CN203079808U - Sewage treatment system capable of realizing sewage zero emission during paper making - Google Patents
Sewage treatment system capable of realizing sewage zero emission during paper making Download PDFInfo
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- 239000010865 sewage Substances 0.000 title claims abstract description 48
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 75
- 238000003756 stirring Methods 0.000 claims abstract description 38
- 238000001914 filtration Methods 0.000 claims abstract description 25
- 230000003647 oxidation Effects 0.000 claims abstract description 25
- 238000007254 oxidation reaction Methods 0.000 claims abstract description 25
- 239000002699 waste material Substances 0.000 claims abstract description 22
- 238000006243 chemical reaction Methods 0.000 claims abstract description 15
- 238000004519 manufacturing process Methods 0.000 claims abstract description 9
- 238000004062 sedimentation Methods 0.000 claims description 53
- 239000010802 sludge Substances 0.000 claims description 19
- 239000002002 slurry Substances 0.000 claims description 18
- 238000001556 precipitation Methods 0.000 claims description 13
- 239000000945 filler Substances 0.000 claims description 7
- 239000007787 solid Substances 0.000 claims description 7
- 238000012856 packing Methods 0.000 claims description 6
- 230000003139 buffering effect Effects 0.000 claims 1
- 239000013530 defoamer Substances 0.000 claims 1
- 238000007599 discharging Methods 0.000 claims 1
- 239000002351 wastewater Substances 0.000 abstract description 32
- 238000005096 rolling process Methods 0.000 abstract description 6
- 239000002518 antifoaming agent Substances 0.000 abstract description 4
- 230000000694 effects Effects 0.000 abstract description 4
- 238000004065 wastewater treatment Methods 0.000 abstract description 4
- 239000006260 foam Substances 0.000 abstract description 2
- 238000012216 screening Methods 0.000 abstract 4
- 230000002401 inhibitory effect Effects 0.000 abstract 1
- 210000003437 trachea Anatomy 0.000 description 13
- 239000000126 substance Substances 0.000 description 6
- 235000013601 eggs Nutrition 0.000 description 4
- 239000005416 organic matter Substances 0.000 description 4
- 238000011084 recovery Methods 0.000 description 4
- 230000015556 catabolic process Effects 0.000 description 3
- 238000006731 degradation reaction Methods 0.000 description 3
- 239000007789 gas Substances 0.000 description 3
- 230000006872 improvement Effects 0.000 description 3
- 239000002245 particle Substances 0.000 description 3
- 238000001179 sorption measurement Methods 0.000 description 3
- 230000008901 benefit Effects 0.000 description 2
- 238000003912 environmental pollution Methods 0.000 description 2
- 239000000835 fiber Substances 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 238000005215 recombination Methods 0.000 description 2
- 230000006798 recombination Effects 0.000 description 2
- 230000003254 anti-foaming effect Effects 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000004042 decolorization Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000003344 environmental pollutant Substances 0.000 description 1
- 238000007667 floating Methods 0.000 description 1
- 238000005187 foaming Methods 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
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- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
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Abstract
Description
技术领域 technical field
本实用新型涉及一种废水处理系统,尤其是涉及一种造纸零排放污水处理系统。 The utility model relates to a wastewater treatment system, in particular to a papermaking zero-discharge sewage treatment system.
背景技术 Background technique
我国每年排放的污水量很大,经处理后排放的又不多,对环境造成很大破坏,我国各大水系都产生不同程度的污染,水环境严重恶化。长期以来,造纸废水一直是制约纸业快速发展的问题之一,造纸废水中污染物浓度高,成分较复杂,含有大量的造纸原料和化学药品,耗氧严重,致使造纸废水处理困难,成为严重污染环境的行业之一。如果造纸废水直接排出会严重污染环境,所以必须经过净化处理。 The amount of sewage discharged in our country is very large every year, and the amount discharged after treatment is not much, which has caused great damage to the environment. All major water systems in our country have produced varying degrees of pollution, and the water environment has seriously deteriorated. For a long time, papermaking wastewater has been one of the problems restricting the rapid development of the paper industry. The concentration of pollutants in papermaking wastewater is high, the composition is relatively complex, it contains a large amount of papermaking raw materials and chemicals, and the oxygen consumption is serious, which makes the treatment of papermaking wastewater difficult. One of the industries that pollute the environment. If the papermaking wastewater is directly discharged, it will seriously pollute the environment, so it must be purified.
现有造纸污水处理装置包括定距格栅机、废水收集池、斜网捞浆池、沉淀池、污泥回收池及回水池,定距格栅机的出口连接废水收集池的入口,废水收集池的出口连接斜网捞浆池,斜网捞浆池的出口连接沉淀池入口,所述沉淀池的排泥口连接污泥回收池的入口,所述沉淀池的出水口连接回水池,处理时,废水的大块悬浮或漂浮的污物经定距格栅机拦截后进入斜网捞浆池,斜网捞浆池内设有70目的斜网用以过滤水中的细小纤维、杂质,从斜网捞浆池内流出的废水进入沉淀池进行沉淀处理,经沉淀池处理后的废水流入回水池回用,沉淀池内的污泥则通过排泥口排入泥水回收池。这种处理物化处理系统,处理步骤简单,但是处理后的废水水质不好,只能去除废水中小部分的SS和COD,这种方式处理而得的回用水,易恶化发臭,且脱色效果不明显,不能有效降解水中致色物质,水中的有机物去除率低,处理后的废水泡沫现象严重,出水色度深,不能长期循环回用,污水中的COD常常超标排放,对水质污染造成影响。 The existing papermaking sewage treatment device includes a fixed-distance grid machine, a waste water collection tank, an inclined net slurry tank, a sedimentation tank, a sludge recovery tank and a return pool. The outlet of the fixed-distance grid machine is connected to the entrance of the waste water collection tank, and the waste water The outlet of the pool is connected to the inclined net slurry tank, the outlet of the inclined net slurry tank is connected to the entrance of the sedimentation tank, the sludge discharge port of the sedimentation tank is connected to the inlet of the sludge recovery tank, and the outlet of the sedimentation tank is connected to the backwater tank. When the large pieces of suspended or floating dirt in the wastewater are intercepted by the fixed-distance grid machine, they enter the inclined net slurry tank. There is a 70-mesh inclined net in the inclined net slurry tank to filter fine fibers and impurities in the water. The wastewater flowing out of the net fishing slurry tank enters the sedimentation tank for sedimentation treatment, the wastewater treated by the sedimentation tank flows into the backwater tank for reuse, and the sludge in the sedimentation tank is discharged into the mud water recovery tank through the sludge discharge port. This kind of treatment physical and chemical treatment system has simple treatment steps, but the quality of the treated wastewater is not good, and only a small part of SS and COD in the wastewater can be removed. The reused water obtained in this way is easy to deteriorate and smell, and the decolorization effect is not good. Obviously, it cannot effectively degrade the color-causing substances in the water, the removal rate of organic matter in the water is low, the foaming phenomenon of the treated wastewater is serious, the effluent color is deep, and it cannot be recycled for a long time. The COD in the sewage is often discharged beyond the standard, which has an impact on water quality pollution.
实用新型内容 Utility model content
因此,针对上述的问题,本实用新型提供一种废水处理效果好,可全部回收于生产,实现对外零排放,减少污染,节约生产成本的造纸零排放污水处理系统。 Therefore, in view of the above problems, the utility model provides a papermaking zero-discharge sewage treatment system with good wastewater treatment effect, which can be completely recycled in production, realizes zero discharge to the outside, reduces pollution, and saves production costs.
为达到上述目的,本实用新型是通过以下技术方案实现的:一种造纸零排放污水处理系统,包括集水池、过滤滚筛机、废浆收集池、搅拌反应塔、一级沉淀池、二级沉淀过滤塔及回水池,所述集水池的出口通过水泵连接过滤滚筛机,所述过滤滚筛机的出水口连接搅拌反应塔的进水口,所述过滤滚筛机的废浆出口连接废浆收集池的废浆进口,所述搅拌反应塔的出水口连接一级沉淀池,所述一级沉淀池的出水口连接二级沉淀过滤塔的进水口,所述二级沉淀过滤塔的出水口通过水管连接回水池,所述二级沉淀过滤塔与回水池之间的水管内部设有抑泡消泡剂,所述一级沉淀池与二级沉淀过滤塔之间还设有生物接触氧化池,所述生物接触氧化池内下部铺设有气管,所述气管上均布有出气孔,所述气管的一端伸出池外与风机相连,所述生物接触氧化池内位于气管的出气口上部设有活性污泥填料。 In order to achieve the above purpose, the utility model is realized through the following technical solutions: a zero-discharge sewage treatment system for papermaking, including a sump, a filter rolling screen machine, a waste slurry collection tank, a stirring reaction tower, a primary sedimentation tank, a secondary The sedimentation filter tower and the return pool, the outlet of the sump is connected to the filter roller sieve machine through the water pump, the water outlet of the filter roller sieve machine is connected to the water inlet of the stirring reaction tower, and the waste slurry outlet of the filter roller sieve machine is connected to the waste The waste slurry inlet of the slurry collection tank, the outlet of the stirring reaction tower is connected to the primary sedimentation tank, the water outlet of the primary sedimentation tank is connected to the water inlet of the secondary sedimentation filter tower, and the outlet of the secondary sedimentation filter tower The water outlet is connected to the return pool through a water pipe. The water pipe between the secondary sedimentation filter tower and the return pool is provided with an anti-foaming and defoaming agent. The lower part of the biological contact oxidation tank is laid with a trachea, and the air outlet is evenly distributed on the said trachea. Activated sludge filler.
进一步改进的是:所述二级沉淀过滤塔包括塔体、设于塔体上的塔盖、进污水管,所述塔体上部设有出水口,所述塔体下部设有集污斗,所述集污斗下部设有排泥口,所述塔体内由下自上依次设有让固体颗粒快速沉淀的快速沉淀装置及填料过滤层,所述塔体内位于快速沉淀装置下部设有缓冲槽,所述进污水管的出水端依次穿过塔盖、过滤填料层及快速沉淀装置与塔体内的缓冲槽相连,所述进污水管的进水口连接生物接触氧化池的出水口。 It is further improved that: the secondary sedimentation and filtration tower includes a tower body, a tower cover arranged on the tower body, and a sewage inlet pipe, the upper part of the tower body is provided with a water outlet, and the lower part of the tower body is provided with a sewage bucket, The lower part of the dirt collecting hopper is provided with a mud discharge port, and the tower body is sequentially provided with a rapid sedimentation device and a packing filter layer for rapid sedimentation of solid particles from bottom to top, and a buffer tank is arranged at the lower part of the tower body , the water outlet end of the sewage inlet pipe passes through the tower cover, the filter packing layer and the rapid sedimentation device in turn to be connected with the buffer tank in the tower body, and the water inlet of the sewage inlet pipe is connected to the water outlet of the biological contact oxidation tank.
进一步改进的是:所述快速沉淀装置包括设置在沉淀过滤塔体内侧的外圆柱筒体及设于外圆柱筒体内侧的中部设有供进污水管插入穿孔的内圆柱筒体,所述外圆柱筒体与内圆筒体之间沿径向方向斜置均布有复数个缓冲沉淀斜板。 A further improvement is: the rapid sedimentation device includes an outer cylindrical body arranged on the inside of the sedimentation and filtration tower body and an inner cylindrical body arranged in the middle of the inner side of the outer cylindrical body for inserting and perforating the sewage pipe. Between the cylinder body and the inner cylinder body, a plurality of buffer sedimentation slant plates are evenly arranged obliquely along the radial direction.
进一步改进的是:所述搅拌反应塔包括搅拌塔及设于搅拌塔内的搅拌装置,所述搅拌装置包括搅拌轴及均布于搅拌轴圆周外侧的搅拌叶片,所述各搅拌叶片的下部还分别设有拨动杆。 A further improvement is: the stirring reaction tower includes a stirring tower and a stirring device arranged in the stirring tower, the stirring device includes a stirring shaft and stirring blades uniformly distributed on the outside of the stirring shaft circumference, and the lower part of each stirring blade is also There are toggle levers respectively.
进一步改进的是:所述一级沉淀池的底部设有排污口,所述排污口上设有排污阀。 A further improvement is: the bottom of the primary sedimentation tank is provided with a sewage outlet, and a sewage valve is provided on the sewage outlet.
通过采用前述技术方案,本实用新型的有益效果是:利用本造纸零排放污水处理系统处理后的回水水质好,使得造纸废水经处理后可重复循环利用,全部回用于生产,基本实现对外零排放,不仅不会排放污水污染环境而且可节约大量生产成本,降低了资源浪费,可有效地对造纸废水进行回收利用,对环境的污染降到最低,并且本处理装置还能从污水中提取废浆,该废浆可用于生产运输蛋用的蛋托,从而实现废物重组利用的效益。所述一级沉淀池与二级沉淀过滤塔之间还设有生物接触氧化池,生物接触氧化池内下部铺设有气管,所述气管上均布有出气孔,所述气管的一端伸出池外与风机相连,所述生物接触氧化池内位于气管的出气口上部设有活性污泥填料,由此风机可通过气管向生物接触氧化池内输送气体,使生物接触氧化池内的废水不断运动,使废水与池内的活性污泥互相触碰,使活性污泥与废水充分接触反应,增加活性污泥与污水之间的接触吸附机会,有效提高降解能力,可有效降解水中致色物质、去除水中悬浮物,提高污水有机物的去除率,使废水中的COD可达标排放。 By adopting the above-mentioned technical scheme, the beneficial effect of the utility model is: the return water treated by the papermaking zero-discharge sewage treatment system is of good quality, so that the papermaking wastewater can be reused after treatment, and all of it can be reused in production, basically realizing external Zero discharge, not only will not discharge sewage to pollute the environment, but also can save a lot of production costs, reduce waste of resources, can effectively recycle papermaking wastewater, minimize environmental pollution, and this treatment device can also extract waste water from sewage Waste pulp, which can be used to produce egg trays for transporting eggs, so as to realize the benefits of waste recombination and utilization. There is also a biological contact oxidation tank between the first-level sedimentation tank and the second-level sedimentation and filtration tower, and a trachea is laid on the lower part of the biological contact oxidation tank. It is connected with the fan, and the activated sludge filler is arranged on the upper part of the air outlet of the trachea in the biological contact oxidation tank, so that the fan can deliver gas to the biological contact oxidation tank through the trachea, so that the wastewater in the biological contact oxidation tank moves continuously, so that the wastewater and The activated sludge in the pool touches each other, so that the activated sludge and wastewater can fully contact and react, increase the contact and adsorption opportunities between activated sludge and sewage, effectively improve the degradation ability, and can effectively degrade color-causing substances in water and remove suspended solids in water. Improve the removal rate of organic matter in sewage, so that COD in wastewater can reach the standard discharge. the
附图说明 Description of drawings
图1是本实用新型实施例的流程示意图。 Fig. 1 is a schematic flow chart of the utility model embodiment.
图2是本实用新型实施 例二级沉淀过滤塔的结构示意图。 Fig. 2 is the structural representation of the secondary sedimentation filter tower of the utility model embodiment.
图3是本实用新型实施例生物接触氧化池的结构示意图。 Fig. 3 is a schematic structural view of the biological contact oxidation tank of the embodiment of the present invention.
具体实施方式 Detailed ways
下面结合附图对本实用新型作进一步说明: The utility model will be further described below in conjunction with the accompanying drawings:
实施例: Example:
参考图1与图3,本实施例公开一种造纸零排放污水处理系统,包括集水池1、过滤滚筛机2、废浆收集池3、搅拌反应塔4、一级沉淀池5、二级沉淀过滤塔6及回水池7,所述集水池1的出口通过水泵11连接过滤滚筛机2进水口,所述过滤滚筛机2的出水口连接搅拌反应塔4的进水口,所述过滤滚筛机2的废浆出口连接废浆收集池3的废浆进口,所述搅拌反应塔4的出水口连接一级沉淀池5的进水口,所述一级沉淀池5的出水口连接二级沉淀过滤塔6的进水口,所述一级沉淀池5的底部设有排污口,所述排污口上设有排污阀52,所述二级沉淀过滤塔6的出水口通过水管9连接回水池7,所述二级沉淀过滤塔6与回水池7之间的水管9内部设有抑泡消泡剂8。所述一级沉淀池5与二级沉淀过滤塔6之间还设有生物接触氧化池10,所述生物接触氧化池10内下部铺设有气管101,所述气管101上均布有出气孔,所述气管101的一端伸出池外与风机102相连,所述生物接触氧化池10内位于气管101的出气口上部设有活性污泥填料103,风机可通过气管向生物接触氧化池内输送气体,使生物接触氧化池内的废水不断运动,使废水与池内的活性污泥互相触碰,使活性污泥与废水充分接触反应,增加活性污泥与污水之间的接触吸附机会,有效提高降解能力,可有效降解水中致色物质、去除水中悬浮物,提高污水有机物的去除率,使废水中的COD可达标排放。
Referring to Figure 1 and Figure 3, this embodiment discloses a papermaking zero-discharge sewage treatment system, including a water collection tank 1, a filter roller sieve machine 2, a waste slurry collection tank 3, a stirring reaction tower 4, a primary sedimentation tank 5, a secondary Precipitation and filtration tower 6 and backwater pool 7, the outlet of described sump 1 is connected to the water inlet of filter roller sieve machine 2 through
参考图2,所述二级沉淀过滤塔包括塔体61、设于塔体61上的塔盖62、进污水管63,所述塔体61上部设有出水口611,所述塔体61下部设有集污斗64,所述集污斗64下部设有排泥口,所述塔体61内由下自上依次设有让固体颗粒快速沉淀的快速沉淀装置65及填料过滤层66,所述塔体61内位于快速沉淀装置65下部设有缓冲槽67,所述进污水管63的出水端依次穿过塔盖62、过滤填料层66及快速沉淀装置65与塔体61内的缓冲槽67相连,所述进污水管63的进水口生物接触氧化池10的出水口,所述快速沉淀装置65包括设置在塔体61内侧的外圆柱筒体651及设于外圆柱筒体651内侧的中部设有供进污水管插入穿孔的内圆柱筒体652,所述外圆柱筒体652与内圆筒体651之间沿径向方向斜置均布有缓冲沉淀斜板653。废水经生物接触氧化池10处理后从进污水管进入沉淀塔体内后经缓冲槽缓冲后向四周扩散,然后平稳的向塔顶流动,污水在上升过程中,密度大于水的固体悬浮物如造填料、细小纤维、泥纱等无机颗粒不断的下沉并通过快速沉淀装置,加速沉淀,缓冲沉淀装置的每两块缓冲沉淀斜板相当于一个很小的沉淀池,使颗粒沉淀时间大为缩短,利用竖流原理,达到快速沉淀的目的,从缓冲沉淀装置流过的污水经过滤填料层进一步过滤后从塔体上部的出水口流入回收池。
With reference to Fig. 2, described secondary sedimentation filter tower comprises
所述搅拌反应塔4包括搅拌塔及设于搅拌塔内的搅拌装置,所述搅拌装置包括搅拌轴及均布于搅拌轴圆周外侧的搅拌叶片,所述各搅拌叶片的下部还分别设有拨动杆,拨动杆可拓宽搅拌装置的搅拌范围,使得搅拌效果更好,更均匀。 The stirring reaction tower 4 comprises a stirring tower and a stirring device located in the stirring tower, the stirring device comprises a stirring shaft and stirring blades uniformly distributed on the outside of the stirring shaft circumference, and the bottom of each stirring blade is respectively provided with a dial The moving rod can broaden the stirring range of the stirring device, making the stirring effect better and more uniform.
利用本造纸零排放污水处理系统处理后的回水水质好,使得造纸废水经处理后可重复循环利用,全部回用于生产,基本实现对外零排放,不仅不会排放污水污染环境而且可节约大量生产成本,降低了资源浪费,可有效地对造纸废水进行回收利用,对环境的污染降到最低,并且本处理装置还能从污水中提取废浆,该废浆可用于生产运输蛋用的蛋托,从而实现废物重组利用的效益。所述一级沉淀池与二级沉淀过滤塔之间还设有生物接触氧化池,生物接触氧化池内下部铺设有气管,所述气管上均布有出气孔,所述气管的一端伸出池外与风机相连,所述生物接触氧化池内位于气管的出气口上部设有活性污泥填料,由此风机可通过气管向生物接触氧化池内输送气体,使生物接触氧化池内的废水不断运动,使废水与池内的活性污泥互相触碰,使活性污泥与废水充分接触反应,增加活性污泥与污水之间的接触吸附机会,有效提高降解能力,可有效降解水中致色物质、去除水中悬浮物,提高污水有机物的去除率,使废水中的COD可达标排放。 The return water treated by this papermaking zero-discharge sewage treatment system is of good quality, so that the papermaking wastewater can be reused after treatment, and all of it can be reused in production, basically realizing zero discharge to the outside world, not only will not discharge sewage to pollute the environment, but also can save a lot The production cost reduces the waste of resources, and can effectively recycle papermaking wastewater to minimize environmental pollution, and the treatment device can also extract waste pulp from sewage, which can be used to produce eggs for transporting eggs. To realize the benefit of waste recombination and utilization. There is also a biological contact oxidation tank between the first-level sedimentation tank and the second-level sedimentation and filtration tower, and a trachea is laid on the lower part of the biological contact oxidation tank. It is connected with the fan, and the activated sludge filler is arranged on the upper part of the air outlet of the trachea in the biological contact oxidation tank, so that the fan can deliver gas to the biological contact oxidation tank through the trachea, so that the wastewater in the biological contact oxidation tank moves continuously, so that the wastewater and The activated sludge in the pool touches each other, so that the activated sludge and wastewater can fully contact and react, increase the contact and adsorption opportunities between activated sludge and sewage, effectively improve the degradation ability, and can effectively degrade color-causing substances in water and remove suspended solids in water. Improve the removal rate of organic matter in sewage, so that COD in wastewater can reach the standard discharge.
以上所记载,仅为利用本创作技术内容的实施例,任何熟悉本项技艺者运用本创作所做的修饰、变化,皆属本创作主张的专利范围,而不限于实施例所揭示者。 The above records are only examples of using the technical content of this creation. Any modifications and changes made by those who are familiar with this technology using this creation belong to the scope of patents claimed by this creation, and are not limited to those disclosed in the examples.
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| CN105862683A (en) * | 2016-04-22 | 2016-08-17 | 广东省水利水电科学研究院 | Multi-layer and multi-order pore plate used for reducing aeration and restraining bubbles and rapid construction method for multi-layer and multi-order pore plate |
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