CN201386031Y - Sewage oil slick isolation device - Google Patents
Sewage oil slick isolation device Download PDFInfo
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- CN201386031Y CN201386031Y CN200920080507U CN200920080507U CN201386031Y CN 201386031 Y CN201386031 Y CN 201386031Y CN 200920080507 U CN200920080507 U CN 200920080507U CN 200920080507 U CN200920080507 U CN 200920080507U CN 201386031 Y CN201386031 Y CN 201386031Y
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- 239000010865 sewage Substances 0.000 title claims abstract description 42
- 238000002955 isolation Methods 0.000 title abstract description 6
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 51
- 238000005192 partition Methods 0.000 claims abstract description 18
- 238000000926 separation method Methods 0.000 abstract description 11
- 238000003860 storage Methods 0.000 abstract description 10
- 238000000034 method Methods 0.000 abstract description 6
- 239000000654 additive Substances 0.000 abstract description 2
- 239000004519 grease Substances 0.000 description 20
- 239000007788 liquid Substances 0.000 description 4
- 230000000694 effects Effects 0.000 description 3
- 238000009434 installation Methods 0.000 description 3
- 239000002245 particle Substances 0.000 description 3
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 239000007789 gas Substances 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 239000001301 oxygen Substances 0.000 description 2
- 229910052760 oxygen Inorganic materials 0.000 description 2
- 239000004576 sand Substances 0.000 description 2
- 238000004062 sedimentation Methods 0.000 description 2
- 239000002351 wastewater Substances 0.000 description 2
- 241000251468 Actinopterygii Species 0.000 description 1
- 229910000831 Steel Inorganic materials 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 230000002542 deteriorative effect Effects 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000010959 steel 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A20/00—Water conservation; Efficient water supply; Efficient water use
- Y02A20/20—Controlling water pollution; Waste water treatment
- Y02A20/204—Keeping clear the surface of open water from oil spills
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Abstract
一种污水浮油隔离装置,涉及含油污水处理设施的设计技术领域,包括分离池和导水管,分离池包括沉砂池、隔油池和蓄水池,在沉砂池、隔油池和蓄水池之间设置有隔板,隔板上分别设置有进、出水斜导管,本实用新型改变隔油斜管设计的方法,提供一种能达到隔除污水中浮油的污水浮油隔离装置,经多次试验,在没加入增加油溶解度的添加剂的情况下,本装置可将含油量在30~100mg/L的含油污水的污水含油量降到5mg/L以下,达到GB8978-1996一级排放标准,实现了达标排放。
A sewage floating oil isolation device relates to the technical field of design of oily sewage treatment facilities, comprising a separation tank and a water guide pipe, wherein the separation tank comprises a grit chamber, an oil separator and a water storage tank, a partition is arranged between the grit chamber, the oil separator and the water storage tank, and an inlet and outlet inclined conduit are arranged on the partition respectively. The utility model changes the design method of the oil separator inclined pipe, and provides a sewage floating oil isolation device capable of isolating and removing floating oil in sewage. After multiple tests, it is found that without adding additives for increasing oil solubility, the device can reduce the oil content of oily sewage with an oil content of 30 to 100 mg/L to below 5 mg/L, reaching the first-level emission standard of GB8978-1996, and achieving standard emission.
Description
技术领域:Technical field:
一种污水浮油隔离装置,用于将把污水中的浮油进行有效隔离,涉及含油污水处理设施的技术领域。A sewage oil slick isolating device is used for effectively isolating the slick oil in sewage, and relates to the technical field of oily sewage treatment facilities.
背景技术:Background technique:
含油污水在工作、生活中是普遍存在的,以油为动力的机械在使用中,存在油的跑、冒、滴、漏,因此,在日常工作中,与污水混合形成的含油污水也是很常见的,特别是集中进行的机械设备冲洗,清洗的油污与水混合形成大量的含油污水,稍有不慎就会流出容器对环境造成污染;污水中的油一般有三种存在形态:浮油、乳化油、溶解油,其中浮油是含油污水中含油量的主要部分,同时也是污染危害最严重的,浮油在废水中分散颗粒较大,粒径大于100μm,易于从污水中分离出来;如果浮油不去除,进入水体形成油膜,将阻碍空气中的氧气进入水体,水体复氧能力就会降低,水体中的鱼因氧的缺少而死亡,并造成水体在厌氧条件下变黑、变臭,使水质恶化;含油污水产生量较大的场所是炼化厂和大型的机械加工制造厂、大型餐饮业、大型加油站等,目前这些场所均建有含油污水的处理设备,对污水中的浮油进行收集,处理效果也较好;但是普遍存在的小型机械加工制造业、小型餐饮业、小型加油站等产生的含油污水,污水量较小,由于处理设备成本高,难以集中实施设备化处理,外排又不能达到国家排放标准,因此,目前这些地方大多数只构建有几个土建的隔油池,并采用低进高出的斜管隔油方法,对其进行储存和简单的处理,这些方法虽对污水中浮油有一定去除效果,但浮油主要是停留在几个隔油池中的第一个池中,而第一个池一般是用于调节污水的流量,起缓冲和沉砂作用,面积相对较大,所以留在里面的浮油不好收集,当暴雨季节等水量较大情况时,就会很容易造成池中浮油外溢,对污染造成严重的环境。Oily sewage is ubiquitous in work and life. During the use of oil-powered machinery, there are oil running, leaking, dripping, and leaking. Therefore, in daily work, oily sewage mixed with sewage is also very common. Yes, especially in the intensive cleaning of mechanical equipment, the cleaned oil and water are mixed to form a large amount of oily sewage, which will flow out of the container and pollute the environment if you are not careful; oil in sewage generally exists in three forms: oil slick, emulsified Oil and dissolved oil, among which slick oil is the main part of the oil content in oily sewage, and it is also the most serious pollution hazard. The slick oil has large dispersed particles in the wastewater, with a particle size greater than 100 μm, which is easy to separate from the sewage; if the slick If the oil is not removed, it will enter the water body to form an oil film, which will hinder the oxygen in the air from entering the water body, and the reoxygenation ability of the water body will be reduced. The fish in the water body will die due to the lack of oxygen, and the water body will turn black and smelly under anaerobic conditions. , deteriorating the water quality; places with a large amount of oily sewage are refineries, large-scale mechanical processing and manufacturing plants, large-scale catering industries, large-scale gas stations, etc. At present, these places are equipped with oily sewage treatment equipment to treat Oil slicks are collected, and the treatment effect is good; however, the oily sewage generated by the ubiquitous small machinery processing manufacturing industry, small catering industry, small gas stations, etc., has a small amount of sewage. Due to the high cost of treatment equipment, it is difficult to implement centralized equipment Therefore, at present, most of these places only have a few civil grease traps, and adopt the method of inclined pipe oil separation with low entry and high exit for storage and simple treatment. Although these methods have a certain effect on removing oil slicks in sewage, the oil slicks mainly stay in the first pool of several grease traps, and the first pool is generally used to adjust the flow of sewage and act as a buffer And sand settling effect, the area is relatively large, so the oil slick left in it is not easy to collect. When the water volume is large during the rainy season, it will easily cause the oil slick in the pool to overflow, causing serious environmental pollution.
发明内容:Invention content:
本实用新型的目的是针对现有技术的问题,通过改变隔油斜管设计的方法,提供一种能达到有效隔除污水中浮油的污水浮油隔离装置。The purpose of the utility model is to solve the problems in the prior art and provide a sewage oil slick isolation device which can effectively isolate the oil slick in the sewage by changing the design method of the oil slick tube.
本实用新型是这样实现的:本实用新型包括分离池和导水管,其特征是:所述分离池是一个带有底面的矩形结构,包括沉砂池、隔油池和蓄水池,在沉砂池、隔油池和蓄水池之间分别设置有隔板,在所述隔板上分别设置有进、出水斜导管;The utility model is achieved in this way: the utility model comprises a separation tank and a water guide pipe, and is characterized in that the separation tank is a rectangular structure with a bottom surface, including a grit chamber, a grease trap and a water storage tank. Partition plates are respectively arranged between the sand tank, the grease trap and the water storage tank, and inclined conduits for water inlet and outlet are respectively arranged on the partition plates;
所述进水斜导管安装在沉砂池与隔油池之间的隔板上,进口端在上,出口端在下,斜度为45°~50°;The water inlet inclined conduit is installed on the partition between the grit chamber and the grease trap, with the inlet end on the top and the outlet end on the bottom, with a slope of 45° to 50°;
所述出水斜导管安装在隔油池与蓄水池之间的隔板上,进口端向下,出口端向上,斜度为45°~50°;The outlet inclined conduit is installed on the partition between the grease trap and the reservoir, the inlet end is downward, the outlet end is upward, and the slope is 45°-50°;
所述沉砂池、隔油池和蓄水池之间分别设置的两个隔板比四边的隔板高50~100mm;The two partitions respectively arranged between the grit chamber, the grease trap and the reservoir are 50-100mm higher than the partitions on the four sides;
所述设置的进水斜导管的进口端的顶面低于矩形结构四边隔板的顶面,进水斜导管的进口端的顶面比出水斜导管出口端的顶面高50~100mm;The top surface of the inlet end of the inclined water inlet conduit is lower than the top surface of the four-sided partition of the rectangular structure, and the top surface of the inlet end of the inclined water inlet conduit is 50-100mm higher than the top surface of the outlet end of the inclined water outlet conduit;
在所述沉砂池、隔油池和蓄水池之间分别设置的隔板上可各安装一道进、出水斜导管,也可以各安装2~4道进、出水斜导管;One inlet and outlet inclined conduits can be installed respectively on the partition plates respectively arranged between the grit chamber, the grease trap and the water storage tank, or 2 to 4 inlet and outlet inclined conduits can be installed respectively;
按照矩形结构设计一个污水浮油隔离装置,将分离池分为沉砂池、隔油池和蓄水池,在沉砂池、隔油池和蓄水池之间分别设置两道高于四边的隔板,并在隔板上设置进、出水斜导管,便于污水在隔离装置中的污水和油底分离;Design a sewage oil slick isolation device according to the rectangular structure, divide the separation tank into a grit chamber, a grease trap and a water storage tank, and set up two separations higher than the four sides between the grit chamber, grease trap and water storage tank plate, and set the inlet and outlet inclined pipes on the partition to facilitate the separation of sewage and oil bottom in the isolation device;
本实用新型的原理为:The principle of the utility model is:
利用油和水密度底不同,其原理表示如下式:Utilizing the difference in density between oil and water, the principle is expressed as follows:
式中u-油品上浮速度,m/s;In the formula, u-oil floating speed, m/s;
ρs-油品的密度,kg/m3;ρ s - the density of the oil product, kg/m 3 ;
ρr-液体的密度,kg/m3;ρ r - the density of the liquid, kg/m 3 ;
d-油品粒径,m;d-oil particle size, m;
μ-液体黏度,Pa·s;μ-liquid viscosity, Pa s;
因此,在隔油池中,相对密度小于1的油品上浮至池面,并通过进、出水斜导管底连通,达到最终油水分离的目的;Therefore, in the oil separation tank, the oil with a relative density less than 1 floats to the surface of the tank, and connects through the bottom of the water inlet and outlet inclined conduits to achieve the final purpose of oil-water separation;
本实用新型底有益效果是:经过多次试验,在没加入使油乳化和增加油溶解度的添加剂的情况下,将含油底污水通过本实用新型底装置,可将含油量在30~100mg/L的含油污水的污水含油量降到5mg/L以下,含油指标达到《污水综合排放标准》(GB8978-1996)一级标准,实现了排放污水在含油指标方面达标。The beneficial effects of the bottom of the utility model are: after many tests, without adding additives to emulsify oil and increase oil solubility, the oily bottom sewage can be passed through the bottom device of the utility model, and the oil content can be reduced to 30-100 mg/L. The oil content of the oily sewage is reduced to below 5mg/L, and the oil content index reaches the first-level standard of the "Comprehensive Discharge Standard for Sewage" (GB8978-1996), realizing that the discharged sewage reaches the standard in terms of oil content index.
附图说明:Description of drawings:
图1为本实用新型的剖面结构示意图。Fig. 1 is a schematic cross-sectional structure diagram of the utility model.
图2为本实用新型的俯视结构示意图。Fig. 2 is a top view structural diagram of the utility model.
具体实施方式:Detailed ways:
下面结合附图给出本实用新型的实施例:本实用新型包括分离池和导水管,分离池是一个带有底面的矩形结构,包括沉砂池7、隔油池8和蓄水池9,在沉砂池7、隔油池8和蓄水池9之间分别设置有隔板3和4,在隔板3和4上分别设置有进、出水斜导管2和5,进水斜导管2安装在沉砂池7与隔油池8之间的隔板3上,进水斜导管2的进口端在上,出口端在下,安装斜度为45°~50°;出水斜导管5安装在隔油池8与蓄水池9之间的隔板4上,出水斜导管5的进口端向下,出口端向上,安装斜度为45°~50°;在沉砂池7、隔油池8和蓄水池9之间分别设置的两个隔板3和4比四边的隔板1高50~100mm;设置的进水斜导管2的进口端的顶面低于矩形结构四边的隔板1的顶面,进水斜导管5的进口端的顶面比出水斜导管5出口端的顶面高50~100mm;为了防止流量较大溢出的情况,可以在沉砂池7、隔油池8和蓄水池9之间分别设置的隔板3和4上可各安装一道进、出水斜导管,也可以各安装2~4道进、出水斜导管;Provide the embodiment of the present utility model below in conjunction with accompanying drawing: the present utility model comprises separating tank and aqueduct, and separating tank is a rectangular structure with bottom surface, comprises
本实用新型特别适用于含油污水产生量较小,以浮油为主的场所,也适用于以浮油为主污水量较大的场所;The utility model is especially suitable for places where oily sewage is produced in a small amount and oil slicks are the main source, and it is also suitable for places where oil slicks are the main source of sewage;
使用时,含油废水首先由管道输入沉砂池7,当液面的高度到达设置的进水斜导管5的进口端时,液体就会通过进水斜导管5的进口进入隔油池8,较重的物质则留在沉砂池7中,由于浮在上面的主要是油污,所以流入隔油池8的包括浮油和污水,带有浮油的污水进入隔油池8后,浮油上浮,由于设置的出水斜导管5的进水口向下,而出水口向上,所以,留在下面的水通过设置的出水斜导管5的进水口通过斜管上溢至蓄水池9,而浮在表面的浮油就留在了隔油池8中,最终流入蓄水池9的水通过前面两个池的沉淀和排油,达标的水通过出口6排出;当沉淀物在沉淀池7中达到一定高度时,可以暂时停止污水的输入,将沉淀池7和隔油池8中的固体物质和分出的油污清除后再开始清除油污的程序;During use, the oily waste water is first imported into the
设置的进、出水斜导管2和5可以是pvc管或者钢管,可用圆形管,也可用矩形管;The set inlet and outlet
制作时,如考虑道污水池油含量较高的情况时,可采用将本使用新型进行串联设计的方式,串连2~3个本实用新型的装置,实现多级隔除油污的目标,各部分的设置与安装与单个的相同。When making, if considering the situation of high oil content in the sewer sewage pool, the method of cascading the utility model can be adopted, and 2 to 3 devices of the utility model can be connected in series to realize the goal of multi-stage separation and removal of oil pollution, each Partial setup and installation are the same as single ones.
Claims (6)
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| CN200920080507U CN201386031Y (en) | 2009-04-30 | 2009-04-30 | Sewage oil slick isolation device |
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Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103359846A (en) * | 2013-08-08 | 2013-10-23 | 河南城建学院 | Oily wastewater treatment system and process for treating oily wastewater by using same |
| CN105198038A (en) * | 2014-06-26 | 2015-12-30 | 江苏天地化纤有限公司 | Oil-water separation device for oily wastewater in chemical fiber production |
| CN111115889A (en) * | 2020-02-10 | 2020-05-08 | 中国石油天然气股份有限公司 | Device and method for recovering and treating waste liquid generated in oilfield operation under negative pressure |
| CN114891562A (en) * | 2022-05-27 | 2022-08-12 | 郝艺琳 | Processing system of edible vegetable oil |
-
2009
- 2009-04-30 CN CN200920080507U patent/CN201386031Y/en not_active Expired - Fee Related
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103359846A (en) * | 2013-08-08 | 2013-10-23 | 河南城建学院 | Oily wastewater treatment system and process for treating oily wastewater by using same |
| CN103359846B (en) * | 2013-08-08 | 2014-10-22 | 河南城建学院 | Oily wastewater treatment system and process for treating oily wastewater by using same |
| CN105198038A (en) * | 2014-06-26 | 2015-12-30 | 江苏天地化纤有限公司 | Oil-water separation device for oily wastewater in chemical fiber production |
| CN111115889A (en) * | 2020-02-10 | 2020-05-08 | 中国石油天然气股份有限公司 | Device and method for recovering and treating waste liquid generated in oilfield operation under negative pressure |
| CN114891562A (en) * | 2022-05-27 | 2022-08-12 | 郝艺琳 | Processing system of edible vegetable oil |
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