CN206228987U - A kind of device being automatically separated for water and organic solvent - Google Patents
A kind of device being automatically separated for water and organic solvent Download PDFInfo
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Abstract
Description
技术领域technical field
本实用新型涉及液体分离技术领域,具体涉及一种用于水和有机溶剂自动分离的装置。The utility model relates to the technical field of liquid separation, in particular to a device for automatic separation of water and organic solvents.
背景技术Background technique
工业生产中,产生的废水中一般含有较多的有机溶剂,直接排放会对环境造成较大的污染。由于一般有机溶剂和水比重不同,一般采用不同高度排放口进行分离。但是,分离时大部分靠人工操作,不易控制,很容易造成分离效果差,导致需要多次分离提纯,工作量大,加工成本高,分离效率低。In industrial production, the wastewater produced generally contains more organic solvents, and direct discharge will cause greater pollution to the environment. Due to the different specific gravity of general organic solvents and water, different height discharge outlets are generally used for separation. However, most of the separation is manual operation, which is not easy to control, and it is easy to cause poor separation effect, resulting in the need for multiple separation and purification, heavy workload, high processing cost and low separation efficiency.
现有技术中,专利文献CN102210944A中公开了一种溶剂回收分离装置,设有在其内部分隔成储油室、缓冲室、储水室和出水室共4个溶液室的密封容器。缓冲室设混合溶液入口,储油室设有机溶剂出口和排渣口;储油室、缓冲室、储水室设排水口,在出水室设出水口;有机溶剂出口设齿轮油泵,储油室顶部设磁浮球液位开关,储水室、缓冲室顶部设排气口;储油室设人孔,缓冲室的底部与储水室相通,缓冲室上部与储油室相通,储水室上设有过水板,水通过过水板上部进入出水室。储水室与缓冲室相隔的过水板顶面低于缓冲室与储油室之间有机溶剂过流板顶面。利用有机溶剂与水的密度差别及过水板与有机溶剂过流板的顶面高度差,有机溶剂和水从缓冲室自动分层进入储油室和储水室。水被自动抽回到系统循环使用。溶剂被油泵自动抽至溶剂储存罐。然而该装置存在结构较复杂,不容易清洗的问题,不适合分离较慢的水和有机溶剂混合物的连续分离。In the prior art, patent document CN102210944A discloses a solvent recovery and separation device, which is provided with a sealed container which is divided into four solution chambers: an oil storage chamber, a buffer chamber, a water storage chamber and a water outlet chamber. The buffer room is equipped with a mixed solution inlet, and the oil storage room is equipped with an organic solvent outlet and a slag discharge port; the oil storage room, buffer room, and water storage room are provided with a drain port, and the water outlet room is provided with a water outlet; the organic solvent outlet is provided with a gear oil pump, and the oil storage room The top is equipped with a magnetic float level switch, the water storage room and the top of the buffer room are equipped with an exhaust port; A water passing board is provided, and water enters the water outlet chamber through the upper part of the water passing board. The top surface of the water flow plate separating the water storage chamber from the buffer chamber is lower than the top surface of the organic solvent flow plate between the buffer chamber and the oil storage chamber. Utilizing the difference in density between the organic solvent and water and the height difference between the water flow plate and the top surface of the organic solvent flow plate, the organic solvent and water are automatically stratified from the buffer chamber into the oil storage chamber and the water storage chamber. Water is automatically pumped back into the system for recycling. The solvent is automatically pumped to the solvent storage tank by the oil pump. However, this device has the problems of complex structure and difficult cleaning, and is not suitable for the continuous separation of slow separation of water and organic solvent mixtures.
因此,急需研发一种结构简单、适合水和有机溶剂连续分离的装置。Therefore, there is an urgent need to develop a device with a simple structure and suitable for continuous separation of water and organic solvents.
实用新型内容Utility model content
针对现有技术中的缺陷,本实用新型的目的是提供一种用于水和有机溶剂自动分离的装置。Aiming at the defects in the prior art, the purpose of this utility model is to provide a device for automatic separation of water and organic solvents.
本实用新型的目的是通过以下技术方案实现的:The purpose of this utility model is achieved by the following technical solutions:
本实用新型提供了一种用于水和有机溶剂自动分离的装置,包括储液容器、液体流入管和界面浮球液位计;所述液体流入管伸入至储液容器底部,所述储液容器侧壁设置有下层液体排放口和上层液体溢流口;所述界面浮球液位计设置在储液容器上方,界面浮球液位计的浮球一端伸入储液容器内。The utility model provides a device for automatic separation of water and organic solvents, which comprises a liquid storage container, a liquid inflow pipe and an interface float level gauge; the liquid inflow pipe extends into the bottom of the liquid storage container, and the liquid storage The side wall of the liquid container is provided with a lower liquid discharge port and an upper liquid overflow port; the interface float level gauge is arranged above the liquid storage container, and one end of the float ball of the interface float level gauge extends into the liquid storage container.
优选地,所述液体流入管伸入至储液容器底部的一端距离储液容器底部50mm-150mm。Preferably, the end of the liquid inflow pipe extending into the bottom of the liquid storage container is 50mm-150mm away from the bottom of the liquid storage container.
优选地,所述界面浮球液位计的浮球密度介于水密度和有机溶剂密度之间。Preferably, the float density of the interface float level gauge is between the density of water and the density of organic solvent.
优选地,所述界面浮球液位计的浮球密度为水和有机溶剂的平均密度。由此可使浮球的高度处于分界液面处。Preferably, the float density of the interface float level gauge is the average density of water and organic solvent. The height of the float can thus be at the boundary liquid level.
优选地,所述上层液体溢流口的高度d1、储液容器高度d、下层液体排放口的高度d2之间的关系为:Preferably, the relationship between the height d 1 of the upper liquid overflow port, the height d of the liquid storage container, and the height d 2 of the lower liquid discharge port is:
0.9d≤d1<d,且d2<0.2d。0.9d≤d 1 <d, and d 2 <0.2d.
优选地,所述界面浮球液位计的探测高度为0-d3,其中d≤d3,更优选d=d3。Preferably, the detection height of the interface float level gauge is 0-d 3 , where d≤d 3 , more preferably d=d 3 .
优选地,所述界面浮球液位计的一侧设置有液位变送器,所述下层液体排放口处设置有阀门。Preferably, a liquid level transmitter is provided on one side of the interface float level gauge, and a valve is provided at the lower liquid discharge port.
优选地,所述液位变送器与阀门通过导线连接。Preferably, the liquid level transmitter is connected to the valve through wires.
优选地,所述上层溶液溢流口和下层液体排放口分别设置在不同的侧面。Preferably, the upper layer solution overflow port and the lower layer liquid discharge port are respectively arranged on different sides.
优选地,所述界面液位d4在0.5d1≤d4<d1范围时,阀门打开;当界面液面d4在d2<d4<0.5d1范围时,阀门关闭。Preferably, when the interface liquid level d 4 is in the range of 0.5d 1 ≤ d 4 <d 1 , the valve is opened; when the interface liquid level d 4 is in the range of d 2 <d 4 <0.5d 1 , the valve is closed.
本实用新型的分离装置的使用方法如下:将含有有机溶剂的工业废水经液体流入管流入储液容器中,水和有机溶剂由于不相溶而分层,形成两相的分界液面,将界面浮球液位计插入混合溶液中,当液位变送器探测浮球高度为0.5d1~d1时,阀门打开,分解液面下层的溶液从下层液体排放口排出,分界液面上层溶液到达上层液体溢流口高度时,上层溶液从上层液体溢流口流出;当液位变送器探测浮球高度为d2~0.5d1时,阀门关闭,下层溶液不流出,分界液面上层溶液到达上层液体溢流口高度时,上层溶液从上层液体溢流口流出。由此,混合溶液中的水和有机溶剂得到有效分离。The use method of the separation device of the present utility model is as follows: the industrial wastewater containing organic solvent flows into the liquid storage container through the liquid inflow pipe, and the water and the organic solvent are layered due to immiscibility, forming a two-phase boundary liquid surface, and the interface The float level gauge is inserted into the mixed solution. When the liquid level transmitter detects that the height of the float is 0.5d 1 ~d 1 , the valve opens, and the solution in the lower layer of the decomposed liquid surface is discharged from the discharge port of the lower layer liquid, and the upper layer solution on the boundary liquid surface When the height of the upper liquid overflow port is reached, the upper liquid solution flows out from the upper liquid overflow port; when the liquid level transmitter detects that the height of the float is d 2 ~ 0.5d 1 , the valve is closed, the lower layer solution does not flow out, and the upper layer on the boundary liquid surface When the solution reaches the height of the upper liquid overflow port, the upper layer solution flows out from the upper liquid overflow port. Thus, water and organic solvents in the mixed solution are effectively separated.
与现有技术相比,本实用新型具有如下的有益效果:Compared with the prior art, the utility model has the following beneficial effects:
1、本实用新型的水和有机溶剂分离装置,通过浮球界面液位计和液位变送器对分离界面的探测,并根据探测液位的高度,控制阀门的开关,实现有机溶剂和废水的有效分离和自控排放,减少工作量,降低加工成本。1. The water and organic solvent separation device of the present utility model detects the separation interface through the float interface liquid level gauge and liquid level transmitter, and controls the switch of the valve according to the height of the detected liquid level to realize the separation of organic solvents and waste water. Effective separation and self-controlled discharge, reducing workload and processing costs.
2、本实用新型结构简单,分离效果好,适用于工业废水中不溶于水的有机溶剂的分离。2. The utility model has simple structure and good separation effect, and is suitable for the separation of water-insoluble organic solvents in industrial waste water.
附图说明Description of drawings
通过阅读参照以下附图对非限制性实施例所作的详细描述,本实用新型的其它特征、目的和优点将会变得更明显:Other features, objects and advantages of the present invention will become more apparent by reading the detailed description of non-limiting embodiments with reference to the following drawings:
图1为本实用新型的结构示意图;Fig. 1 is the structural representation of the utility model;
其中:1、储液容器;2、液体流入管;3、上层液体溢流口;4、下层液体排放口;5、阀门;6、界面浮球液位计;7、液位变送器。Among them: 1. Liquid storage container; 2. Liquid inflow pipe; 3. Upper liquid overflow port; 4. Lower liquid discharge port; 5. Valve; 6. Interface float level gauge; 7. Liquid level transmitter.
具体实施方式detailed description
下面结合具体实施例对本实用新型进行详细说明。以下实施例将有助于本领域的技术人员进一步理解本实用新型,但不以任何形式限制本实用新型。应当指出的是,对本领域的普通技术人员来说,在不脱离本实用新型构思的前提下,还可以做出若干变化和改进。这些都属于本实用新型的保护范围。The utility model is described in detail below in conjunction with specific embodiments. The following examples will help those skilled in the art to further understand the utility model, but do not limit the utility model in any form. It should be noted that those skilled in the art can make several changes and improvements without departing from the concept of the present utility model. These all belong to the protection domain of the present utility model.
本实用新型提供了一种用于水和有机溶剂自动分离的装置,如图1所示,包括储液容器1、液体流入管2和界面浮球液位计6;所述液体流入管2伸入至储液容器1底部,所述储液容器1侧壁设置有下层液体排放口4和上层液体溢流口3;所述界面浮球液位计6设置在储液容器1上方,界面浮球液位计6的浮球一端伸入储液容器1内。The utility model provides a device for automatic separation of water and organic solvents, as shown in Figure 1, comprising a liquid storage container 1, a liquid inflow pipe 2 and an interface float level gauge 6; the liquid inflow pipe 2 extends into the bottom of the liquid storage container 1, the side wall of the liquid storage container 1 is provided with a lower liquid discharge port 4 and an upper liquid overflow port 3; the interface float level gauge 6 is arranged above the liquid storage container 1, and the interface float One end of the floating ball of the ball level gauge 6 extends into the liquid storage container 1 .
所述液体流入管2伸入至储液容器1底部的一端距离储液容器1底部50mm-150mm。One end of the liquid inflow pipe 2 extending into the bottom of the liquid storage container 1 is 50mm-150mm away from the bottom of the liquid storage container 1 .
所述界面浮球液位计6的浮球密度介于水密度和有机溶剂密度之间。The float density of the interface float level gauge 6 is between the density of water and the density of organic solvent.
所述界面浮球液位计6的浮球密度为水和有机溶剂的平均密度。The float density of the interface float level gauge 6 is the average density of water and organic solvent.
所述上层液体溢流口3的高度d1、储液容器高度d、下层液体排放口4的高度d2之间的关系为:The relationship between the height d 1 of the upper liquid overflow port 3, the height d of the liquid storage container, and the height d 2 of the lower liquid discharge port 4 is:
0.9d≤d1<d,且d2<0.2d。0.9d≤d 1 <d, and d 2 <0.2d.
所述界面浮球液位计6的探测高度为0-d3,其中d≤d3,更优选d=d3。The detection height of the interface float level gauge 6 is 0-d 3 , where d≤d 3 , more preferably d=d 3 .
所述界面浮球液位计6的一侧设置有液位变送器7,所述下层液体排放口4处设置有阀门5。A liquid level transmitter 7 is provided on one side of the interface float level gauge 6 , and a valve 5 is provided at the lower liquid discharge port 4 .
所述液位变送器7与阀门5通过导线连接。The liquid level transmitter 7 is connected with the valve 5 through wires.
所述上层溶液溢流口3和下层液体排放口4分别设置在不同的侧面。The upper layer solution overflow port 3 and the lower layer liquid discharge port 4 are respectively arranged on different sides.
所述界面液位d4在0.5d1≤d4<d1范围时,控制阀门打开;当界面液面d4在d2<d4<0.5d1范围时,阀门关闭。When the interface liquid level d 4 is in the range of 0.5d 1 ≤ d 4 <d 1 , the control valve is opened; when the interface liquid level d 4 is in the range of d 2 <d 4 <0.5d 1 , the valve is closed.
实施例Example
本实施例提供了一种用于分离有机溶剂的装置,用于分离工业废水中不溶于水的有机溶剂,包括储液容器1、液体流入管2和界面浮球液位计6;所述液体流入管2伸入至储液容器1底部,所述储液容器1侧壁设置有下层液体排放口4和上层液体溢流口3;所述界面浮球液位计6设置在储液容器1上方,界面浮球液位计6的浮球一端伸入储液容器1内。This embodiment provides a device for separating organic solvents, which is used to separate water-insoluble organic solvents in industrial wastewater, including a liquid storage container 1, a liquid inflow pipe 2 and an interface float level gauge 6; the liquid The inflow pipe 2 extends into the bottom of the liquid storage container 1, and the side wall of the liquid storage container 1 is provided with a lower liquid discharge port 4 and an upper liquid overflow port 3; the interface float level gauge 6 is arranged on the liquid storage container 1 Above, one end of the floating ball of the interface float level gauge 6 extends into the liquid storage container 1 .
所述液体流入管2伸入至储液容器1底部的一端距离储液容器1底部50mm-150mm。One end of the liquid inflow pipe 2 extending into the bottom of the liquid storage container 1 is 50mm-150mm away from the bottom of the liquid storage container 1 .
所述废水密度ρ1=1.020g/cm3,有机溶剂密度ρ2=0.820g/cm3,浮球液位计6的浮球密度ρ=0.920g/cm3。The density of the wastewater ρ 1 =1.020g/cm 3 , the density of the organic solvent ρ 2 =0.820g/cm 3 , and the density of the float of the float level gauge 6 =0.920g/cm 3 .
所述上层液体溢流口3的高度d1为800mm、储液容器高度d为1000mm、下层液体排放口4的高度d2为100mm.。The height d 1 of the upper liquid overflow port 3 is 800 mm, the height d of the liquid storage container is 1000 mm, and the height d 2 of the lower liquid discharge port 4 is 100 mm.
所述界面浮球液位计的探测高度为0-1000mm。The detection height of the interface float level gauge is 0-1000mm.
所述界面浮球液位计6的一侧设置有液位变送器7,所述下层液体排放口4处设置有阀门5。A liquid level transmitter 7 is provided on one side of the interface float level gauge 6 , and a valve 5 is provided at the lower liquid discharge port 4 .
所述液位变送器7与阀门5通过导线连接。The liquid level transmitter 7 is connected with the valve 5 through wires.
所述上层溶液溢流口3和下层液体排放口4分别设置在不同的侧面。The upper layer solution overflow port 3 and the lower layer liquid discharge port 4 are respectively arranged on different sides.
所述界面液位d4在700mm时,阀门5打开;当界面液位d4在300mm时,阀门5关闭。When the interface liquid level d4 is 700mm, the valve 5 is opened; when the interface liquid level d4 is 300mm, the valve 5 is closed.
本实施例的装置工作过程如下:The working process of the device of this embodiment is as follows:
首先将混和有有机溶剂的工业废水通过有机溶剂混合物的液体流入管2注入储液容器1,由于废水中的有机溶剂与废水密度不同(本实施例废水密度大于有机溶剂密度),有机溶剂上浮,废水下沉形成分界面,分离后有机溶剂从上层液体的溢流口3溢流排出;随着废水有机溶剂的混合物的持续注入,废水液位逐渐升高,推动界面浮球液位计6浮球上升,当废水液位达到700mm高度时,界面浮球液位计6浮球同时达到700mm,液位变送器7输出信号,打开下层液体的底部排放口4上的阀门5,把废水排出;等废水液位排放到300mm是,界面浮球液位计6浮球同时达到800mm,液位变送器7输出信号,关闭下层液体排放口4上的阀门5。所述阀门为电磁阀。First, the industrial waste water mixed with the organic solvent is injected into the liquid storage container 1 through the liquid inflow pipe 2 of the organic solvent mixture. Since the density of the organic solvent in the waste water is different from that of the waste water (the density of the waste water in this embodiment is greater than that of the organic solvent), the organic solvent floats up. The wastewater sinks to form an interface, and after separation, the organic solvent overflows from the overflow port 3 of the upper liquid; with the continuous injection of the mixture of wastewater organic solvents, the wastewater liquid level gradually rises, pushing the interface float level gauge 6 to float. The ball rises, and when the waste water level reaches 700mm, the floating ball of the interface float level gauge 6 reaches 700mm at the same time, the liquid level transmitter 7 outputs a signal, and the valve 5 on the bottom discharge port 4 of the lower liquid is opened to discharge the waste water When the waste water level is discharged to 300mm, the floating ball of the interface float level gauge 6 reaches 800mm at the same time, the liquid level transmitter 7 outputs a signal, and the valve 5 on the lower liquid discharge port 4 is closed. The valve is a solenoid valve.
其中,本领域技术人员能够利用现有技术实现液位变送器和电磁阀,例如型号为MC1151的液位变送器和型号为OSA6305A的电磁阀。液位变送器和电磁阀连接在电路回路中,液位变送器输出的触发信号触发电磁阀打开或者关闭。Wherein, those skilled in the art can use the existing technology to realize the liquid level transmitter and the solenoid valve, for example, the liquid level transmitter of model MC1151 and the solenoid valve of model OSA6305A. The liquid level transmitter and the solenoid valve are connected in a circuit loop, and the trigger signal output by the liquid level transmitter triggers the solenoid valve to open or close.
本实用新型具有如下的有益效果:The utility model has the following beneficial effects:
1、本实用新型的水和有机溶剂分离装置,通过浮球界面液位计和液位变送器对分离界面的探测,并设置探测上下探测液位,实现有机溶剂和废水的有效分离和自控排放,减少工作量,降低加工成本。1. The water and organic solvent separation device of the present utility model detects the separation interface through the floating ball interface liquid level gauge and the liquid level transmitter, and sets up and down to detect the liquid level, so as to realize the effective separation and automatic control of the organic solvent and the waste water Emissions, reduce workload, reduce processing costs.
2、本实用新型结构简单,分离效果好,适用于工业废水中不溶于水的有机溶剂的分离。2. The utility model has simple structure and good separation effect, and is suitable for the separation of water-insoluble organic solvents in industrial waste water.
以上对本实用新型的具体实施例进行了描述。需要理解的是,本实用新型并不局限于上述特定实施方式,本领域技术人员可以在权利要求的范围内做出各种变化或修改,这并不影响本实用新型的实质内容。在不冲突的情况下,本申请的实施例和实施例中的特征可以任意相互组合。The specific embodiments of the present utility model have been described above. It should be understood that the utility model is not limited to the above-mentioned specific embodiments, and those skilled in the art may make various changes or modifications within the scope of the claims, which do not affect the essence of the utility model. In the case of no conflict, the embodiments of the present application and the features in the embodiments can be combined with each other arbitrarily.
Claims (9)
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| CN (1) | CN206228987U (en) |
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107860635A (en) * | 2017-10-30 | 2018-03-30 | 中国海洋石油总公司 | Rock core displacement device for washing oil and method |
| CN108421281A (en) * | 2018-03-30 | 2018-08-21 | 湖南凯美特气体股份有限公司 | A kind of device for the two phase stratification liquid being discharged in the container of on-line operation |
| CN109126206A (en) * | 2018-09-29 | 2019-01-04 | 任少虎 | A kind of mixing liquid separation method and device |
| CN111013196A (en) * | 2019-11-28 | 2020-04-17 | 中材锂膜有限公司 | Liquid level control device for dichloromethane condensate layering tank |
| CN113069793A (en) * | 2021-03-19 | 2021-07-06 | 楚天华通医药设备有限公司 | Liquid separation device and liquid separation system |
| CN115671792A (en) * | 2022-11-21 | 2023-02-03 | 山东爱地高分子材料有限公司 | Automatic draining device |
| CN116903171A (en) * | 2023-07-14 | 2023-10-20 | 河北铭万精细化工有限公司 | Multicomponent chemical wastewater treatment device |
| CN117232612A (en) * | 2022-06-07 | 2023-12-15 | 时代思康新材料有限公司 | Device for boundary position measurement and boundary position measurement method |
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2016
- 2016-12-06 CN CN201621330229.2U patent/CN206228987U/en not_active Expired - Fee Related
Cited By (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107860635A (en) * | 2017-10-30 | 2018-03-30 | 中国海洋石油总公司 | Rock core displacement device for washing oil and method |
| CN107860635B (en) * | 2017-10-30 | 2024-02-06 | 中国海洋石油总公司 | Core flooding oil washing device and method |
| CN108421281A (en) * | 2018-03-30 | 2018-08-21 | 湖南凯美特气体股份有限公司 | A kind of device for the two phase stratification liquid being discharged in the container of on-line operation |
| CN109126206A (en) * | 2018-09-29 | 2019-01-04 | 任少虎 | A kind of mixing liquid separation method and device |
| CN111013196A (en) * | 2019-11-28 | 2020-04-17 | 中材锂膜有限公司 | Liquid level control device for dichloromethane condensate layering tank |
| CN113069793A (en) * | 2021-03-19 | 2021-07-06 | 楚天华通医药设备有限公司 | Liquid separation device and liquid separation system |
| CN113069793B (en) * | 2021-03-19 | 2024-10-18 | 楚天华通医药设备有限公司 | Liquid separation device and liquid separation system |
| CN117232612A (en) * | 2022-06-07 | 2023-12-15 | 时代思康新材料有限公司 | Device for boundary position measurement and boundary position measurement method |
| CN115671792A (en) * | 2022-11-21 | 2023-02-03 | 山东爱地高分子材料有限公司 | Automatic draining device |
| CN116903171A (en) * | 2023-07-14 | 2023-10-20 | 河北铭万精细化工有限公司 | Multicomponent chemical wastewater treatment device |
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| CF01 | Termination of patent right due to non-payment of annual fee |
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