CN201101907Y - Combined oil water separation device - Google Patents
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- 238000000926 separation method Methods 0.000 title claims abstract description 119
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 42
- 239000007788 liquid Substances 0.000 claims abstract description 64
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- 238000004519 manufacturing process Methods 0.000 abstract description 4
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- 235000019198 oils Nutrition 0.000 description 25
- 230000005484 gravity Effects 0.000 description 11
- 238000004062 sedimentation Methods 0.000 description 6
- 238000000034 method Methods 0.000 description 5
- 230000000694 effects Effects 0.000 description 4
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- 239000012528 membrane Substances 0.000 description 3
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Abstract
本实用新型涉及用于在陆上处理站及海上采油平台的复合式油水分离装置,包括分流器的进、出液口分别与水平总进液管、垂直管和下水平管连通;该垂直管与弯管连通;下水平管与螺旋管的输入端口连接,该螺旋管连入第四分离箱体,它与第二沉降分离箱体连通,其顶部通过中间管与第四沉降分离箱体顶部连通;在第四沉降分离箱体与入口对应的侧壁底部出口上安装水平排水管和在顶部安装水平排油管,该水平排油管一端从第三沉降分离箱体底部穿入,另一端口与第三沉降分离箱体底部出口固定;上水平管与第一螺旋管连通,第一螺旋管另一出口连入第三沉降分离箱体,第一和第三沉降分离箱体的底部和顶部侧壁之间连有管路;在2根水平排水管上通过三通分别安装出水管和出油管。
The utility model relates to a composite oil-water separation device used in land processing stations and offshore oil production platforms, which includes the inlet and outlet of the flow divider respectively communicated with the horizontal main liquid inlet pipe, the vertical pipe and the lower horizontal pipe; the vertical pipe It communicates with the elbow; the lower horizontal pipe is connected to the input port of the spiral pipe, and the spiral pipe is connected to the fourth separation box, which communicates with the second settling separation box, and its top is connected to the top of the fourth settling separation box through the middle pipe Connected; Install a horizontal drain pipe on the bottom outlet of the side wall corresponding to the entrance of the fourth settling separation box and install a horizontal oil drain pipe on the top. One end of the horizontal oil drain pipe penetrates from the bottom of the third settling separation box, and the other port is connected to The bottom outlet of the third settling separation box is fixed; the upper horizontal pipe communicates with the first spiral pipe, and the other outlet of the first spiral pipe is connected to the third settling separation box, the bottom and top sides of the first and third settling separation boxes Pipelines are connected between the walls; water outlet pipes and oil outlet pipes are respectively installed on the two horizontal drain pipes through tees.
Description
技术领域technical field
本实用新型涉及一种将油水两相混合液进行分离的装置和方法,特别是涉及一种应用在陆上及海上采油平台的复合式油水分离装置和分离系统和方法。The utility model relates to a device and method for separating oil-water two-phase mixed liquid, in particular to a composite oil-water separation device, separation system and method applied to land and sea oil production platforms.
背景技术Background technique
在许多行业,例如石化企业,油水分离设备是其重要生产设备。分离技术对行业发展至关重要。In many industries, such as petrochemical enterprises, oil-water separation equipment is an important production equipment. Separation technology is crucial to the development of the industry.
当前所采用的分离原理有:重力,离心,过滤,静电、破乳等,初期分离设备,一般均采用一种分离原理进行油水分离,近年来应用多种分离原理结合起来进行分离的设备是发展方向。例如专利公开号:CN2569538Y,一种高效油水分离器,描述的是一个主要采用重力分离原理的分离装置;中国科学院生态研究中心的发明专利一螺旋流道膜油水分离装置(专利公开号:CN1299693.A),采用了离心原理和膜技术结合起来进行分离的设备和方法。The separation principles currently used are: gravity, centrifugation, filtration, electrostatic, demulsification, etc. The initial separation equipment generally adopts one separation principle for oil-water separation. In recent years, the combination of multiple separation principles for separation equipment is the development direction. For example, the patent publication number: CN2569538Y, a high-efficiency oil-water separator, describes a separation device that mainly adopts the principle of gravity separation; the invention patent of the Ecological Research Center of the Chinese Academy of Sciences - a spiral channel membrane oil-water separation device (patent publication number: CN1299693. A), adopt the centrifugal principle and membrane technology to combine and separate the equipment and method.
在现实生产中,往往需要对大量的油水混合液进行快速分离,重力原理和膜技术都是有效的分离技术手段,但处理速度慢,因此导致设备结构复杂体、积庞大。In actual production, it is often necessary to quickly separate a large amount of oil-water mixture. Gravity principle and membrane technology are effective separation techniques, but the processing speed is slow, which leads to complex structure and bulky equipment.
发明内容Contents of the invention
本实用新型的目的是针对以上油水分离装置采用单一分离原理,在进行分离的过程中对于来液参数发生变化时,处理效率显著降低的缺点,从而提供一种采用离心、重力、膨胀等多种分离原理结合在一起的、将分流器、沉降分离箱和设计有螺旋管的沉降分离箱,通过管线组成的复合式油水分离装置,该系统是一种提高分离效率,处理量大;具有结构简单,减轻分离器重量的有效途径,既适合陆上油田,也适应海上油田。The purpose of this utility model is to solve the above oil-water separation device adopting a single separation principle. When the parameters of the incoming liquid change during the separation process, the processing efficiency is significantly reduced. Combining the separation principle, the splitter, the sedimentation separation box and the sedimentation separation box designed with a spiral tube are combined to form a composite oil-water separation device through pipelines. This system improves separation efficiency and has a large processing capacity; it has a simple structure , an effective way to reduce the weight of the separator, which is suitable for both onshore oilfields and offshore oilfields.
本实用新型的目的是这样实现的:The purpose of this utility model is achieved in that:
本实用新型提供的复合式油水分离装置,如图4所示,该系统包括第一分流器10、沉降分离箱和连接管线;其特征在于,分流器的进液口11、上出液口12和下出液口13分别与水平总进液管21、垂直管22和下水平管23连通;该垂直管22与弯管31和上水平管24依次连通;在所述的下水平管23和上水平管24之间,三根平行设置的垂直管22并联;所述的下水平管23与安装于第二沉降分离箱体602中的第二螺旋管502的输入端口连接,该第二螺旋管502的输出端口通过出液管552连入第四分离箱体604,该第二沉降分离箱体602底部通过一根中间管802与第四沉降分离箱体604底部连通,其顶部通过一根中间管804与第四沉降分离箱体604顶部连通;在第四沉降分离箱体604与入口对应的侧壁底部出口上安装水平排水管27,和在中部安装水平排油管28,该水平排油管28另一端从第三沉降分离箱体603中部穿入,并且该水平排水管27另一端口与第三沉降分离箱体603底部出口固定;所述的上水平管24的末端口与输送管线26连接,该输送管线26与第一沉降分离箱体601中的第一螺旋管501输入口连通,第一螺旋管501安装于沉降分离箱601内;该第一螺旋管501的另一出口通过出液管551连入第三沉降分离箱体603,第一沉降分离箱体601与第三沉降分离箱体603的底部和顶部侧壁之间连有第一管路801和第二管路803;在第三沉降分离箱体603与入口对应的侧壁底部出口与水平排水管27的另一端口连通;水平排油管28的高度低于第三沉降分离箱体603、第四沉降分离箱体604两箱体内溢流口150-300mm,水平排水管27的高度高于箱体底部100mm;在水平排水管27和水平排油管28上通过三通分别安装出水管81和出油管82,做为出水口和出油口。The composite oil-water separation device provided by the utility model, as shown in Figure 4, the system includes a
在上述的技术方案中,还包括第二分流器20,所述的上水平管24的末端口与第二分流器20的一端口连通,第二分流器20的另2个端口分别连接送油管25和输送管线26,该送油管25与第三沉降分离箱体603连通。通过连接第二分流器,可以加强油水分层,对含水率低的油进行更精细的分离。In the above technical solution, a
在上述的技术方案中,所述的分流器包括一本体,所述本体是三通管形结构的耐压容器,三通管的左侧管口11是进液口,三通管的右侧管口13是下出液口,三通管的上管口12是上出液口的耐压容器,在其内部的腔体内有一个水平设置的分流隔板16,该分流隔板将腔体分成上下两个空间,上层空间14与上出液口12相连通,下层空间15与下出液口13相连通,两层空间都与进液口11相连通,所述内腔直径和与进液口相连接的来液管的直径相等;所述的分流隔板位于三通管右侧管口一端的上方有将该管口上部封闭的堵头161;所述堵头朝向进液口一端的纵向截面为抛物线形;所述本体的中轴线至上出液口的高度H与分流器内腔半径r之比小于5;所述的本体内腔壁上有至少两组高度不相同的、并能分别与分流隔板的两个侧边相配合的条形槽;并且本体的进液口至水平出液口长度L与分流器内腔半径r之比小于10,所述的本体的每个管口处均设置有连接用法兰;参考图1A和图1B。In the above technical solution, the flow divider includes a body, the body is a pressure-resistant container with a three-way pipe structure, the
在上述的技术方案中,所述分流器的分流隔板的端部与所述进液口的端部相平齐。In the above technical solution, the end of the flow divider of the flow divider is flush with the end of the liquid inlet.
在上述的技术方案中,还包括3个阀门,该第一阀门41安装在所述的垂直管22上端口,阀门41另一端口与90度弯头底口31连接,弯头与上水平管24连接;其余两个阀门分别安装在其它两根垂直管22中。In the above-mentioned technical solution, three valves are also included, the
在上述的技术方案中,所述的垂直管管径d小于水平管管径D,垂直管长度H为15倍垂直管管径d,相邻垂直管间距S大于30倍水平管管径D。In the above technical solution, the diameter d of the vertical pipe is smaller than the diameter D of the horizontal pipe, the length H of the vertical pipe is 15 times the diameter d of the vertical pipe, and the distance S between adjacent vertical pipes is greater than 30 times the diameter D of the horizontal pipe.
在上述的技术方案中,所述的螺旋管包括螺旋管主体500为立式结构,该螺旋管主体500固定在螺旋管主体的支架90上,螺旋管主体500的螺旋管输入管51一端口安装输入管阀门42,螺旋管输入管55一端口安装输出管阀门43;总圈数为N,N==4-30;螺旋管主体500的螺旋管上部分有4圈为带孔段54,带孔段以下为封闭段52,带孔段的每一圈上开有圆孔70,所述的圆孔70从距离输出管55的出口1/4圆周处开始开孔,并且圆孔70均匀开在螺旋管的外侧,与水平线成α=45°夹角的位置,相邻两圈螺旋管上的圆孔70之间间隔半圈的螺旋管上不带圆孔;不带孔的螺旋管段为调整段,所述的调整段长度为1/2圆周;第二圈螺旋管所开圆孔70与第三圈所开圆孔70之间间隔半圈的螺旋管段。In the above technical solution, the spiral tube includes a spiral tube main body 500 as a vertical structure, the spiral tube main body 500 is fixed on the
在上述技术方案中,所述的螺旋管主体500的螺旋管回转半径为R,螺距为H,管内径为D1,管外径为D2,其设计参数遵循以下关系:
在上述技术方案中,所述的螺旋管主体500的螺旋管上的4圈带孔段54,从螺旋管上部自上到下3圈小孔的数目分别为n1、n2、n3,孔径分别为d1、d2、d3;圆孔的数目和孔径应遵循以下设计准则:n1≤n2≤n3,d1≤d2≤d3。In the above technical solution, the numbers of the 4 circles of
在上述技术方案中,本实用新型的沉降分离箱为圆形或方形金属容器,直径大于或等于1000mm,高度大于或等于1200mm;还包括在第一和第二沉降箱体中间设有垂直的隔板,该垂直隔板的两侧壁固定在沉降分离箱两侧壁上,把容器分隔为两部分,底部连通,上部空隙处为溢流口,容器进、出口管线分别设在垂直隔板两侧,垂直隔板的做用是减少来液对沉降分离的扰动,水可以在隔板下部连通流动,油通过溢流口由一侧进入到另一侧。所述的隔板的端部与所述进液口的端部相平齐。In the above technical solution, the settling separation box of the present invention is a circular or square metal container with a diameter greater than or equal to 1000mm and a height greater than or equal to 1200mm; it also includes a vertical partition between the first and second settling boxes The two side walls of the vertical partition are fixed on the two side walls of the settling separation box, which divides the container into two parts, the bottom is connected, and the upper gap is the overflow port. On the side, the function of the vertical partition is to reduce the disturbance of the incoming liquid on the settlement and separation, the water can flow in the lower part of the partition, and the oil enters from one side to the other through the overflow port. The end of the partition is flush with the end of the liquid inlet.
本实用新型的优点在于:The utility model has the advantages of:
本实用新型的利用离心、重力、膨胀复合原理的油水分离系统采用组合式分离构件,包括T形管、分流器、螺旋管,重力沉降分离箱体,各部分构件可以方便的进行组合调节,以达到最佳的分离状态。The oil-water separation system of the utility model using the combined principle of centrifugation, gravity and expansion adopts combined separation components, including T-shaped pipes, flow dividers, spiral pipes, and gravity settlement separation boxes. The components of each part can be combined and adjusted conveniently. to achieve the best separation state.
本实用新型的分离系统还采用带孔螺旋管分离器,该螺旋管分离器是一种新型的离心分离部件,在工艺允许的条件下应首先考虑减少回转半径,增加圈数来提高离心力,管壁开孔数量、大小和位置对于分离效率影响显著,通过实验和理论分析可以确定一个最佳方案。The separation system of the utility model also adopts a helical tube separator with holes, which is a new type of centrifugal separation component. Under the conditions allowed by the process, it should first consider reducing the radius of gyration and increasing the number of turns to improve the centrifugal force. The number, size and position of the wall openings have a significant impact on the separation efficiency, and an optimal scheme can be determined through experiments and theoretical analysis.
本实用新型的分离系统还采用具有膨胀和重力原理的预分效果的T型管部件,能起到气液预分的作用,作为进入螺旋管分离器的前置装备以达到良好的分离效果。The separation system of the utility model also adopts the T-shaped tube part with the pre-separation effect of the principle of expansion and gravity, which can play the role of gas-liquid pre-separation, and can be used as the pre-equipment of the spiral tube separator to achieve a good separation effect.
到目前为止,在国际和国内还没有发现这种复合式分离器,它在不同油品和油水配比条件下可以达到油中含水小于1%的分离效果。So far, no such composite separator has been found in the world and at home, and it can achieve the separation effect of less than 1% water in oil under different oil products and oil-water ratio conditions.
附图说明Description of drawings
图1是本发明的分流器结构正(a)、侧(b)视剖面图;Fig. 1 is front (a), side (b) cross-sectional view of flow divider structure of the present invention;
图2是本发明的T形管分离装置结构示意图;Fig. 2 is a schematic structural view of a T-shaped pipe separation device of the present invention;
图3是本发明的螺旋管结构示意图;Fig. 3 is a schematic diagram of the spiral tube structure of the present invention;
图4是本发明的复合式油水分离器结构示意图;Fig. 4 is the structural representation of composite oil-water separator of the present invention;
图5是本发明的另一种复合式油水分离器实施例示意图;Fig. 5 is another kind of composite oil-water separator embodiment schematic diagram of the present invention;
具体实施方式Detailed ways
下面结合附图和实施例对本实用新型进行详细地说明Below in conjunction with accompanying drawing and embodiment the utility model is described in detail
实施例1Example 1
参阅图1,制作第一分流器10和第二分流器20,分流器的本体是具有三通管形结构的耐压容器,其耐压容器上设有一个进液口11,三通管的左侧管口是进液口11,三通管的右侧管口是下出液口13,三通管的上管口是上出液口12;在其内部的腔体内有一个水平设置的分流隔板16将腔体分成上下两个空间,上腔14与上出液口12相连通,下腔15与下出液口(或水平出液口)13相连通,两层空间都与进液口相连通。所述的分流隔板的端部与所述进液口的端部相平齐。所述的分流隔板位于三通管右侧管口一端的上方有将该管口上部封闭的堵头161,该堵头朝向进液口一端的纵向截面为抛物线形。所述的三通管结构的分离器本体的每个管口处均设置有连接用法兰17。所述的分流器本体内腔壁上有三组高度不相同的并能分别与分流隔板的两个侧边相配合的条形槽。Referring to Fig. 1, make the
第一分流器10和第二分流器20的总长与内腔半径之L/r=8,分流腔体具有适当的容积,内腔长与半径之比l/r=5或6,高度与内腔半径之比分H/r=4,分流器内径与水平来液管21(参阅图3)内径相等。The total length of the
实施例2:Example 2:
参阅图1和图2,制作一个T形管分离装置:T形管分离装置也就是由水平总进液管21,上水平管24,下水平管23,垂直管22,分流器10(20)及阀门41组成。水平总进液管21连接来流管线,另一端与分流器10入口11连接,分流器上出口12与垂直管22连接,水平出口13与下水平管23连接,垂直管上端与阀门41连接,41另侧与90度弯头底口31连接,弯头与上水平管24连接。在上水平管24和下水平管23间有N根垂直管22并联,由此构成T形管分离装置。T形管至少有一根总进液管,一根垂直管,一根上水平管和一根下水平管组成,可以有多根垂直管。T形管上、下水平管管径为50mm,垂直管管径d小于水平管管径D,本实施例中管径为40mm。相邻垂直管间距S大于30倍水平管管径D。垂直管长度L为15倍垂直管管径d,本实施例为600mm。总进液管与第一根垂直管处可以不连接分流器,只使用三通管,或连接分流器,加强油水分层,例如本实施例。上水平管末端可不连接分流器,直接进入501螺旋管,也可以连接分流器,如本实施例。Referring to Fig. 1 and Fig. 2, make a T-shaped pipe separation device: T-shaped pipe separation device is exactly by horizontal total
实施例3Example 3
参阅图3,制作一个螺旋管分离器:螺旋管主体500为立式结构,该螺旋管主体500固定在螺旋管主体的支架90上,螺旋管主体500的螺旋管输入管51一端口安装输入管阀门42,螺旋管输入管55一端口安装输出管阀门43;总圈数为25,螺旋管主体500的螺旋管上部分有4圈为带孔段54,带孔段以下为封闭段52;从螺旋管上部自上到下3圈小孔的数目分别为n1、n2、n3,孔径分别为d1、d2、d3;圆孔的数目和孔径应遵循以下设计准则:n1≤n2≤n3,d1≤d2≤d3;带孔段的每一圈上开有圆孔70,所述的圆孔70从距离输出管55的出口1/4圆周处开始开孔,并且圆孔70均匀开在螺旋管的外侧,与水平线成α=45°夹角的位置,相邻两圈螺旋管上的圆孔70之间间隔半圈的螺旋管上不带圆孔;不带孔的螺旋管段为调整段,所述的调整段长度为1/2圆周;第二圈螺旋管所开圆孔70与第三圈所开圆孔70之间间隔半圈的螺旋管段。Referring to Fig. 3, make a spiral pipe separator: the spiral pipe main body 500 is a vertical structure, and the spiral pipe main body 500 is fixed on the support 90 of the spiral pipe main body, and the spiral pipe input pipe 51-port of the spiral pipe main body 500 is installed with the input pipe Valve 42, helical pipe input pipe 55 one port is installed output pipe valve 43; The total number of turns is 25, and the helical pipe upper part of helical pipe main body 500 has 4 circles to be band hole section 54, and the band hole section below is closed section 52; The number of small holes in the upper part of the spiral tube from top to bottom is n 1 , n 2 , n 3 , and the diameters are d 1 , d 2 , d 3 ; the number and diameter of round holes should follow the following design criteria: n 1 ≤n 2 ≤n 3 , d 1 ≤d 2 ≤d 3 ; a circular hole 70 is opened on each circle of the section with a hole, and the circular hole 70 is opened from the 1/4 circumference of the outlet of the output pipe 55 holes, and the round holes 70 are evenly opened on the outside of the spiral tube, at the position of an angle of α=45° with the horizontal line, and there is no round hole on the spiral tube between the round holes 70 on two adjacent turns of the spiral tube. The spiral pipe section without holes is the adjustment section, and the length of the adjustment section is 1/2 circle; the spiral pipe section with a half-circle interval between the
在本实施例中螺旋管主体500的螺旋管回转半径为R,螺距为H,管内径为D1,管外径为D2,其设计参数遵循以下关系:
其中R、D1、D2的取值在如下范围内最合适:150mm≤R≤200mm,20mm≤D1≤30mm、25mm≤D2≤35mm。Among them, the values of R, D 1 and D 2 are most suitable in the following ranges: 150mm≤R≤200mm, 20mm≤D 1 ≤30mm, 25mm≤D 2 ≤35mm.
实施例4Example 4
参阅图4,制作一由实施例1-3的分流器、T形管分离装置、螺旋管组成的复合式油水分离装置。Referring to Fig. 4, make a composite oil-water separation device consisting of the diverter of embodiment 1-3, the T-shaped pipe separation device, and the spiral pipe.
复合式分离器由第一分流器10的3个端口分别与水平总进液管21、垂直管22和下水平管23连通;该垂直管22与弯管31和上水平管24依次连通;在所述的下水平管23和上水平管24之间,三根平行设置的垂直管22并联;所述的下水平管23与安装于第二沉降分离箱体602中的第二螺旋管502的输入端口连接,该第二螺旋管502的输出端口通过出液管552连入第四分离箱体604,该第二沉降分离箱体602底部通过一根中间管802与第四沉降分离箱体604底部连通,顶部通过一根中间管804与第四沉降分离箱体顶部连通;在第四沉降分离箱体604与入口对应的侧壁底部管顶部还设有水平排水管27和水平排油管28;第四沉降分离箱体设有垂直隔板将出入口两侧分隔为两部分;所述的上水平管24的末端口与第二分流器20的一端口连通,第二分流器20的另2个端口分别连接送油管25和输送管线26,该送油管25与第三沉降分离箱体603连通,该输送管线26与第一沉降分离箱体601中的第一螺旋管501输入口连通,该第一螺旋管501安装于沉降分离箱601内,它的另一出口通过出液管551连入第三沉降分离箱体603,第一沉降分离箱体601与第三沉降分离箱体603的底部和顶部侧壁之间连有输水管801和输油管803;在第三沉降分离箱体603与入口对应的侧壁底部和中部还设有水平排水管27和水平排油管28;第三沉降分离箱体内的两侧上垂直固定隔板,该隔板将出入口两侧分隔为两部分,该隔板顶与第三沉降分离箱体内顶面之间的空隙为溢流口;水平排油管28的高度低于第三沉降分离箱体603、第四沉降分离箱体604两箱体内溢流口150-300mm,水平排水管27的高度高于箱体底部100mm;分别有输水管81和输油管82通过三通连接在水平排水管27和水平排油管28上,做为出水口和出油口。本实施例中上、下水平管管径为50mm,垂直管22管径d为40mm;垂直管长度H为600mm。两相邻的垂直管的距离为1500mm。所述的螺旋管主体500的螺旋管总圈数为20,封闭段52的圈数为16圈。The composite separator is communicated with the horizontal total liquid inlet pipe 21, the vertical pipe 22 and the lower horizontal pipe 23 by three ports of the first flow divider 10; Between the lower horizontal pipe 23 and the upper horizontal pipe 24, three parallel vertical pipes 22 are connected in parallel; Port connection, the output port of the second spiral tube 502 is connected to the fourth separation box 604 through the liquid outlet pipe 552, and the bottom of the second sedimentation separation box 602 is connected to the bottom of the fourth sedimentation separation box 604 through an intermediate pipe 802 Connected, the top communicates with the top of the fourth sedimentation separation box through an intermediate pipe 804; the top of the bottom pipe of the side wall corresponding to the entrance of the fourth sedimentation separation box 604 is also provided with a horizontal drain pipe 27 and a horizontal oil drain pipe 28; Four settling separation boxes are provided with vertical partitions to separate the two sides of the inlet and outlet into two parts; the end port of the upper horizontal pipe 24 communicates with a port of the second flow divider 20, and the other two ports of the second flow divider 20 Respectively connect the oil delivery pipe 25 and the delivery pipeline 26, the oil delivery pipe 25 communicates with the third settling separation box 603, the delivery pipeline 26 communicates with the input port of the first spiral pipe 501 in the first settling separation box 601, the first Spiral pipe 501 is installed in the settling separation box 601, and its other outlet is connected into the 3rd settling separation box 603 by outlet pipe 551, the bottom and the top of the first settling separation box 601 and the 3rd settling separation box 603 A water delivery pipe 801 and an oil delivery pipe 803 are connected between the side walls; a horizontal drainage pipe 27 and a horizontal oil discharge pipe 28 are also provided at the bottom and middle of the side wall corresponding to the entrance of the third settling separation box 603; Both sides are vertically fixed partitions, which divide the two sides of the inlet and outlet into two parts, and the gap between the top of the partition and the top surface in the third settling separation box is an overflow port; the height of the horizontal oil discharge pipe 28 is lower than The third settling separation box 603 and the fourth settling separation box 604 have an overflow port of 150-300 mm in the two boxes, and the height of the horizontal drain pipe 27 is 100 mm higher than the bottom of the box body; there are respectively a water delivery pipe 81 and an oil delivery pipe 82 connected by a tee On the horizontal drain pipe 27 and the horizontal oil drain pipe 28, it is used as a water outlet and an oil outlet. In this embodiment, the diameter of the upper and lower horizontal pipes is 50 mm, and the diameter d of the
实施例5Example 5
参阅图5,制做一本实用新型的油水分离系统。Referring to Fig. 5, make a utility model oil-water separation system.
本实施例与实施例4的不同点在于,采用一体化设计,将分流器、T形管、螺旋管和沉降分离箱体组合为一个整体结构,体积紧凑,重量轻,管线分布合理。本实施例本体是4个独立的箱体组合在一起形成一个整体密闭承压容器。T形管分离装置设置在本实施例容器的外侧或内部,长度为容器外周长的4分之3,作用是对油水进行初分;第一螺旋管501和第二螺旋管502分别处理第一分流器连接的上水平管24中的来液,和该第一分流器10的下水平管23来液,第一螺旋管501在第一沉降箱体601中,第二螺旋管502在第二沉降箱体602中,两个箱体内的液体不互相流通;经第一螺旋管501旋流离心分离处理后的液体通过551进入第三沉降分离箱体603继续进行重力分离;第一沉降箱体601与第三沉降箱体603间安装有溢流管803,管径为50mm,数量为6个,高度低于螺旋管开孔的最低位置,第一沉降箱体601上层的油可以通过溢流管进入第三沉降箱体603继续进行重力沉降;经螺旋管502旋流离心分离处理后的液体通过552进入沉降分离箱体604继续进行重力分离;第二沉降箱体602与第四沉降箱体604间安装有溢流管804,管径为50mm,数量为6个,高度低于螺旋管开孔的最低位置,第二沉降箱体602上层的油可以通过溢流管进入第四沉降箱体604继续进行重力沉降;上水平管的末端进入螺旋管前安装有第二分流器20,其上出液口通过管26直接进入第四沉降箱体604(也可以进入第三沉降箱体603)进行重力沉降分离;最终在第三沉降箱体603与第四沉降箱体604中得到含水率小于1%的油;水从容器底部开口引出。The difference between this embodiment and Embodiment 4 is that the integrated design is adopted, and the flow divider, T-shaped pipe, spiral pipe and settling separation box are combined into an overall structure, which is compact in size, light in weight, and the distribution of pipelines is reasonable. The main body of this embodiment is composed of four independent boxes to form an integral airtight pressure-bearing container. The T-shaped tube separation device is arranged on the outside or inside of the container of this embodiment, and the length is 3/4 of the outer circumference of the container, and its effect is to carry out preliminary separation of oil and water; the first
还可以再包括3个阀门,该第一阀门41安装在所述的垂直管22上端口,阀门41另一端口与90度弯头底口31连接,弯头与上水平管24连接;其余两个阀门分别安装在其它两根垂直管22中。It can also include 3 valves, the
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Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
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CN101411951B (en) * | 2007-10-17 | 2012-02-08 | 中国科学院力学研究所 | Oil-water separation system and method using centrifugal, gravity, and expansion composite principles |
CN103894003A (en) * | 2014-04-17 | 2014-07-02 | 国家电网公司 | Oil-water separating device for transformer accident oil reservoir |
CN104974928A (en) * | 2015-07-15 | 2015-10-14 | 重庆科技学院 | Fluid mixing tube for cell fluid experiment and use method of fluid mixing tube |
CN107253794A (en) * | 2017-07-28 | 2017-10-17 | 南京律智诚专利技术开发有限公司 | A kind of kitchen grease initial gross separation device |
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Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
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CN101411951B (en) * | 2007-10-17 | 2012-02-08 | 中国科学院力学研究所 | Oil-water separation system and method using centrifugal, gravity, and expansion composite principles |
CN103894003A (en) * | 2014-04-17 | 2014-07-02 | 国家电网公司 | Oil-water separating device for transformer accident oil reservoir |
CN103894003B (en) * | 2014-04-17 | 2016-01-20 | 国家电网公司 | A kind of application of oily-water seperating equipment of Accident of Transformer oil storage pool |
CN104974928A (en) * | 2015-07-15 | 2015-10-14 | 重庆科技学院 | Fluid mixing tube for cell fluid experiment and use method of fluid mixing tube |
CN104974928B (en) * | 2015-07-15 | 2017-11-21 | 重庆科技学院 | A kind of cell flow experiment mixed flow tube and application method |
CN107253794A (en) * | 2017-07-28 | 2017-10-17 | 南京律智诚专利技术开发有限公司 | A kind of kitchen grease initial gross separation device |
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