CN200992514Y - Waste water treating and concurrently classified collecting device for chemical laboratory - Google Patents
Waste water treating and concurrently classified collecting device for chemical laboratory Download PDFInfo
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- CN200992514Y CN200992514Y CN 200620141862 CN200620141862U CN200992514Y CN 200992514 Y CN200992514 Y CN 200992514Y CN 200620141862 CN200620141862 CN 200620141862 CN 200620141862 U CN200620141862 U CN 200620141862U CN 200992514 Y CN200992514 Y CN 200992514Y
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- 239000000126 substance Substances 0.000 title claims abstract description 23
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 34
- 238000006243 chemical reaction Methods 0.000 claims abstract description 20
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- 239000004576 sand Substances 0.000 claims abstract description 18
- 238000004065 wastewater treatment Methods 0.000 claims abstract description 14
- 239000010865 sewage Substances 0.000 claims abstract description 10
- 239000002699 waste material Substances 0.000 claims description 20
- 239000003513 alkali Substances 0.000 claims description 9
- 229910001385 heavy metal Inorganic materials 0.000 claims description 9
- 239000002253 acid Substances 0.000 claims description 8
- 239000010815 organic waste Substances 0.000 claims description 8
- 239000010805 inorganic waste Substances 0.000 claims description 5
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- 239000003795 chemical substances by application Substances 0.000 description 3
- 239000000706 filtrate Substances 0.000 description 3
- 238000001914 filtration Methods 0.000 description 3
- 239000005416 organic matter Substances 0.000 description 3
- 239000010802 sludge Substances 0.000 description 3
- 239000006228 supernatant Substances 0.000 description 3
- UCKMPCXJQFINFW-UHFFFAOYSA-N Sulphide Chemical compound [S-2] UCKMPCXJQFINFW-UHFFFAOYSA-N 0.000 description 2
- 238000004140 cleaning Methods 0.000 description 2
- 239000000701 coagulant Substances 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-M hydroxide Chemical compound [OH-] XLYOFNOQVPJJNP-UHFFFAOYSA-M 0.000 description 2
- 239000007800 oxidant agent Substances 0.000 description 2
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- AXCZMVOFGPJBDE-UHFFFAOYSA-L calcium dihydroxide Chemical compound [OH-].[OH-].[Ca+2] AXCZMVOFGPJBDE-UHFFFAOYSA-L 0.000 description 1
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Abstract
本实用新型涉及一种化学实验室废水处理兼分类收集装置,由由废水分类收集罐、废水调节池、高位反应槽和沉降池构成,其中废水分类收集罐包括由六个废水分类收集罐构成,分别利用带控制阀的管道和调节池相连;调节池再通过带控制阀和污水提升泵的管道和高位反应槽相连,高位反应槽的出水管和沉降池相连,沉降池的溢流管和砂滤器相连,砂滤器顶部连接带控制阀的净水排放管。该装置具有能够在化学实验室对废水进行集中分类收集,具有提高处理效果、可以反冲洗废水、不需要投入大量的新鲜药剂并达到有效处理的优点。且结构简单、使用方便、生产成本低,充分体现“以污治污”的思想,在化学实验室废水处理方面得到广泛推广和应用。
The utility model relates to a chemical laboratory wastewater treatment and classification collection device, which is composed of a wastewater classification collection tank, a wastewater adjustment tank, a high-level reaction tank and a settling tank, wherein the wastewater classification collection tank is composed of six waste water classification collection tanks, The pipelines with control valves are respectively connected to the regulating tank; the regulating tank is connected to the high-level reaction tank through a pipeline with a control valve and a sewage lifting pump, the outlet pipe of the high-level reaction tank is connected to the settling tank, and the overflow pipe of the settling tank is connected to the sand The filter is connected, and the top of the sand filter is connected with a clean water discharge pipe with a control valve. The device has the advantages of being able to centrally classify and collect waste water in a chemical laboratory, improve the treatment effect, backwash waste water, and achieve effective treatment without the need to invest a large amount of fresh chemicals. The utility model has the advantages of simple structure, convenient use and low production cost, which fully embodies the idea of "controlling pollution with pollution", and has been widely promoted and applied in chemical laboratory wastewater treatment.
Description
技术领域technical field
本实用新型涉及一种废水处理兼分类收集装置,尤其涉及一种化学实验废水处理兼分类收集装置。The utility model relates to a wastewater treatment and classification collection device, in particular to a chemical experiment wastewater treatment and classification collection device.
背景技术Background technique
当前我国很多学校、科研院所的化学实验室每天产生的废水、废液未严格处理并排入城市生活污水管网或河流,对城市污水厂产生很大的负荷冲击,特别是重金属和难降解有机物的排放会严重污染环境,威胁人们的健康。化学实验室废水排放特点是:间断性、量相对较少、水质成分复杂多变、高危害性。目前在工业中使用的废水处理方法、工艺、设备具有水力负荷大、废水成分相对简单、连续运行、设备费及运转费高等特点,不适合化学实验室废水的处理。At present, the waste water and waste liquid produced by the chemical laboratories of many schools and scientific research institutes in our country are not strictly treated and discharged into the urban domestic sewage pipe network or rivers, which has a great load impact on urban sewage plants, especially heavy metals and refractory The discharge of organic matter will seriously pollute the environment and threaten people's health. The characteristics of chemical laboratory wastewater discharge are: intermittent, relatively small amount, complex and changeable water quality components, and high hazard. The wastewater treatment methods, processes and equipment currently used in industry have the characteristics of large hydraulic load, relatively simple wastewater components, continuous operation, high equipment costs and high operating costs, and are not suitable for the treatment of chemical laboratory wastewater.
目前也有针对实验室废水获得专利授权的废水处理装置,如ZL02211281.2主要由集液池、污水泵、吸附过滤槽、净水池等构件连接而成;ZL200420018566.9主要由搅拌釜、泵、悬浮物过滤器、有机物过滤器等构件连接而成。这些装置处理效果都不佳,其不足之处如下:1、这些装置是通过同一工艺流程把所有的实验废水合并或简单分成两大类综合处理,但实验室废水水质的复杂性会大大降低最终处理效果;2、根据实验室废水的产生及排放特征,其废水的收集工作是无法回避的,而只有集中分类收集才可以有效处理,而这些装置没有充分考虑这些因素;3、这些装置在过滤过程中产生的滤渣非常多,滤渣的清理量或反冲洗水量很大,没有考虑反冲洗废水的处理;4、这些装置没有体现“以污治污”的思想,需要投入大量的新鲜药剂。At present, there are also wastewater treatment devices that have obtained patent authorization for laboratory wastewater. For example, ZL02211281.2 is mainly composed of liquid collection tanks, sewage pumps, adsorption filter tanks, and water purification tanks; ZL200420018566.9 is mainly composed of stirring tanks, pumps, Suspended matter filter, organic matter filter and other components are connected. The treatment effects of these devices are not good, and their shortcomings are as follows: 1. These devices combine or simply divide all experimental wastewater into two categories for comprehensive treatment through the same process, but the complexity of laboratory wastewater quality will be greatly reduced. Treatment effect; 2. According to the generation and discharge characteristics of laboratory wastewater, the collection of wastewater cannot be avoided, and only centralized and classified collection can be effectively treated, and these devices do not fully consider these factors; 3. These devices are filtering There are a lot of filter residues produced in the process, and the cleaning amount of filter residues or the amount of backwash water is very large, and the treatment of backwash wastewater is not considered; 4. These devices do not reflect the idea of "using pollution to control pollution" and require a large amount of fresh chemicals.
发明内容Contents of the invention
本实用新型其目的就在于克服以上缺陷而提供一种能够在化学实验室对废水进行集中分类收集、提高处理效果、可以反冲洗废水、不需要投入大量的新鲜药剂并能进行有效处理的装置。The purpose of this utility model is to overcome the above defects and provide a device that can collect and classify waste water in a chemical laboratory, improve the treatment effect, backwash waste water, and can effectively treat the waste water without inputting a large amount of fresh chemicals.
实现上述目的而采取的技术方案包括:由废水分类收集罐、废水调节池、高位反应槽和沉降池构成,其中废水分类收集罐包括由六个废水分类收集罐构成,分别为废酸罐、重金属离子废水罐、废碱罐,有机废水罐、其它无机废水罐、备用罐;每个收集罐都为正三棱柱,且集中拼合在一起整体构成正六棱柱。每个收集罐设有废水收集导管,导管进口设在正三棱柱顶部,导管出口设在正三棱柱中下部。导管进口分别为:废酸罐导管口、重金属离子废水罐导管口、废碱罐导管口,有机废水罐导管口、其它无机废水罐导管口、备用罐导管口。The technical scheme adopted to achieve the above purpose includes: it is composed of a waste water classification collection tank, a waste water regulating tank, a high-level reaction tank and a settling tank. Ion waste water tank, waste alkali tank, organic waste water tank, other inorganic waste water tank, spare tank; each collection tank is a regular triangular prism, and they are put together together to form a regular hexagonal prism. Each collecting tank is provided with a waste water collecting conduit, the conduit inlet is arranged at the top of the regular triangular prism, and the conduit outlet is arranged at the middle and lower part of the regular triangular prism. The conduit inlets are respectively: the conduit port of the waste acid tank, the conduit port of the heavy metal ion wastewater tank, the conduit port of the waste alkali tank, the conduit port of the organic wastewater tank, the conduit port of other inorganic wastewater tanks, and the backup tank conduit port.
每个收集罐底部通过带有控制阀的管道和调节池相连。调节池底面为水平夹角15°的倾斜面,调节池底部设置在地槽中,污水提升泵进口管设置在调节池右下角,其出口管连接控制阀,再和高位反应槽连接。高位反应槽中装有搅拌器,其顶部设有投药口,高位反应槽左下端出水管连接控制阀,再和沉降池的中心管相连,中心管出口为喇叭形,并在出口处设置一档板。沉降池上部设有一层水平倾角为60°斜板,沉降池下半部为倒圆锥体,沉降池底部连接排泥管。The bottom of each collection tank is connected to the regulating tank through a pipeline with a control valve. The bottom surface of the adjustment tank is an inclined surface with a horizontal angle of 15°. The bottom of the adjustment tank is set in the ground tank. The inlet pipe of the sewage lifting pump is set at the lower right corner of the adjustment tank. The outlet pipe is connected to the control valve and then connected to the high-level reaction tank. The high-level reaction tank is equipped with an agitator, and its top is equipped with a drug injection port. The outlet pipe at the lower left end of the high-level reaction tank is connected to the control valve, and then connected to the center pipe of the sedimentation tank. The outlet of the center pipe is trumpet-shaped, and a gear is set at the outlet. plate. The upper part of the settling tank is equipped with a layer of sloping plate with a horizontal inclination angle of 60°, the lower part of the settling tank is an inverted cone, and the bottom of the settling tank is connected to the mud discharge pipe.
沉降池右上端连有带控制阀的溢流管,溢流管下端和砂滤器底部进水管相连,砂滤器顶部连接带控制阀的净水排放管。另外,砂滤器顶部还连接带控制阀的反冲洗进水管,底部连接带控制阀的反冲洗出水管。The upper right end of the settling tank is connected with an overflow pipe with a control valve, the lower end of the overflow pipe is connected with the water inlet pipe at the bottom of the sand filter, and the top of the sand filter is connected with a clean water discharge pipe with a control valve. In addition, the top of the sand filter is also connected with a backwash water inlet pipe with a control valve, and the bottom is connected with a backwash water outlet pipe with a control valve.
与现有技术相比本实用新型的优点在于,Compared with the prior art, the utility model has the advantages that,
1、该装置是通过不同的工艺流程把所有的实验室废水进行综合分类处理,使得实验室废水水质的复杂性会大大提高最终处理效果;1. The device comprehensively classifies and treats all laboratory wastewater through different technological processes, so that the complexity of laboratory wastewater quality will greatly improve the final treatment effect;
2、根据实验室废水的产生及排放特征,其废水的收集工作是无法回避的,恰当的集中分类收集形成最佳处理。2. According to the generation and discharge characteristics of laboratory wastewater, the collection of wastewater is unavoidable, and appropriate centralized and classified collection forms the best treatment.
3、本装置在过滤过程中产生的滤渣非常少,滤渣的清理量或反冲洗水量很小,充分合理的对反冲洗废水进行处理。3. This device produces very little filter residue during the filtration process, and the cleaning amount of filter residue or the amount of backwash water is very small, and the backwash wastewater is fully and reasonably treated.
4、充分体现“以污治污”的思想,不需要投入大量的新鲜药剂;4. Fully embodies the idea of "pollution control with pollution", and does not need to invest a lot of fresh chemicals;
附图说明Description of drawings
图1为本实用新型结构示意图。Fig. 1 is the structural representation of the utility model.
图2为废水分类收集罐顶部俯视图。Figure 2 is a top plan view of the waste water classification collection tank.
图3为废水分类收集罐底部仰视图。Figure 3 is a bottom view of the wastewater classification collection tank.
具体实施方式Detailed ways
如图1、图2和图3所示,本实例,其结构由废水分类收集罐16、调节池1、高位反应槽6和沉降池10构成,其中废水分类收集罐由6个废水分类收集罐A、B、C、D、E、F构成,分别为:废酸罐A、重金属离子废水罐B、废碱罐C,有机废水罐D、其它无机废水罐E、备用罐F;每个收集罐为形状一样的正三棱柱,且集中拼合在一起整体构成正六棱柱。每个收集罐设有废水收集导管,从顶部开口进入,且导管口分别为:废酸罐导管口a、重金属离子废水罐导管口b、废碱罐导管口c,有机废水罐导管口d、其它无机废水罐导管口e、备用罐导管口f,可把不同性质的废水分别从不同的导管口导入相应收集罐。每个收集罐底部都带有控制阀的管道和调节池1相连,打开相应控制阀,废水可单独也可合并进入低位调节池1。这样既可以单独处理每种废水,也可根据各废水组成情况合并处理;另外,通过废酸罐A和废碱罐B可以调节调节池1中废水的PH值,使之达到最佳范围,这样不仅可单独提高处理效果,也不缺乏处理方式的灵活性,还可以达到“以污治污”的目的。As shown in Figure 1, Figure 2 and Figure 3, in this example, its structure is composed of waste water classification collection tank 16, regulating tank 1, high-
调节池1底面为水平夹角15°的倾斜面,调节池1底部设置在地槽中,调节池1右下角连有排水管。调节完毕后通过污水提升泵2把废水提升到高位反应槽6,启动高位反应槽6中的搅拌器4,并从投药口5投入相应的氧化剂、还原剂、絮凝剂或助凝剂等药剂,在高位反应槽6中发生化学反应生成氢氧化物、硫化物、絮胶状沉淀物等。反应完成后,废水经过带控制阀出水管3进入中心管7,中心管7中废水缓缓进入沉降池10。为增强沉降效果,要求大直径沉降池,沉降池10上部设一层水平倾角为60°斜板9,下半部设为倒圆锥体,污泥在此沉积,另外沉降池10还具有暂时储存污泥的功能。定期沉降池10打开其底部排泥管15排泥,让污泥进入固体废物处理系统。The bottom surface of the adjustment pool 1 is an inclined surface with a horizontal angle of 15°, the bottom of the adjustment pool 1 is arranged in the ground trough, and the lower right corner of the adjustment pool 1 is connected with a drain pipe. After the adjustment is completed, the waste water is lifted to the high-
沉降池10上层沉清液从溢流管8流出,从砂滤器13底部进水管进入砂滤器13,废水在砂滤器13中从下向上缓慢流动,滤液从净水排放管12直接排放。由于整个过程属于间歇式操作,沉降和过滤速度非常缓慢,处理效果非常好,其能耗较低,非常适合化学实验室废水处理。The supernatant liquid in the upper layer of the
对砂滤器13要进行定期反冲洗,反冲洗水从带控制阀的反冲洗进水管11进入砂滤器13,废水从上向下流动,反冲洗废水从砂滤器13底部进入带控制阀的反冲洗出水管14进入调节池1。由于过滤前面是沉降池10,反冲洗周期比较长;另外,反冲洗水进入调节池1,其滤渣再通过沉降被除去。整个工艺过程非常环保。The
其中在反冲洗阶段,反冲洗进水管11和反冲洗出水管14上的控制阀为打开状态;溢流管8和净水排放管12上的控制阀上为关闭状态。当在非反冲洗阶段,反冲洗进水管11和反冲洗出水管14上的控制阀为关闭状态;溢流管8和净水排放管12上的控制阀上为打开状态。Wherein in the backwashing stage, the control valves on the backwashing
具体实施过程如下:实验室可根据每次产生的废水类型,把废水暂存在相对应的收集罐中,等收集到一定量则启动后面的装置进行集中处理。The specific implementation process is as follows: the laboratory can temporarily store the wastewater in the corresponding collection tank according to the type of wastewater generated each time, and when a certain amount is collected, the subsequent devices will be activated for centralized treatment.
如果要处理含重金属离子废水,打开重金属离子废水罐B底部控制阀,让废水进入低位调节池1,再根据废水中重金属离子化学性质,可缓慢打开废酸罐A或废碱罐C底部控制阀,使调节池1中溶液的酸碱度达到最佳范围,可根据需要利用其它收集罐中的废液作为调节剂。再启动污水提升泵2,把调节池1中废水送入高位反应槽6中,启动搅拌器4,从投药口5投入必要的絮凝剂、助凝剂或其它药剂,在高位反应槽5中发生化学反应生成氢氧化物、硫化物、絮胶状物等,反应到一定时间打开出水管3上的控制阀,废水流入中心管7,中心管7中废水缓缓进入沉降池10,沉积物在沉降池10底部沉积。上层沉清液从溢流管8进入砂滤器13,滤液从砂滤器13顶部出来经净水排放管12直接排放。If wastewater containing heavy metal ions is to be treated, open the bottom control valve of heavy metal ion wastewater tank B to allow the wastewater to enter the low-level regulating tank 1, and then slowly open the bottom control valve of waste acid tank A or waste alkali tank C according to the chemical properties of heavy metal ions in the wastewater , so that the pH of the solution in the regulating tank 1 reaches the optimum range, and the waste liquid in other collection tanks can be used as a regulating agent as required. Then start the
如果要处理有机废水,打开有机废水罐D底部控制阀,让有机废水进入低位调节池1,再根据废水中有机物化学性质,缓慢打开废酸罐A或废碱罐C底部控制阀,使调节池1中溶液的酸碱度达到最佳范围,可根据需要利用其它收集罐中的废液作为调节剂。再启动污水提升泵2,把调节池1中废水送入高位反应槽6中,启动搅拌器4,从投药口5投入氧化剂、石灰水、絮凝剂等,发生氧化还原反应进行分解和中和反应,生成沉淀,反应到一定时间打开出水管3上的控制阀,废水流入中心管7,中心管7中废水缓缓进入沉降池10,沉积物在沉降池10底部沉积。上层沉清液从溢流管8流出进入砂滤器13,滤液从砂滤器13顶部流出经净水排放管12直接排放。If organic waste water is to be treated, open the control valve at the bottom of organic waste water tank D to allow the organic waste water to enter the low-level regulating tank 1, and then slowly open the control valve at the bottom of waste acid tank A or waste alkali tank C according to the chemical properties of the organic matter in the waste water to make the regulating tank The pH of the solution in 1 reaches the optimal range, and the waste liquid in other collection tanks can be used as a regulator according to needs. Start the
Claims (7)
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| Application Number | Priority Date | Filing Date | Title |
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| CN 200620141862 CN200992514Y (en) | 2006-12-31 | 2006-12-31 | Waste water treating and concurrently classified collecting device for chemical laboratory |
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| Application Number | Priority Date | Filing Date | Title |
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| CN 200620141862 CN200992514Y (en) | 2006-12-31 | 2006-12-31 | Waste water treating and concurrently classified collecting device for chemical laboratory |
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Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101659504B (en) * | 2009-09-09 | 2011-08-03 | 周瑞兴 | A laboratory wastewater treatment method and device |
| CN102432121A (en) * | 2011-10-31 | 2012-05-02 | 福建师范大学 | Device for separately storing and treating chemical experiment wastewater |
| CN103319023A (en) * | 2013-05-10 | 2013-09-25 | 浙江卓锦工程技术有限公司 | Process and system for treatment of ceramic processing wastewater |
| CN109626539A (en) * | 2019-01-21 | 2019-04-16 | 河海大学 | A kind of laboratory waste liquid collection processing system implementing |
-
2006
- 2006-12-31 CN CN 200620141862 patent/CN200992514Y/en not_active Expired - Fee Related
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101659504B (en) * | 2009-09-09 | 2011-08-03 | 周瑞兴 | A laboratory wastewater treatment method and device |
| CN102432121A (en) * | 2011-10-31 | 2012-05-02 | 福建师范大学 | Device for separately storing and treating chemical experiment wastewater |
| CN103319023A (en) * | 2013-05-10 | 2013-09-25 | 浙江卓锦工程技术有限公司 | Process and system for treatment of ceramic processing wastewater |
| CN103319023B (en) * | 2013-05-10 | 2014-09-10 | 浙江卓锦工程技术有限公司 | Process and system for treatment of ceramic processing wastewater |
| CN109626539A (en) * | 2019-01-21 | 2019-04-16 | 河海大学 | A kind of laboratory waste liquid collection processing system implementing |
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Granted publication date: 20071219 Termination date: 20100201 |