CN104386887B - A kind of bean curd factory effluent minitype direct exhaust type biological treatment and equipment - Google Patents
A kind of bean curd factory effluent minitype direct exhaust type biological treatment and equipment Download PDFInfo
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- 235000013527 bean curd Nutrition 0.000 title claims abstract description 41
- 239000002351 wastewater Substances 0.000 claims abstract description 70
- 238000000034 method Methods 0.000 claims abstract description 48
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 43
- 238000004519 manufacturing process Methods 0.000 claims abstract description 34
- 230000001105 regulatory effect Effects 0.000 claims abstract description 20
- 239000000463 material Substances 0.000 claims abstract description 7
- 238000012856 packing Methods 0.000 claims abstract description 7
- 230000001276 controlling effect Effects 0.000 claims abstract description 4
- 238000005273 aeration Methods 0.000 claims description 17
- 239000012535 impurity Substances 0.000 claims description 7
- 238000004062 sedimentation Methods 0.000 claims description 6
- 238000001556 precipitation Methods 0.000 claims description 5
- 239000002245 particle Substances 0.000 claims description 4
- 238000002203 pretreatment Methods 0.000 claims 1
- 230000000694 effects Effects 0.000 abstract description 5
- 238000004065 wastewater treatment Methods 0.000 abstract description 2
- 239000007787 solid Substances 0.000 description 7
- 239000010865 sewage Substances 0.000 description 5
- 239000010802 sludge Substances 0.000 description 5
- 238000005259 measurement Methods 0.000 description 3
- 244000005700 microbiome Species 0.000 description 3
- 238000012163 sequencing technique Methods 0.000 description 3
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- 241000255925 Diptera Species 0.000 description 2
- 238000004458 analytical method Methods 0.000 description 2
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 2
- 230000003247 decreasing effect Effects 0.000 description 2
- 239000000945 filler Substances 0.000 description 2
- 229910052760 oxygen Inorganic materials 0.000 description 2
- 239000001301 oxygen Substances 0.000 description 2
- 238000011160 research Methods 0.000 description 2
- 238000005070 sampling Methods 0.000 description 2
- 238000001179 sorption measurement Methods 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 244000068988 Glycine max Species 0.000 description 1
- 235000010469 Glycine max Nutrition 0.000 description 1
- 235000010627 Phaseolus vulgaris Nutrition 0.000 description 1
- 244000046052 Phaseolus vulgaris Species 0.000 description 1
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 description 1
- 108010073771 Soybean Proteins Proteins 0.000 description 1
- 229920002472 Starch Polymers 0.000 description 1
- 230000002411 adverse Effects 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000010170 biological method Methods 0.000 description 1
- 230000003139 buffering effect Effects 0.000 description 1
- SOCTUWSJJQCPFX-UHFFFAOYSA-N dichromate(2-) Chemical compound [O-][Cr](=O)(=O)O[Cr]([O-])(=O)=O SOCTUWSJJQCPFX-UHFFFAOYSA-N 0.000 description 1
- 238000006073 displacement reaction Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 235000019197 fats Nutrition 0.000 description 1
- 238000000855 fermentation Methods 0.000 description 1
- 230000004151 fermentation Effects 0.000 description 1
- 238000011010 flushing procedure Methods 0.000 description 1
- 235000013305 food Nutrition 0.000 description 1
- 238000000265 homogenisation Methods 0.000 description 1
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- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 231100000252 nontoxic Toxicity 0.000 description 1
- 230000003000 nontoxic effect Effects 0.000 description 1
- 235000015097 nutrients Nutrition 0.000 description 1
- 229910052698 phosphorus Inorganic materials 0.000 description 1
- 239000011574 phosphorus Substances 0.000 description 1
- 235000018102 proteins Nutrition 0.000 description 1
- 108090000623 proteins and genes Proteins 0.000 description 1
- 102000004169 proteins and genes Human genes 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 239000002002 slurry Substances 0.000 description 1
- 235000019710 soybean protein Nutrition 0.000 description 1
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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
- C02F9/00—Multistage treatment of water, waste water or sewage
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2103/00—Nature of the water, waste water, sewage or sludge to be treated
- C02F2103/32—Nature of the water, waste water, sewage or sludge to be treated from the food or foodstuff industry, e.g. brewery waste waters
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2301/00—General aspects of water treatment
- C02F2301/08—Multistage treatments, e.g. repetition of the same process step under different conditions
-
- 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
- C02F3/301—Aerobic and anaerobic treatment in the same reactor
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- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Activated Sludge Processes (AREA)
- Biological Treatment Of Waste Water (AREA)
Abstract
本发明涉及一种豆腐生产废水小型直排式生物处理工艺及设备,属于废水处理领域,为了克服现有处理豆腐生产废水方法对于小型企业存在的困难,该设备包括控制器、带有格栅的调节池、SBR池、第一电磁阀、通过进气管与SBR池内部联通的空气泵、设置在SBR池内部的多孔填料和水位传感器、设置在SBR池底部的垫层、设置在SBR池底部的排水口、控制SBR池的排水口开关的第二电磁阀,SBR池底部的垫层的制作材料为粗糙材料。本发明中的设备易操作、工艺简单易行、成本低、效果好,具有环境和社会的双重效益,非常适合小水量的豆腐生产废水,可以被小型企业运用,还可应用于其他高浓度废水的处理,具有良好的应用前景。
The invention relates to a small-scale direct-discharge biological treatment process and equipment for tofu production wastewater, which belongs to the field of wastewater treatment. In order to overcome the difficulties existing in the existing methods for treating tofu production wastewater for small enterprises, the equipment includes a controller, a grille The regulating pool, the SBR pool, the first solenoid valve, the air pump communicated with the inside of the SBR pool through the air intake pipe, the porous packing and the water level sensor set inside the SBR pool, the cushion layer set at the bottom of the SBR pool, the water level sensor set at the bottom of the SBR pool Drain, the second electromagnetic valve controlling the switch of the drain of the SBR pool, and the cushion layer at the bottom of the SBR pool are made of rough materials. The equipment in the present invention is easy to operate, the process is simple and easy to implement, the cost is low, and the effect is good. It has double benefits of the environment and society. It is very suitable for small-volume tofu production wastewater, can be used by small enterprises, and can also be applied to other high-concentration wastewater The treatment has a good application prospect.
Description
技术领域technical field
本发明属于废水处理领域,具体涉及一种豆腐生产废水小型直排式生物处理工艺及设备。The invention belongs to the field of wastewater treatment, and in particular relates to a small-scale direct-discharge biological treatment process and equipment for wastewater from tofu production.
背景技术Background technique
豆腐是人们日常的食品,但其制作过程中会产生大量的废水,一般认为单位质量豆腐成品和排放废水的比例在1:10以上,即生产1kg豆腐至少产生10L废水。由于市场上50%以上的豆腐由分布在城郊结合部的豆腐作坊废水生产,废水水量小而分散,但污染程度高,排放方式大都是直接排放,其后果一是增加了市政污水管网的负荷,二是容易产生臭气、滋生蚊蝇而影响周围环境和人类健康。豆腐生产过程中产生废水主要是泡豆水、黄浆水和车间冲洗水。豆腐生产废水含有其中含有大量的蛋白质、脂肪、淀粉等营养物质,从污水处理角度而言,排放的豆腐生产废水水质指标范围为:CODcr(重铬酸盐指数)含量在2000-20000mg/L,BOD5(消耗的溶解氧量)含量在800-12000mg/L,是一种高浓度有机废水,但无毒无害,适用于生物处理。Tofu is a daily food for people, but a large amount of waste water will be generated in the production process. It is generally believed that the ratio of unit mass of tofu finished product and discharged waste water is more than 1:10, that is, the production of 1 kg of tofu produces at least 10 L of waste water. Since more than 50% of the tofu in the market is produced by the waste water of tofu workshops distributed in the suburbs of the city, the amount of waste water is small and scattered, but the degree of pollution is high, and the discharge method is mostly direct discharge. The first consequence is to increase the load on the municipal sewage pipe network Second, it is easy to produce odor, breed mosquitoes and flies and affect the surrounding environment and human health. The waste water produced in the tofu production process is mainly soaked bean water, yellow slurry water and workshop flushing water. Tofu production wastewater contains a large amount of protein, fat, starch and other nutrients. From the perspective of sewage treatment, the range of water quality indicators for the discharged tofu production wastewater is: CODcr (dichromate index) content is 2000-20000mg/L, The content of BOD5 (consumed dissolved oxygen) is 800-12000mg/L, which is a kind of high-concentration organic wastewater, but it is non-toxic and harmless, and is suitable for biological treatment.
目前国内外主要采用生物法处理豆腐生产废水,主要有厌氧生物处理法、好氧处理法和序批式生物反应器法(SBR),由于序批式生物反应器法(SBR)具有间歇运行、好氧厌氧交替、脱氮除磷等特点,非常适合豆腐废水的排放特点。上述方法在规模化豆制品生产企业均有采用,有条件的还进行了大豆蛋白等有用物质的回收,由于污水处理是个系统工程,处理的废水量大,多见于为大型企业,但同时对设备和人员的要求高,将这些工艺设备直接用于小型豆腐生产废水,由于难于实现小型废水的集中收集,不能够充分发挥设备的功效。对于小型企业(排水量≤1吨/天),由于缺乏资金和技术,引进成套设备增加了成本,更不用说回收利用了,同时小型企业产生的废水量小,但又不能直接排入下水道,否则易造成腐败发酵甚至下水道堵塞影响周围环境。At present, biological methods are mainly used to treat tofu production wastewater at home and abroad, mainly including anaerobic biological treatment method, aerobic treatment method and sequencing batch bioreactor (SBR), because sequencing batch bioreactor (SBR) has intermittent operation , aerobic and anaerobic alternation, nitrogen and phosphorus removal, etc., are very suitable for the discharge characteristics of tofu wastewater. The above method has been adopted in large-scale soybean product production enterprises, and some useful substances such as soybean protein have also been recovered if possible. Since sewage treatment is a systematic project, the amount of wastewater treated is large, and it is more common in large-scale enterprises, but at the same time, the equipment The requirements for personnel and personnel are high, and these process equipment are directly used for small-scale tofu production wastewater. Because it is difficult to realize the centralized collection of small-scale wastewater, the efficacy of the equipment cannot be fully utilized. For small enterprises (displacement ≤ 1 ton/day), due to lack of capital and technology, the introduction of complete sets of equipment increases the cost, let alone recycling. At the same time, the amount of waste water produced by small enterprises is small, but it cannot be directly discharged into the sewer, otherwise It is easy to cause corruption and fermentation and even sewer blockage to affect the surrounding environment.
发明内容Contents of the invention
为了克服现有处理豆腐生产废水方法对于小型企业存在的困难,本发明提供一种豆腐生产废水小型直排式生物处理工艺及设备。In order to overcome the difficulties existing in small enterprises in the existing methods for treating wastewater from tofu production, the invention provides a small-scale direct discharge biological treatment process and equipment for wastewater from tofu production.
本发明的技术方案是:一种豆腐生产废水小型直排式生物处理工艺的设备,该设备包括带有格栅的调节池、SBR池、连接调节池出水口和SBR池进水口的第一电磁阀、通过进气管与SBR池内部联通的空气泵、设置在SBR池内部的水位传感器、设置在SBR池底部的垫层、设置在SBR池底部的排水口、控制SBR池的排水口开关的第二电磁阀、与水位传感器连接并控制第一电磁阀和第二电磁阀的控制器,SBR池底部的垫层的制作材料为粗糙材料。The technical solution of the present invention is: a small-scale direct discharge type biological treatment process equipment for tofu production wastewater, which includes a regulating tank with a grid, an SBR tank, a first electromagnetic tank connecting the water outlet of the regulating tank and the water inlet of the SBR tank. Valve, the air pump connected to the inside of the SBR pool through the intake pipe, the water level sensor set inside the SBR pool, the cushion layer set at the bottom of the SBR pool, the drain port set at the bottom of the SBR pool, and the first switch for controlling the drain switch of the SBR pool Two solenoid valves, a controller connected to the water level sensor and controlling the first solenoid valve and the second solenoid valve, and the cushion layer at the bottom of the SBR pool are made of rough materials.
所述格栅上开孔的直径小于1毫米。The diameter of the holes on the grid is less than 1mm.
所述调节池的容积要大于1立方米。The volume of the regulating pool is greater than 1 cubic meter.
所述SBR池内部还设有多孔填料,多孔填料为空心球形填料,其固定设置在排水口的周围。The inside of the SBR pool is also provided with porous fillers, which are hollow spherical fillers and are fixedly arranged around the drain outlet.
所述排水口设置于SBR池底部的中心位置,将排水口的开口位置被抬高。The drain port is set at the center of the bottom of the SBR pool, and the opening position of the drain port is raised.
所述SBR池池底从中心至四壁抬高有2%的坡度。The bottom of the SBR pool is raised with a slope of 2% from the center to the four walls.
一种豆腐生产废水小型直排式生物处理工艺,该工艺的处理过程按先后顺序被分为预处理和SBR池主处理两个过程,其中,SBR池主处理主要流程包括:进水、曝气、沉淀、排水和闲置。A small-scale direct-discharge biological treatment process for tofu production wastewater. The treatment process of this process is divided into two processes: pretreatment and SBR tank main treatment in sequence. Among them, the main process of SBR tank main treatment includes: water intake, aeration , sedimentation, drainage and idle.
该工艺的具体流程如下:步骤1,第一电磁阀关闭,步骤2,豆腐生产产生的废水通过阻拦下废水中的大颗粒物和大直径杂质的格栅流入调节池,步骤3,废水在调节池内进行杂质沉淀的预处理,步骤4,预处理完成后,控制器控制第一电磁阀打开,废水通过调节池出水口进入SBR池,步骤5,SBR池内的水位传感器感应到SBR池内的废水达到设定水位后,控制器控制第一电磁阀关闭,同时控制器控制空气泵开启,对SBR池内的废水进行曝气处理,步骤6,曝气处理后,控制器控制空气泵停止运行,SBR池内的废水进入沉淀时间,步骤7,沉淀后,控制器控制第二电磁阀打开,开始排水,步骤8,排水完成后,控制器控制第二电磁阀关闭,返回步骤2。The specific flow of the process is as follows: step 1, the first solenoid valve is closed, step 2, the waste water produced by tofu production flows into the regulating tank through the grid that blocks the large particles and large-diameter impurities in the waste water, and step 3, the waste water is in the regulating tank Carry out the pretreatment of impurity precipitation, step 4, after the pretreatment is completed, the controller controls the first solenoid valve to open, the waste water enters the SBR pool through the outlet of the regulating pool, step 5, the water level sensor in the SBR pool senses that the waste water in the SBR pool reaches the set level After the water level is fixed, the controller controls the first electromagnetic valve to close, and at the same time the controller controls the air pump to open to aerate the wastewater in the SBR tank. Step 6. After the aeration treatment, the controller controls the air pump to stop running, and the water in the SBR tank The waste water enters the sedimentation time, step 7, after sedimentation, the controller controls the second electromagnetic valve to open, and starts to drain, step 8, after the drainage is completed, the controller controls the second electromagnetic valve to close, and returns to step 2.
所述曝气处理的时间为2小时。The time of the aeration treatment is 2 hours.
所述沉淀时间为1小时。The precipitation time is 1 hour.
本发明的有益效果为:本发明中的设备易操作、工艺简单易行、成本低、效果好,具有环境和社会的双重效益,非常适合小水量(<1吨)的豆腐生产废水,可以被小型企业运用,还可应用于其他高浓度废水的处理,具有良好的应用前景。The beneficial effects of the present invention are: the equipment in the present invention is easy to operate, the process is simple and easy, the cost is low, the effect is good, and there are double benefits of the environment and society, and it is very suitable for the tofu production wastewater with a small amount of water (<1 ton), and can be processed by It is used by small enterprises and can also be applied to the treatment of other high-concentration wastewater, which has a good application prospect.
附图说明Description of drawings
图1为本发明具体实施方式豆腐生产废水小型直排式生物处理设备的结构示意图;Fig. 1 is the structural representation of the tofu production waste water small-scale straight discharge type biological treatment equipment of the specific embodiment of the present invention;
图中,1为格栅,2为调节池,3为第一电磁阀,4为SBR池,5为空气泵,6为空心球形填料,7为排水口,8为垫层,9为第二电磁阀。In the figure, 1 is the grille, 2 is the regulating pool, 3 is the first solenoid valve, 4 is the SBR pool, 5 is the air pump, 6 is the hollow spherical packing, 7 is the drainage port, 8 is the cushion, 9 is the second The electromagnetic valve.
具体实施方式detailed description
下面对照附图,通过对实施例的描述,本发明的具体实施方式如所涉及的各构件的形状、构造、各部分之间的相互位置及连接关系、各部分的作用及工作原理、制造工艺及操作使用方法等,作进一步详细的说明,以帮助本领域技术人员对本发明的发明构思、技术方案有更完整、准确和深入的理解。Referring to the accompanying drawings, through the description of the embodiments, the specific embodiments of the present invention include the shape, structure, mutual position and connection relationship of each part, the function and working principle of each part, and the manufacturing process of the various components involved. And the method of operation and use, etc., are described in further detail to help those skilled in the art have a more complete, accurate and in-depth understanding of the inventive concepts and technical solutions of the present invention.
如图1所示,一种豆腐生产废水小型直排式生物处理工艺的设备,该设备包括带有格栅1的调节池2、SBR(序批式生物反应器法)池4、连接调节池2出水口和SBR池4进水口的第一电磁阀3、通过进气管与SBR池4内部联通的空气泵5、设置在SBR池4内部的空心球形填料6和水位传感器、设置在SBR池4底部的垫层8、设置在SBR池4底部的排水口7、控制SBR池4的排水口7开关的第二电磁阀9、与水位传感器连接并控制第一电磁阀3和第二电磁阀9的控制器。为了拦截废水中的大颗粒物和大直径杂质,所述格栅1上开孔的直径小于1毫米。由于小型豆腐厂一般废水产生阶段较为集中,为了容纳废水,调节池2的容积大小要保证能容纳小型豆腐厂一天的废水量,而小型豆腐厂的排水量≤1吨/天,故调节池2的容积要大于1立方米。为了加强微生物的吸附和减缓排水时的水流流速,SBR池4底部的垫层8的制作材料为粗糙材料,在进行排水时,粗糙材料制作的垫层8还会使得污泥不易被水流带走,同时,初始排掉了部分污泥又起到了微生物更新的作用。为了增加微生物的附着效果,对水流进行二次缓冲及吸附,进一步降低污泥损失,空心球形填料6固定设置在排水口7的周围,排水口7设置于SBR池4的中心位置,为了进一步减缓水流带动池底微生物的不利影响,将排水口7的开口位置被抬高,使得SBR池4池底从中心至四壁有一定的抬高坡度,该坡度为2%。As shown in Fig. 1, a kind of equipment of tofu production wastewater small-scale in-line biological treatment process, this equipment comprises the adjusting pool 2 with grid 1, SBR (sequencing batch bioreactor method) pool 4, connecting adjusting pool 2 The first solenoid valve 3 of the water outlet and the water inlet of the SBR pool 4, the air pump 5 communicating with the interior of the SBR pool 4 through the intake pipe, the hollow spherical packing 6 and the water level sensor arranged inside the SBR pool 4, and the water level sensor arranged in the SBR pool 4 The cushion layer 8 at the bottom, the drain outlet 7 arranged at the bottom of the SBR pool 4, the second solenoid valve 9 that controls the switch of the drain outlet 7 of the SBR pool 4, is connected with the water level sensor and controls the first solenoid valve 3 and the second solenoid valve 9 controller. In order to intercept large particles and large-diameter impurities in the waste water, the diameter of the holes on the grid 1 is less than 1 mm. Since small-scale tofu factories generally produce more concentrated waste water, in order to accommodate the waste water, the volume of the regulating pool 2 must ensure that it can accommodate the daily waste water volume of the small tofu factory, and the discharge of the small tofu factory is ≤ 1 ton per day, so the volume of the regulating pool 2 The volume must be greater than 1 cubic meter. In order to strengthen the adsorption of microorganisms and slow down the water flow rate during drainage, the material of the cushion layer 8 at the bottom of the SBR pool 4 is rough material. When draining, the cushion layer 8 made of rough material will also make the sludge difficult to be taken away by the water flow. , At the same time, part of the sludge was initially discharged and played a role in microbial renewal. In order to increase the attachment effect of microorganisms, perform secondary buffering and adsorption on the water flow, and further reduce the sludge loss, the hollow spherical packing 6 is fixedly arranged around the outlet 7, and the outlet 7 is arranged at the center of the SBR pool 4, in order to further slow down the sludge loss. The water flow drives the adverse effect of microorganisms at the bottom of the pool, and the opening position of the drain outlet 7 is raised, so that the bottom of the SBR pool 4 has a certain elevation slope from the center to the four walls, and the slope is 2%.
经过以上措施后,通过实验证明在小流量的出水条件下,仅在初始10分钟左右排水口7的出水会携带部分污泥而流失,排出的水悬浮固体浓度(MLSS)为大于3g/L,但10分钟后,出水较为澄清,排出的水MLSS为0.75g/L,随排水时间的增加,出水的MLSS最终保持小于0.3g/L的值,从而实现了直接排水。After the above measures, it has been proved by experiments that under the condition of small flow of water outlet, only in the initial 10 minutes or so, the outlet water of the outlet 7 will carry part of the sludge and be lost, and the concentration of suspended solids (MLSS) in the discharged water is greater than 3g/L. But after 10 minutes, the effluent was relatively clear, and the MLSS of the discharged water was 0.75g/L. With the increase of drainage time, the MLSS of the effluent finally remained at a value less than 0.3g/L, thus realizing direct drainage.
一种豆腐生产废水小型直排式生物处理工艺,该工艺的处理方式为预处理和SBR池主处理两个过程串联,主要流程包括:进水、曝气、沉淀、排水和闲置。具体流程如下:步骤1,第一电磁阀3关闭,步骤2,豆腐生产产生的废水通过阻拦下废水中的大颗粒物和大直径杂质的格栅1流入调节池2,步骤3,废水在调节池2内进行预处理,预处理就是对进入调节池2的废水进行杂质沉淀,有利于均匀化废水,有效地降低了有机污染的初始浓度,步骤4,预处理完成后,控制器控制第一电磁阀3打开,废水通过调节池2出水口进入SBR池4,步骤5,SBR池4内的水位传感器感应到SBR池4内的废水达到设定水位后,控制器控制第一电磁阀3关闭,同时控制器控制空气泵5开启,对SBR池4内的废水进行曝气处理,步骤6,曝气处理2小时后,控制器控制空气泵5停止运行,SBR池4内的废水进入沉淀时间,步骤7,沉淀1小时后,控制器控制第二电磁阀9打开,开始排水,步骤8,排水完成后,控制器控制第二电磁阀9关闭,返回步骤2。A small-scale direct-discharge biological treatment process for tofu production wastewater. The treatment method of the process is that the two processes of pretreatment and SBR tank main treatment are connected in series. The main process includes: water intake, aeration, sedimentation, drainage and idle. The specific process is as follows: step 1, the first solenoid valve 3 is closed, step 2, the waste water produced by tofu production flows into the regulating pool 2 through the grid 1 that blocks the large particles and large-diameter impurities in the waste water, and step 3, the waste water is in the regulating pool 2 to perform pretreatment, pretreatment is to carry out impurity precipitation on the wastewater entering the regulating tank 2, which is conducive to the homogenization of wastewater and effectively reduces the initial concentration of organic pollution. Step 4, after the pretreatment is completed, the controller controls the first electromagnetic The valve 3 is opened, and the waste water enters the SBR pool 4 through the outlet of the regulating pool 2. Step 5, after the water level sensor in the SBR pool 4 senses that the waste water in the SBR pool 4 reaches the set water level, the controller controls the first solenoid valve 3 to close, At the same time, the controller controls the air pump 5 to open, and the wastewater in the SBR pool 4 is aerated. In step 6, after 2 hours of aeration, the controller controls the air pump 5 to stop running, and the wastewater in the SBR pool 4 enters the settling time. Step 7, after settling for 1 hour, the controller controls the second solenoid valve 9 to open, and starts to drain water. Step 8, after the drainage is completed, the controller controls the second solenoid valve 9 to close, and returns to step 2.
在SBR池4的尺寸设定为40cm×40cm×80cm的情形下,以一批次废水量(100L)为研究对象,在初始时刻对调节池2内混合废水进行取样(n=5)分析测定CODcr(化学需氧量),再对曝气工序的不同曝气时段(0.5h、1h、2h、3h、4h、5h)SBR池4内的废水取样n=5经沉淀1小时后进行分析测定CODcr,测定结果如表1所示,结果表明随着曝气时间的增加,经过沉淀后的CODcr呈逐渐减少的趋势,经过0.5小时的处理,去除率已经达到了近40%,到了2小时后,出水指标满足国家污水综合排放标准的三级标准,作为小型豆腐厂而言,该标准已经比目前的大多数直接排放入下水道改进了许多。When the size of the SBR pool 4 is set to 40cm×40cm×80cm, a batch of wastewater (100L) is taken as the research object, and the mixed wastewater in the regulating tank 2 is sampled (n=5) for analysis and measurement at the initial moment CODcr (Chemical Oxygen Demand), and then analyze and measure the waste water in the SBR pool 4 in different aeration periods (0.5h, 1h, 2h, 3h, 4h, 5h) of the aeration process n=5 after settling for 1 hour CODcr, the measurement results are shown in Table 1. The results show that with the increase of aeration time, the CODcr after precipitation is gradually decreasing. After 0.5 hours of treatment, the removal rate has reached nearly 40%. After 2 hours , The effluent index meets the third-level standard of the national comprehensive sewage discharge standard. As a small tofu factory, this standard has improved a lot compared to most of the current direct discharge into the sewer.
表1不同曝气时间豆腐生产废水的进出水COD指标(距水面5cm采样并沉淀1h)Table 1 COD index of influent and effluent water from tofu production wastewater at different aeration times (sampling at 5 cm from the water surface and sedimentation for 1 h)
在SBR池4的尺寸设定为40cm×40cm×80cm的情形下,以一批次废水量(100L)为研究对象,在初始时刻对调节池2内混合废水进行取样n=3分析测定SS(悬浮物浓度),再对曝气工序的不同曝气时段(0.5h、1h、2h、3h、4h、5h)出水口7的出水进行取样(n=3)分析测定SS,测定结果如表2所示,结果表明:随着曝气时间的增加,出水口的悬浮物浓度(SS)呈逐渐减少的趋势,经过0.5h的处理,去除率已经超过30%,1h后出水基本满足国家污水综合排放标准的三级标准,3h后出水肉眼可见基本澄清,且后续处理出水指标保持较低数值,处理效果稳定、趋缓。When the size of the SBR pool 4 is set to 40cm x 40cm x 80cm, a batch of wastewater (100L) is taken as the research object, and the mixed wastewater in the regulating pool 2 is sampled n=3 at the initial moment for analysis and determination of SS( concentration of suspended solids), and then sample (n=3) the effluent from the outlet 7 in different aeration periods (0.5h, 1h, 2h, 3h, 4h, 5h) of the aeration process to analyze and measure SS, and the measurement results are shown in Table 2 As shown, the results show that: with the increase of aeration time, the concentration of suspended solids (SS) at the outlet is gradually decreasing. After 0.5 hours of treatment, the removal rate has exceeded 30%. After 1 hour, the effluent basically meets the national sewage comprehensive The three-level standard of the discharge standard, after 3 hours, the effluent is basically clear to the naked eye, and the effluent index of the subsequent treatment remains low, and the treatment effect is stable and slows down.
表2不同曝气时间豆腐生产废水的进出水SS指标(出水口采样)Table 2 The SS index of the influent and effluent water of tofu production wastewater at different aeration times (outlet sampling)
所以本发明中曝气处理的时间选择为2小时。Therefore, the time of aeration treatment in the present invention is selected as 2 hours.
上面结合附图对本发明进行了示例性描述,显然本发明具体实现并不受上述方式的限制,只要采用了本发明的方法构思和技术方案进行的各种非实质性的改进,或未经改进将本发明的构思和技术方案直接应用于其它场合的,均在本发明的保护范围之内。The present invention has been exemplarily described above in conjunction with the accompanying drawings. Obviously, the specific implementation of the present invention is not limited by the above methods, as long as various insubstantial improvements are adopted in the method concept and technical solutions of the present invention, or there is no improvement Directly applying the concept and technical solutions of the present invention to other occasions is within the protection scope of the present invention.
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