CN206624676U - A kind of oily-water seperating equipment - Google Patents

A kind of oily-water seperating equipment Download PDF

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CN206624676U
CN206624676U CN201720329050.3U CN201720329050U CN206624676U CN 206624676 U CN206624676 U CN 206624676U CN 201720329050 U CN201720329050 U CN 201720329050U CN 206624676 U CN206624676 U CN 206624676U
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曾雄华
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Wuhan Qilong Technology Development Co Ltd
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Abstract

本实用新型公开了一种油水分离装置,包括:除渣机构,其包括除渣罐、格栅、进水口、排渣口、及溢流管;沉淀机构,其包括沉淀池、污泥切割泵及多个第一隔板,每个第一隔板均连接于沉淀池的一侧内壁并与沉淀池的另一侧内壁之间形成有第一间隙,相邻两个隔板交错设置;分离机构,其包括分离池、油槽、刮油机、排水管、多个气泡发生器及多个第二隔板。本实用新型一方面在沉淀池内设置多个第一隔板,使沉淀池上端形成首尾连通的S型流道,其避免了对流道的出水端形成冲击,提高沉淀效率,同时设置第二间隙也便于沉淀于底部的残渣的排出;另一方面设置第二隔板,其降低了对分离池内油水的冲击且延长了油水分离时间,提高了油水分离效率。

The utility model discloses an oil-water separation device, which comprises: a slag removal mechanism, which includes a slag removal tank, a grid, a water inlet, a slag discharge port, and an overflow pipe; a sedimentation mechanism, which includes a sedimentation tank, and a sludge cutting pump and a plurality of first partitions, each first partition is connected to one inner wall of the sedimentation tank and forms a first gap with the other inner wall of the sedimentation tank, and two adjacent partitions are arranged alternately; separated The mechanism includes a separation pool, an oil tank, an oil scraper, a drain pipe, multiple bubble generators and multiple second partitions. On the one hand, the utility model arranges a plurality of first partitions in the sedimentation tank, so that the upper end of the sedimentation tank forms an S-shaped flow channel connected from end to end, which avoids the impact on the water outlet of the flow channel, improves the sedimentation efficiency, and sets the second gap at the same time. It facilitates the discharge of the residue deposited at the bottom; on the other hand, a second separator is provided, which reduces the impact on the oil and water in the separation tank and prolongs the oil and water separation time, improving the oil and water separation efficiency.

Description

一种油水分离装置An oil-water separation device

技术领域technical field

本实用新型涉及油水分离技术,尤其是涉及一种油水分离装置。The utility model relates to oil-water separation technology, in particular to an oil-water separation device.

背景技术Background technique

随着我国社会经济的发展,大量餐饮企业应运而生,宾馆、酒店、饭店、食堂和集中式餐饮综合体的规模日益扩大,数量日益增多,随之产生的餐饮废水越来越多,其严重的自然生态环境,而油水分离器可较好的对餐饮废水进行处理,以降低其污染率。由于餐饮废水中含有大量的残渣,需要通过格栅或滤网进行过滤,但是过滤后的废水中依然存在小颗粒的固态残渣,故需要对上述固态残渣进行沉淀以将固态残渣排出。目前,一般直接将过滤后的污水进行沉淀处理,但是由于餐饮废水在过滤时进出极不稳定,其过滤后易对沉淀后的污水形成冲击、震荡,导致沉淀池内的废水长期处于浑浊状态,其达不到沉淀固态残渣的目的;同时,现有的油水分离器主要利用油水比重不同进行沉淀式分离,但是在实际应用时,废水是不间断排出的,易导致油水分离时发生震荡,其降低了油水分离效率。With the development of our country's social economy, a large number of catering enterprises have emerged as the times require. The scale and number of hotels, hotels, restaurants, canteens and centralized catering complexes are increasing day by day, and the resulting catering wastewater is increasing. The natural ecological environment, and the oil-water separator can better treat the catering wastewater to reduce its pollution rate. Since the catering wastewater contains a large amount of residue, it needs to be filtered through a grid or a filter, but there are still small particles of solid residue in the filtered wastewater, so the above solid residue needs to be precipitated to discharge the solid residue. At present, the filtered sewage is generally directly subjected to sedimentation treatment, but because the catering wastewater is extremely unstable when it is filtered, it is easy to form impacts and vibrations on the sedimented sewage after filtration, resulting in the long-term turbidity of the wastewater in the sedimentation tank. The purpose of precipitating solid residues cannot be achieved; at the same time, the existing oil-water separator mainly uses the difference in specific gravity of oil and water for sedimentation separation, but in practical application, the waste water is continuously discharged, which may easily lead to vibration during oil-water separation, which reduces the oil-water separation efficiency.

实用新型内容Utility model content

本实用新型的目的在于克服上述技术不足,提出一种油水分离装置,解决现有技术中油水分离时固态残渣分离差、油水分离效率低的技术问题。The purpose of the utility model is to overcome the above-mentioned technical deficiencies, propose an oil-water separation device, and solve the technical problems of poor solid residue separation and low oil-water separation efficiency in the prior art during oil-water separation.

为达到上述技术目的,本实用新型的技术方案提供一种油水分离装置,包括:In order to achieve the above technical purpose, the technical solution of the present utility model provides an oil-water separation device, comprising:

除渣机构,其包括除渣罐、倾斜设置于所述除渣罐内并将所述除渣罐内的除渣腔体分隔形成第一腔体和第二腔体的格栅、与所述第一腔体连通的进水口和排渣口、及与所述第二腔体连通的溢流管;The slag removal mechanism includes a slag removal tank, a grid that is arranged obliquely in the slag removal tank and separates the slag removal cavity in the slag removal tank to form a first cavity and a second cavity, and the grid that is connected to the slag removal tank A water inlet and a slag outlet connected to the first cavity, and an overflow pipe connected to the second cavity;

沉淀机构,其包括进水端与所述溢流管连接的沉淀池、设于所述沉淀池底部的污泥切割泵及平行设置于所述沉淀池内的多个第一隔板,每个第一隔板均连接于所述沉淀池的一侧内壁并与所述沉淀池的另一侧内壁之间形成有第一间隙,相邻两个隔板交错设置,且每个第一隔板下端与沉淀池底部之间具有第二间隙;The sedimentation mechanism includes a sedimentation tank whose water inlet is connected to the overflow pipe, a sludge cutting pump arranged at the bottom of the sedimentation tank, and a plurality of first partitions arranged in parallel in the sedimentation tank. A partition is connected to one inner wall of the sedimentation tank and forms a first gap with the other inner wall of the sedimentation tank, two adjacent partitions are arranged alternately, and the lower end of each first partition There is a second gap with the bottom of the sedimentation tank;

分离机构,其包括分离池、油槽、刮油机、排水管、多个气泡发生器及多个第二隔板,多个所述第二隔板平行内置于所述分离池并将分离池分隔形成首尾依次连通的多个分离腔体,位于前端的分离腔体与所述沉淀池的溢流口连接,位于末端的分离腔体的下端与排水管连接;多个气泡发生器一一对应设置于所述分离腔体底部,所述刮油机一端内置于末端分离腔体的上端、另一端延伸至所述油槽内。The separation mechanism includes a separation tank, an oil tank, an oil scraper, a drain pipe, a plurality of bubble generators and a plurality of second partitions, and a plurality of second partitions are built in parallel in the separation tank and separate the separation tank Form a plurality of separation chambers connected in sequence from end to end, the separation chamber at the front end is connected to the overflow port of the sedimentation tank, and the lower end of the separation chamber at the end is connected to the drain pipe; multiple bubble generators are arranged one by one At the bottom of the separation chamber, one end of the oil scraper is built into the upper end of the terminal separation chamber, and the other end extends into the oil tank.

优选的,所述分离机构还包括设于末端的分离腔体上端的加热器。Preferably, the separation mechanism further includes a heater arranged at the upper end of the separation chamber at the end.

优选的,所述分离机构还包括用于检测所述分离池的液位的液位传感器、设于所述排水管上的电磁阀及根据液位控制所述电磁阀开关的控制器。Preferably, the separation mechanism further includes a liquid level sensor for detecting the liquid level of the separation tank, a solenoid valve provided on the drain pipe, and a controller for controlling the switch of the solenoid valve according to the liquid level.

优选的,所述控制器包括用于采集液位传感器检测液位产生的电信号的液位信号采集电路、用于比较所述电信号是否大于第一阈值的第一比较电路、用于当所述电信号大于第一阈值时驱动所述电磁阀导通的第一驱动电路、用于比较所述电信号是否小于第二阈值的第二比较电路、用于当所述电信号大于第二阈值时驱动所述电磁阀断通的第二驱动电路。Preferably, the controller includes a liquid level signal acquisition circuit for collecting an electrical signal generated by the liquid level sensor to detect the liquid level, a first comparison circuit for comparing whether the electrical signal is greater than a first threshold, and a circuit for when the When the electrical signal is greater than the first threshold, a first drive circuit for driving the solenoid valve to conduct, a second comparison circuit for comparing whether the electrical signal is less than the second threshold, and a second comparison circuit for comparing the electrical signal when the electrical signal is greater than the second threshold The second driving circuit that drives the electromagnetic valve to be turned off at the time.

优选的,所述除渣机构还包括一螺旋排渣机,所述螺旋排渣机水平设置且其进料端与所述排渣口连接。Preferably, the slag removal mechanism further includes a screw slag discharger, the screw slag discharger is arranged horizontally and its feed end is connected to the slag discharge port.

与现有技术相比,本实用新型一方面在沉淀池内设置多个第一隔板,使沉淀池上端形成首尾连通的S型流道,其避免了对流道的出水端形成冲击,提高沉淀效率,同时设置第二间隙也便于沉淀于底部的残渣的排出;另一方面设置第二隔板,其降低了对分离池内油水的冲击且延长了油水分离时间,提高了油水分离效率。Compared with the prior art, on the one hand, the utility model sets a plurality of first partitions in the sedimentation tank, so that the upper end of the sedimentation tank forms an S-shaped flow channel connected from end to end, which avoids the impact on the outlet end of the flow channel and improves the sedimentation efficiency At the same time, setting the second gap also facilitates the discharge of the residue deposited at the bottom; on the other hand, setting the second separator reduces the impact on the oil and water in the separation tank and prolongs the oil and water separation time, improving the oil and water separation efficiency.

附图说明Description of drawings

图1是本实用新型的油水分离装置的连接结构示意图;Fig. 1 is the connection structure schematic diagram of the oil-water separation device of the present utility model;

图2是本实用新型的图1的俯视图;Fig. 2 is the top view of Fig. 1 of the present utility model;

图3是本实用新型的控制器的连接框图。Fig. 3 is a connection block diagram of the controller of the present invention.

具体实施方式detailed description

为了使本实用新型的目的、技术方案及优点更加清楚明白,以下结合附图及实施例,对本实用新型进行进一步详细说明。应当理解,此处所描述的具体实施例仅仅用以解释本实用新型,并不用于限定本实用新型。In order to make the purpose, technical solution and advantages of the utility model clearer, the utility model will be further described in detail below in conjunction with the accompanying drawings and embodiments. It should be understood that the specific embodiments described here are only used to explain the utility model, and are not intended to limit the utility model.

请参阅图1、图2,本实用新型的实施例提供了一种油水分离装置,包括:Referring to Fig. 1 and Fig. 2, the embodiment of the present utility model provides an oil-water separation device, comprising:

除渣机构1,其包括除渣罐11、倾斜设置于所述除渣罐11内并将所述除渣罐11内的除渣腔体分隔形成第一腔体和第二腔体的格栅12、与所述第一腔体连通的进水口13和排渣口14、及与所述第二腔体连通的溢流管15;The slag removal mechanism 1 includes a slag removal tank 11, a grid that is arranged obliquely in the slag removal tank 11 and separates the slag removal chamber in the slag removal tank 11 to form a first cavity and a second cavity 12. A water inlet 13 and a slag outlet 14 communicating with the first cavity, and an overflow pipe 15 communicating with the second cavity;

沉淀机构2,其包括进水端与所述溢流管15连接的沉淀池21、设于所述沉淀池21底部的污泥切割泵22及平行设置于所述沉淀池21内的多个第一隔板23,每个第一隔板23均连接于所述沉淀池21的一侧内壁并与所述沉淀池21的另一侧内壁之间形成有第一间隙231,相邻两个隔板交错设置,且每个第一隔板23下端与沉淀池21底部之间具有第二间隙232;Settling mechanism 2, which includes a settling tank 21 whose water inlet is connected to the overflow pipe 15, a sludge cutting pump 22 arranged at the bottom of the settling tank 21, and a plurality of first settling tanks arranged in parallel in the settling tank 21 A partition 23, each first partition 23 is connected to one side inner wall of the sedimentation tank 21 and forms a first gap 231 with the other side inner wall of the sedimentation tank 21, two adjacent partitions The plates are staggered, and there is a second gap 232 between the lower end of each first partition 23 and the bottom of the sedimentation tank 21;

分离机构3,其包括分离池31、油槽32、刮油机33、排水管34、多个气泡发生器35及多个第二隔板36,多个所述第二隔板36平行内置于所述分离池31并将分离池31分隔形成首尾依次连通的多个分离腔体311,位于前端的分离腔体311与所述沉淀池21的溢流口211连接,位于末端的分离腔体311的下端与排水管34连接;多个气泡发生器35一一对应设置于所述分离腔体311底部,所述刮油机33一端内置于末端分离腔体311的上端、另一端延伸至所述油槽32内。The separation mechanism 3 includes a separation tank 31, an oil tank 32, an oil scraper 33, a drain pipe 34, a plurality of bubble generators 35 and a plurality of second partitions 36, and a plurality of the second partitions 36 are built in parallel Describe the separation tank 31 and separate the separation tank 31 to form a plurality of separation chambers 311 connected in sequence from end to end, the separation chamber 311 at the front end is connected with the overflow port 211 of the sedimentation tank 21, and the separation chamber 311 at the end The lower end is connected to the drain pipe 34; a plurality of bubble generators 35 are arranged one by one at the bottom of the separation chamber 311, one end of the oil scraper 33 is built into the upper end of the terminal separation chamber 311, and the other end extends to the oil tank within 32.

本实施例进行油水分离时,餐饮废水由进水口13进入除渣罐11的第一腔体内,废水中的油水及小颗粒残渣穿过格栅12上的滤孔进入第二腔体,而餐饮废水中的大颗粒残渣则留在第一腔体内,第一腔体内的残渣可通过设于除渣罐11底部的排渣口14排出,而进入第二腔体内的污水及小颗粒残渣则经过溢流管15进入沉淀池21内,沉淀池21内的第一隔板23均竖直交错设置,从而使得分离池31上端形成呈S型的流道,该流道的前端会受到由溢流管15排出的废水的冲击,随着废水沿流道运动其逐渐趋于平静,其有利于废水中的小颗粒残渣的沉淀,同时采用S型流道也增加废水在沉淀池21内的停留时间,其有利于提高小颗粒残渣的沉降率;同时,本实施例第一隔板23下端与沉淀池21底部之间具有第二间隙232,即第一隔板23下端与沉淀池21底部之间具有一定间距,上述间距可用于沉淀小颗粒杂质,其有利于后续通过污泥切割泵22将沉淀的杂质排出;经过沉淀后的废水由沉淀池21上的溢流口211溢流进入分离池31内,而分离池31内的第二隔板36将分离池31分隔形成首尾依次连通的多个分离腔体311,第二隔板36与第一隔板23的设置大致相同,但第二隔板36下端连接于分离池31底部,使得多个分离腔体311连通形成一S型腔体,其延长了废水在分离池31内的停留时间,有利于多个气泡发生器35依次对废水进行油水分离,在分离池31底部的多个气泡发生器35的依次作用下,每个分离腔体311底部均形成较多微小气泡,由于油水比重不同,在微小气泡的作用下,污水中的油随其上浮至液面表层,其提高油水的分离效率;分层后的油水运动至末端的分离腔体311后,由刮油机33将上层的油污带出至油槽32内,而位于下层的污水则有排水管34排出。When oil-water separation is carried out in this embodiment, the catering wastewater enters the first cavity of the slag removal tank 11 through the water inlet 13, and the oily water and small particle residues in the wastewater enter the second cavity through the filter holes on the grid 12, and the catering wastewater enters the second cavity through the filter holes on the grid 12. The large particle residues in the waste water are left in the first cavity, and the residues in the first cavity can be discharged through the slag discharge port 14 located at the bottom of the slag removal tank 11, while the sewage and small particle residues entering the second cavity are passed through The overflow pipe 15 enters the sedimentation tank 21, and the first partitions 23 in the sedimentation tank 21 are all vertically staggered, so that the upper end of the separation tank 31 forms an S-shaped flow channel, and the front end of the flow channel will be affected by the overflow. The impact of the waste water discharged from the pipe 15 tends to calm gradually as the waste water moves along the flow channel, which is conducive to the precipitation of small particle residues in the waste water. At the same time, the use of the S-shaped flow channel also increases the residence time of the waste water in the sedimentation tank 21 , which is conducive to improving the sedimentation rate of small particle residues; at the same time, there is a second gap 232 between the lower end of the first partition 23 and the bottom of the sedimentation tank 21 in this embodiment, that is, between the lower end of the first partition 23 and the bottom of the sedimentation tank 21 With a certain distance, the above distance can be used to precipitate small particles of impurities, which is conducive to the subsequent discharge of the precipitated impurities through the sludge cutting pump 22; after sedimentation, the wastewater overflows from the overflow port 211 on the sedimentation tank 21 and enters the separation tank 31 inside, and the second partition 36 in the separation pool 31 separates the separation pool 31 to form a plurality of separation cavities 311 connected in sequence from end to end, the second partition 36 is set roughly the same as the first partition 23, but the second partition The lower end of the plate 36 is connected to the bottom of the separation tank 31, so that a plurality of separation cavities 311 are connected to form an S-shaped cavity, which prolongs the residence time of the waste water in the separation tank 31, and is beneficial to a plurality of bubble generators 35 to sequentially treat the waste water. Oil-water separation, under the sequential action of multiple bubble generators 35 at the bottom of the separation tank 31, many tiny bubbles are formed at the bottom of each separation chamber 311. Due to the different specific gravity of oil and water, under the action of the tiny bubbles, the oil in the sewage As it floats up to the surface of the liquid surface, it improves the separation efficiency of oil and water; after the stratified oil and water move to the separation chamber 311 at the end, the oil on the upper layer is taken out by the oil scraper 33 into the oil tank 32, while the oil on the lower layer Sewage then has drainage pipe 34 to discharge.

当废油在微小气泡的作用下上浮至污水表层时,油分子结合一起在低温下易形成固态油脂,故本实施例所述分离机构3还包括设于末端的分离腔体311上端的加热器37,其主要用于在冬季或春初对位于末端的分离腔体311的上层油污进行加热,以保证油污为液态,从而便于将其排至油槽32内。When the waste oil floats to the surface of the sewage under the action of tiny air bubbles, the oil molecules combine together to form solid grease at low temperature, so the separation mechanism 3 in this embodiment also includes a heater located at the upper end of the separation cavity 311 at the end 37, which is mainly used to heat the upper layer of oil in the separation chamber 311 located at the end in winter or early spring, so as to ensure that the oil is in a liquid state, so that it can be easily discharged into the oil tank 32.

如图1、图2、图3所示,油水分层效果越好则排水管34排出的污水中含油率越低,其对环境的污染越低,而分离池31内的液位越高则越利于油水分层,故本实施例所述分离机构3还包括用于检测所述分离池31的液位的液位传感器38、设于所述排水管34上的电磁阀39及根据液位控制所述电磁阀39开关的控制器30,其可控制在较高液位时才进行污水的排出。As shown in Fig. 1, Fig. 2 and Fig. 3, the better the effect of oil-water stratification, the lower the oil content in the sewage discharged from the drain pipe 34, the lower the pollution to the environment, and the higher the liquid level in the separation tank 31 The more conducive to oil-water stratification, so the separation mechanism 3 of the present embodiment also includes a liquid level sensor 38 for detecting the liquid level of the separation pool 31, a solenoid valve 39 arranged on the drain pipe 34, and a liquid level sensor according to the liquid level. The controller 30 that controls the switch of the electromagnetic valve 39 can control the sewage to be discharged only when the liquid level is higher.

具体如图3所示,所述控制器30包括用于采集液位传感器38检测液位产生的电信号的液位信号采集电路301、用于比较所述电信号是否大于第一阈值的第一比较电路302、用于当所述电信号大于第一阈值时驱动所述电磁阀39导通的第一驱动电路303、用于比较所述电信号是否小于第二阈值的第二比较电路304、用于当所述电信号大于第二阈值时驱动所述电磁阀39断通的第二驱动电路305。当分离池31内的液位高于上限定值时,液位传感器38检测液位产生电信号大于第一阈值,第一驱动电路303驱动电磁阀39导通,排水管34开始排水;当分离池31内的液位排至低于下限定值时,液位传感器38检测液位产生的电信号小于第二阈值,第二驱动电路305驱动电磁阀39断通,排水管34停止排水,其实现了仅仅当分离池31内液位在上限定值和下限定值之间时才进行排水,避免了水位过低状况下进行排水,保证分离池31内具有一定的液位高度,其有利于保证分离池31的油水不间断进行油水分离,其可最大化的提高油水分离效率。Specifically as shown in FIG. 3 , the controller 30 includes a liquid level signal acquisition circuit 301 for collecting the electrical signal generated by the liquid level sensor 38 to detect the liquid level, and a first circuit for comparing whether the electrical signal is greater than the first threshold. A comparison circuit 302, a first drive circuit 303 for driving the solenoid valve 39 to conduct when the electrical signal is greater than a first threshold, a second comparison circuit 304 for comparing whether the electrical signal is smaller than a second threshold, The second drive circuit 305 is used to drive the solenoid valve 39 off when the electric signal is greater than the second threshold. When the liquid level in the separation tank 31 was higher than the upper limit value, the liquid level sensor 38 detected that the liquid level generated an electrical signal greater than the first threshold, and the first drive circuit 303 drove the solenoid valve 39 to conduct, and the drain pipe 34 began to drain water; When the liquid level in the pool 31 is discharged below the lower limit value, the electric signal generated by the liquid level sensor 38 detected by the liquid level is less than the second threshold value, the second drive circuit 305 drives the solenoid valve 39 to be turned off, and the drain pipe 34 stops draining water. Only when the liquid level in the separation tank 31 is between the upper limit value and the lower limit value, the drainage is realized, which avoids draining water when the water level is too low, and ensures that the separation tank 31 has a certain liquid level height, which is conducive to Ensure that the oil and water in the separation tank 31 are separated from oil and water without interruption, which can maximize the efficiency of oil and water separation.

为了便于排渣,本实施例所述除渣机构1还包括一螺旋排渣机16,所述螺旋排渣机16水平设置且其进料端与所述排渣口14连接。In order to facilitate slag discharge, the slag removal mechanism 1 in this embodiment further includes a spiral slag discharge machine 16 , the spiral slag discharge machine 16 is arranged horizontally and its feed end is connected to the slag discharge port 14 .

与现有技术相比,本实用新型一方面在沉淀池内设置多个第一隔板,使沉淀池上端形成首尾连通的S型流道,其避免了对流道的出水端形成冲击,提高沉淀效率,同时设置第二间隙也便于沉淀于底部的残渣的排出;另一方面设置第二隔板,其降低了对分离池内油水的冲击且延长了油水分离时间,提高了油水分离效率。Compared with the prior art, on the one hand, the utility model sets a plurality of first partitions in the sedimentation tank, so that the upper end of the sedimentation tank forms an S-shaped flow channel connected from end to end, which avoids the impact on the outlet end of the flow channel and improves the sedimentation efficiency At the same time, setting the second gap also facilitates the discharge of the residue deposited at the bottom; on the other hand, setting the second separator reduces the impact on the oil and water in the separation tank and prolongs the oil and water separation time, improving the oil and water separation efficiency.

以上所述本实用新型的具体实施方式,并不构成对本实用新型保护范围的限定。任何根据本实用新型的技术构思所做出的各种其他相应的改变与变形,均应包含在本实用新型权利要求的保护范围内。The specific embodiments of the utility model described above do not constitute a limitation to the protection scope of the utility model. Any other corresponding changes and deformations made according to the technical concept of the utility model shall be included in the protection scope of the claims of the utility model.

Claims (5)

  1. A kind of 1. oily-water seperating equipment, it is characterised in that including:
    Slag removal mechanism, it includes slag removal tank, is obliquely installed and divides in the slag removal tank and by the slagging-off cavity in the slag removal tank Every grid, the water inlet connected with first cavity and the slag-drip opening for forming the first cavity and the second cavity and with described the The overflow pipe of two cavitys connection;
    Mechanism is precipitated, it includes sedimentation basin, the sludge located at the sedimentation basin bottom that water inlet end is connected with the overflow pipe and cut Cut pump and the multiple first partitions being set in parallel in the sedimentation basin, each first partition are all connected to the one of the sedimentation basin Side inwall is simultaneously staggered between the opposite side inwall of the sedimentation basin formed with the first gap, two neighboring dividing plate, and often There is the second gap between individual first partition lower end and sedimentation basin bottom;
    Separating mechanism, it includes separate tank, oil groove, Oil scraper, drainpipe, multiple bubble generators and multiple second partitions, more The individual second partition is parallel to be built in the separate tank and separate tank is separated to form to the multiple disengagement chambers being sequentially communicated from beginning to end Body, the separation cavity positioned at front end are connected with the overfall of the sedimentation basin, positioned at the lower end of the separation cavity of end and draining Pipe connects;Multiple bubble generators correspond and are arranged at the separation cavity bottom, and described Oil scraper one end is built in end Separate the upper end of cavity, the other end is extended in the oil groove.
  2. 2. oily-water seperating equipment according to claim 1, it is characterised in that the separating mechanism is also included located at end Separate the heater of cavity upper end.
  3. 3. oily-water seperating equipment according to claim 1 or 2, it is characterised in that the separating mechanism also includes being used to examine Survey the liquid level sensor, the magnetic valve on the drainpipe and the electromagnetism according to Liquid level of the liquid level of the separate tank The controller of threshold switch.
  4. 4. oily-water seperating equipment according to claim 3, it is characterised in that the controller includes being used to gather liquid level biography Sensor detects the liquid level signal Acquisition Circuit of electric signal caused by liquid level, whether is more than first threshold for the electric signal The first comparison circuit, for driven when the electric signal is more than first threshold the solenoid valve conduction first drive electricity Road, for the electric signal whether be less than Second Threshold the second comparison circuit, for when the electric signal be more than second The second drive circuit that the magnetic valve is open close is driven during threshold value.
  5. 5. oily-water seperating equipment according to claim 4, it is characterised in that the slag removal mechanism also includes a spiral deslagging Machine, the helical slag removing machine is horizontally disposed and its feed end is connected with the slag-drip opening.
CN201720329050.3U 2017-03-31 2017-03-31 A kind of oily-water seperating equipment Expired - Fee Related CN206624676U (en)

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Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN111871005A (en) * 2020-07-14 2020-11-03 国家能源集团煤焦化有限责任公司 Separation device for sulfolane and heat conduction oil
CN112474578A (en) * 2020-10-21 2021-03-12 康硕电气集团有限公司 Multi-effect ultrasonic cleaning machine
CN113006767A (en) * 2021-04-26 2021-06-22 东北石油大学 Underground oil-water separator and separation system thereof
CN115990587A (en) * 2023-01-19 2023-04-21 中国神华煤制油化工有限公司 cleaning equipment
CN116693054A (en) * 2023-06-19 2023-09-05 安徽中源锦天环境科技股份有限公司 High-efficient deep bed jar and sewage treatment system thereof
CN117654119A (en) * 2023-12-28 2024-03-08 腾达建设集团股份有限公司 A mud treatment system
CN117840189A (en) * 2024-01-05 2024-04-09 武汉动力电池再生技术有限公司 Glue removal device

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN111871005A (en) * 2020-07-14 2020-11-03 国家能源集团煤焦化有限责任公司 Separation device for sulfolane and heat conduction oil
CN111871005B (en) * 2020-07-14 2022-03-01 国家能源集团煤焦化有限责任公司 Separation device for sulfolane and heat conduction oil
CN112474578A (en) * 2020-10-21 2021-03-12 康硕电气集团有限公司 Multi-effect ultrasonic cleaning machine
CN113006767A (en) * 2021-04-26 2021-06-22 东北石油大学 Underground oil-water separator and separation system thereof
CN115990587A (en) * 2023-01-19 2023-04-21 中国神华煤制油化工有限公司 cleaning equipment
CN116693054A (en) * 2023-06-19 2023-09-05 安徽中源锦天环境科技股份有限公司 High-efficient deep bed jar and sewage treatment system thereof
CN116693054B (en) * 2023-06-19 2024-08-16 安徽中源锦天环境科技股份有限公司 High-efficient deep bed jar and sewage treatment system thereof
CN117654119A (en) * 2023-12-28 2024-03-08 腾达建设集团股份有限公司 A mud treatment system
CN117840189A (en) * 2024-01-05 2024-04-09 武汉动力电池再生技术有限公司 Glue removal device

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