for making bricks and fertilizers. At the same time, the partially dried mud cake can be put into the sludge incinerator for incineration to generate heat for use in the sludge thickening tank and drying room; after the sludge is dried, it can be obtained The sewage without polluting substances can be returned to the backwater pool as reused water for flushing the livestock house.
除了本发明指明的技术特征和相关工艺之外,本发明中的格栅调节池、物化池、沉淀池、水解酸化反应池、IC反应池、BAF曝气池、气浮机、沼气脱硫器、沼气发电机、沼气燃烧炉、沼液收集箱、污泥浓缩池、压滤机、干燥间、污泥焚烧炉和回水池等均为常见的废水处理结构。In addition to the technical features and related processes specified in the present invention, the grid adjustment tank, physical and chemical tank, sedimentation tank, hydrolysis acidification reaction tank, IC reaction tank, BAF aeration tank, air flotation machine, biogas desulfurizer, Biogas generators, biogas burners, biogas slurry collection tanks, sludge thickening tanks, filter presses, drying rooms, sludge incinerators and backwater tanks are all common wastewater treatment structures.
本发明还提供了一种养殖业污水污泥模块化处理系统的处理工艺,首先将养殖污水加入到格栅调节池中以去除污水中的漂浮物和悬浮物,随后将污水从格栅调节池依次排入物化池和沉淀池进行固液分离、水解酸化反应池进行水解酸化处理、IC反应池进行厌氧处理、BAF曝气池进行好氧处理和气浮机进行气浮处理,并对经以上处理之后的污水进行回收再利用;将从上述格栅调节池、物化池、沉淀池、IC反应池、BAF曝气池和气浮机中排出的滤渣均排入污泥浓缩池中进行污泥初步脱水处理,污泥浓缩池的热量由污泥焚烧炉和沼气燃烧炉提供,将经污泥浓缩池处理之后的污泥运送入压滤机中制作泥饼后运送入干燥间进行干燥处理,干燥间的热量由沼气燃烧炉和污泥焚烧炉提供,将经干燥间处理之后的泥饼运送入污泥焚烧炉中进行焚烧产生热量,将经干燥间处理之后产生的污水通过管路运输至回水池中回收利用;另外,将IC反应池中产生的沼气运送入沼气脱硫器中经高压水洗工艺脱硫后再分别运送入沼气发电机进行发电和沼气燃烧炉进行燃烧,同时将IC反应池中的沼液排入沼液收集箱内用作有机化肥料的原料。The present invention also provides a treatment process of a modular sewage sludge treatment system in the aquaculture industry. First, the aquaculture sewage is added to the grid adjustment tank to remove floating and suspended matter in the sewage, and then the sewage is discharged from the grid adjustment tank Sequentially discharged into the physical and chemical tank and sedimentation tank for solid-liquid separation, hydrolytic acidification reaction tank for hydrolytic acidification treatment, IC reaction tank for anaerobic treatment, BAF aeration tank for aerobic treatment and air flotation machine for air flotation treatment, and the above The treated sewage is recycled and reused; the filter residues discharged from the above-mentioned grid adjustment tank, physical and chemical tank, sedimentation tank, IC reaction tank, BAF aeration tank and air flotation machine are all discharged into the sludge thickening tank for sludge preliminary treatment. Dehydration treatment, the heat of the sludge concentration tank is provided by the sludge incinerator and biogas combustion furnace, and the sludge treated in the sludge concentration tank is transported into the filter press to make mud cakes and then transported to the drying room for drying treatment. The heat in the room is provided by the biogas combustion furnace and the sludge incinerator. The mud cake treated in the drying room is transported into the sludge incinerator for incineration to generate heat. In addition, the biogas generated in the IC reaction pool is transported to the biogas desulfurizer and desulfurized by the high-pressure water washing process, and then transported to the biogas generator for power generation and biogas combustion furnace for combustion. At the same time, the biogas in the IC reaction pool The biogas slurry is discharged into the biogas slurry collection box and used as raw material for organic fertilizer.
上述BAF曝气池采用延时曝气工艺控制溶解氧,将曝气池内的溶解氧浓度控制在高于3-5mg/L,本实施例中的曝气池内的溶解氧浓度控制在5-10mg/L,曝气池出口处溶解氧浓度控制在2mg/l,在进行充分的延时曝气处理后活性污泥进入了微生物内源代谢阶段,因此,会减少排泥量;在BAF曝气池对污水进行处理时向BAF曝气池中加入脱水活性污泥,脱水活性污泥的加入量为曝气池蓄水量的0.5%—0.8%,加入脱水活性污泥可调节污水性能,增加其吸附性,为后续处理创造有利条件,降低了系统的运行费用;水解酸化池的水力停留时间为8-10小时,本实施例中的水解酸化池的水力停留时间为10小时,经实验发现,当水力停留时间为8h时,污水中的COD的去除率为21%~23%,提高水力停留时间至10h时,COD的去除率可提高至26%~29%,继续提高水力停留时间则对COD的去除无明显作用,水解酸化池SS的去除在停留时间相当稳定,去除率维持在70%~75%,本发明综合不同水力停留时间下COD和SS的去除情况,水解酸化池最佳水力停留时间选择为10h,此时,水解酸化池pH稳定在6.5~6.7,COD去除率为27%左右,总磷去除率在4%~6%,提高了废水的可生化性。The above-mentioned BAF aeration tank adopts a delayed aeration process to control dissolved oxygen, and the dissolved oxygen concentration in the aeration tank is controlled to be higher than 3-5 mg/L, and the dissolved oxygen concentration in the aeration tank in this embodiment is controlled at 5-10 mg /L, the dissolved oxygen concentration at the outlet of the aeration tank is controlled at 2mg/l, after sufficient delayed aeration treatment, the activated sludge enters the stage of microbial endogenous metabolism, therefore, the amount of sludge discharge will be reduced; in BAF aeration Add dewatered activated sludge to the BAF aeration tank when the tank treats the sewage. The amount of dehydrated activated sludge added is 0.5%-0.8% of the water storage capacity of the aeration tank. Adding dehydrated activated sludge can adjust the sewage performance and increase Its adsorption creates favorable conditions for follow-up treatment and reduces the operating cost of the system; the hydraulic retention time of the hydrolytic acidification tank is 8-10 hours, and the hydraulic retention time of the hydrolytic acidification tank in the present embodiment is 10 hours. It is found through experiments , when the hydraulic retention time is 8h, the removal rate of COD in the sewage is 21% to 23%, and when the hydraulic retention time is increased to 10h, the COD removal rate can be increased to 26% to 29%. It has no obvious effect on the removal of COD. The removal of SS in the hydrolytic acidification tank is quite stable at the residence time, and the removal rate is maintained at 70% to 75%. The hydraulic retention time is selected as 10h. At this time, the pH of the hydrolytic acidification tank is stable at 6.5-6.7, the removal rate of COD is about 27%, and the removal rate of total phosphorus is 4%-6%, which improves the biodegradability of wastewater.
如上即为本发明的实施例。上述实施例以及实施例中的具体参数仅是为了清楚表述发明验证过程,并非用以限制本发明的专利保护范围,本发明的专利保护范围仍然以其权利要求书为准,凡是运用本发明的说明书及附图内容所作的等同结构变化,同理均应包含在本发明的保护范围内。The above is the embodiment of the present invention. The specific parameters in the above-mentioned embodiments and the embodiments are only for clearly expressing the invention verification process, and are not used to limit the scope of patent protection of the present invention. The scope of patent protection of the present invention is still subject to its claims. Equivalent structural changes made in the description and accompanying drawings should all be included in the protection scope of the present invention.
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