CN203577382U - Flowing liquid wall-washing recoilless filter - Google Patents
Flowing liquid wall-washing recoilless filter Download PDFInfo
- Publication number
- CN203577382U CN203577382U CN201320823034.1U CN201320823034U CN203577382U CN 203577382 U CN203577382 U CN 203577382U CN 201320823034 U CN201320823034 U CN 201320823034U CN 203577382 U CN203577382 U CN 203577382U
- Authority
- CN
- China
- Prior art keywords
- inlet
- outlet
- cavity
- underflow
- overflow
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
Links
- 239000007788 liquid Substances 0.000 title claims abstract description 34
- 238000005406 washing Methods 0.000 title claims abstract description 9
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 34
- 238000005192 partition Methods 0.000 claims abstract description 4
- 238000007789 sealing Methods 0.000 claims abstract description 4
- 238000001914 filtration Methods 0.000 abstract description 10
- 238000000034 method Methods 0.000 abstract description 9
- 235000019476 oil-water mixture Nutrition 0.000 abstract description 7
- 238000000926 separation method Methods 0.000 abstract description 7
- 230000000694 effects Effects 0.000 abstract description 4
- 238000011001 backwashing Methods 0.000 abstract description 2
- 235000019198 oils Nutrition 0.000 description 11
- 239000000463 material Substances 0.000 description 8
- 239000010865 sewage Substances 0.000 description 6
- 239000011148 porous material Substances 0.000 description 3
- 238000003756 stirring Methods 0.000 description 3
- 101000573151 Arabidopsis thaliana Probable pectinesterase 8 Proteins 0.000 description 2
- 238000004140 cleaning Methods 0.000 description 2
- 101001094837 Arabidopsis thaliana Pectinesterase 5 Proteins 0.000 description 1
- 240000007049 Juglans regia Species 0.000 description 1
- 235000009496 Juglans regia Nutrition 0.000 description 1
- 101710113246 Pectinesterase 3 Proteins 0.000 description 1
- 239000006004 Quartz sand Substances 0.000 description 1
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000004891 communication Methods 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000000835 fiber Substances 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000011259 mixed solution Substances 0.000 description 1
- 229920000642 polymer Polymers 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
- 235000020234 walnut Nutrition 0.000 description 1
Landscapes
- Cyclones (AREA)
Abstract
一种来液洗壁无反冲过滤器。主要为了解决现有油水混合液的过滤分离设备需要不断进行反冲洗以至于影响分离效率、增加了分离成本的问题。其特征在于:在罐体的左、右两端分别开有溢流腔出口和底流总出口,在溢流腔出口和底流总出口之间通过三块圆形密封隔板将所述罐体内腔分隔为四个彼此不连通的腔体,在入口腔的罐体侧壁上开有总进口,由左至右贯穿滤后水收集腔固定有一根采用微孔管做成的旋流器锥管,旋流器锥管顶端的入口盘上开有与旋流器锥管入口段圆弧面相切的切向入口,旋流器锥管尾端的底流口则位于底流水出口腔内;溢流口贯穿入口盘而固定在旋流器锥管的顶部。本种过滤器可利用来液对过滤体进行自清洗,不用反冲工艺,并且分离效果好。
A wall-washing non-backflush filter for incoming liquid. The main purpose is to solve the problem that the existing oil-water mixture filtration and separation equipment needs to be continuously backwashed so that the separation efficiency is affected and the separation cost is increased. It is characterized in that: the left and right ends of the tank body are respectively provided with an overflow chamber outlet and an underflow main outlet, and the inner chamber of the tank is sealed by three circular sealing partitions between the overflow chamber outlet and the underflow main outlet. Divided into four chambers that are not connected to each other, there is a general inlet on the side wall of the tank body of the inlet, and a cyclone cone made of microporous pipe is fixed through the filtered water collection chamber from left to right , the inlet disk at the top of the cyclone cone tube is provided with a tangential inlet tangent to the arc surface of the inlet section of the cyclone cone tube, and the underflow port at the tail end of the cyclone cone tube is located in the underflow water outlet; the overflow port Affixed to the top of the cyclone cone through the inlet disk. This kind of filter can use incoming liquid to self-clean the filter body, without backwashing process, and has good separation effect.
Description
技术领域 technical field
本实用新型涉及一种应用于油水混合液分离领域中的过滤分离器。 The utility model relates to a filter separator used in the field of oil-water mixture separation.
背景技术 Background technique
目前适用于油水混合液的过滤分离设备有很多种形式,如石英砂双向过滤器、射流搅拌过滤器、纤维球过滤器、核桃壳过滤器等。但是,经过长时间的使用后,发现这些过滤器都有一些问题,那就是必须滤料,而且必须有反冲洗工艺。否则过滤一段时间,不会超过48小时,滤后水就不能达到过滤前预期的指标要求。另一方面,这些常规形式的过滤器一方面需要反冲搅拌电机,增加了耗能元件,同时在反冲搅拌过程中,存在滤料泄漏问题。 At present, there are many forms of filtration and separation equipment suitable for oil-water mixtures, such as quartz sand two-way filters, jet stirring filters, fiber ball filters, walnut shell filters, etc. However, after a long period of use, it is found that these filters have some problems, that is, the filter material must be used, and there must be a backwashing process. Otherwise, after filtering for a period of time, it will not exceed 48 hours, and the filtered water cannot meet the expected index requirements before filtering. On the other hand, these conventional filters require a recoil stirring motor on the one hand, which increases energy consumption elements, and at the same time, there is a problem of filter material leakage during the recoil stirring process.
发明内容 Contents of the invention
为了解决背景技术中所提到的技术问题,本实用新型提供一种来液洗壁无反冲过滤器,该种过滤器可利用来液对过滤体进行自清洗,不用反冲工艺,并且分离效果好。 In order to solve the technical problems mentioned in the background technology, the utility model provides a non-recoil filter for incoming liquid washing wall, which can use incoming liquid to self-clean the filter body without backflushing process, and separate The effect is good.
本实用新型的技术方案是:该种来液洗壁无反冲过滤器,其主体为一个左、右端面均为圆弧面的罐体,其独特之处在于:在罐体的左、右两端分别开有溢流腔出口和底流总出口,在溢流腔出口和底流总出口之间通过三块圆形密封隔板将所述罐体内腔分隔为四个腔体,分别为溢流腔、入口腔、滤后水收集腔和底流水出口腔;其中,在入口腔的罐体侧壁上开有总进口,由左至右贯穿滤后水收集腔固定有一根采用微孔管做成的旋流器锥管,旋流器锥管顶端的入口盘固定于入口腔中,入口盘上开有与旋流器锥管入口段圆弧面相切的切向入口,旋流器锥管尾端的底流口则位于底流水出口腔内;溢流口贯穿入口盘而固定在旋流器锥管的顶部,溢流口的液流入口与旋流器锥管的内腔相连通,溢流口的液流出口与溢流腔相连通。 The technical scheme of the utility model is: this kind of incoming liquid washes the wall without recoil filter, and its main body is a tank body whose left and right end faces are arc-shaped. The two ends are respectively provided with an overflow chamber outlet and an underflow main outlet. Between the overflow chamber outlet and the underflow main outlet, the inner cavity of the tank is divided into four cavities by three circular sealing partitions. Cavity, inlet cavity, filtered water collection cavity and underflow water outlet cavity; among them, the main inlet is opened on the side wall of the tank body of the inlet cavity, and a microporous tube is fixed to run through the filtered water collection cavity from left to right. The formed cyclone cone tube, the inlet plate at the top of the cyclone cone tube is fixed in the inlet cavity, and the inlet plate is provided with a tangential inlet that is tangent to the arc surface of the inlet section of the cyclone cone tube, and the cyclone cone tube The underflow port at the tail end is located in the underflow water outlet cavity; the overflow port penetrates the inlet plate and is fixed on the top of the cyclone cone tube, the liquid flow inlet of the overflow port is connected with the inner cavity of the cyclone cone tube, and the overflow The liquid outlet of the mouth is in communication with the overflow chamber.
本实用新型具有如下有益效果:该种来液洗壁无反冲过滤器具有其它常规过滤器无法比拟的优点: A、来液对过滤体进行自清洗,不用反冲工艺;B、微孔管做成旋流器的锥体结构,可以使进入微孔管的油水混合液在旋流器腔体内进行部分分离,油相介质向腔体的中心运移,重质相水向边壁运移,使清洗壁面的混合液含油浓度大大降低;C、对于油田污水,特别是含聚污水或三元复合驱污水的处理提供了一种可靠的设备;D、易于操作等。同目前用的常规过滤器相比,具有过滤效率高;过滤效果好的特点。同时,来液洗壁无反冲过滤器运行工艺简单,工作可靠,无其它过滤器随时间而降低过滤效果的现象,也不存在更换滤料的问题。降低了制造成本。 The utility model has the following beneficial effects: the incoming liquid washes the wall without recoil filter and has the advantages that other conventional filters cannot match: A. The incoming liquid can self-clean the filter body without recoil process; B. The microporous tube Made into the cone structure of the cyclone, the oil-water mixture entering the microporous tube can be partially separated in the cyclone cavity, the oil phase medium migrates to the center of the cavity, and the heavy phase water migrates to the side wall , so that the oil concentration of the mixed solution for cleaning the wall surface is greatly reduced; C. It provides a reliable equipment for the treatment of oilfield sewage, especially sewage containing polymer or ASP flooding sewage; D. It is easy to operate and so on. Compared with conventional filters currently used, it has the characteristics of high filtration efficiency and good filtration effect. At the same time, the non-recoil filter for wall washing with incoming liquid has a simple operation process and reliable operation, and there is no phenomenon that other filters will reduce the filtering effect over time, and there is no problem of replacing the filter material. Manufacturing costs are reduced.
附图说明: Description of drawings:
图1是本实用新型的结构示意图。 Fig. 1 is the structural representation of the utility model.
图中1-溢流腔出口,2-溢流腔,3-总进口,4-入口腔,5-滤后水收集腔,6-旋流器锥管,7-底流水出口腔,8-底流总出口,9-底流口,10-收集腔出口,11-入口盘,12-溢流口。 In the figure 1- overflow cavity outlet, 2- overflow cavity, 3- total inlet, 4- inlet cavity, 5- filtered water collection cavity, 6- cyclone cone tube, 7- bottom flow water outlet cavity, 8- Underflow total outlet, 9-underflow port, 10-collection cavity outlet, 11-inlet plate, 12-overflow port.
具体实施方式: Detailed ways:
下面结合附图对本实用新型作进一步说明: Below in conjunction with accompanying drawing, the utility model is further described:
由图1所示,该种来液洗壁无反冲过滤器,其主体为一个左、右端面均为圆弧面的罐体,其独特之处在于:在罐体的左、右两端分别开有溢流腔出口1和底流总出口8,在溢流腔出口1和底流总出口8之间通过三块圆形密封隔板将所述罐体内腔分隔为四个腔体,分别为溢流腔2、入口腔4、滤后水收集腔5和底流水出口腔7;其中,在入口腔4的罐体侧壁上开有总进口3,由左至右贯穿滤后水收集腔5固定有一根采用微孔管做成的旋流器锥管6,旋流器锥管6顶端的入口盘11固定于入口腔4中,入口盘11上开有与旋流器锥管6入口段圆弧面相切的切向入口,旋流器锥管6尾端的底流口9则位于底流水出口腔7内;溢流口12贯穿入口盘11而固定在旋流器锥管6的顶部,溢流口12的液流入口与旋流器锥管6的内腔相连通,溢流口12的液流出口与溢流腔2相连通。另外,在滤后水收集腔5的下部开有收集腔出口10。 As shown in Fig. 1, this kind of incoming liquid washes the wall without recoil filter, and its main body is a tank body whose left and right end faces are arc-shaped. An overflow cavity outlet 1 and an underflow total outlet 8 are opened respectively, and the inner chamber of the tank is divided into four cavities by three circular sealing partitions between the overflow cavity outlet 1 and the underflow total outlet 8, which are respectively The overflow cavity 2, the inlet cavity 4, the filtered water collection cavity 5 and the underflow water outlet cavity 7; wherein, the main inlet 3 is opened on the side wall of the tank body of the inlet cavity 4, and runs through the filtered water collection cavity from left to right 5. A cyclone conical tube 6 made of a microporous tube is fixed. The inlet disk 11 at the top of the cyclone conical tube 6 is fixed in the entrance cavity 4. The inlet disk 11 is provided with the inlet of the cyclone conical tube 6. The tangential inlet of the circular arc surface is tangent, and the underflow port 9 at the tail end of the cyclone cone tube 6 is located in the underflow water outlet cavity 7; the overflow port 12 penetrates the inlet plate 11 and is fixed on the top of the cyclone cone tube 6, The liquid inlet of the overflow port 12 communicates with the inner cavity of the cyclone cone 6 , and the liquid outlet of the overflow port 12 communicates with the overflow chamber 2 . In addition, a collection chamber outlet 10 is opened at the lower part of the filtered water collection chamber 5 .
在本技术方案中,微孔管做成锥形旋流器锥体结构,其入口采用耐磨材料做成切向形式。当增压后的油水混合液进入切向入口时,液体在旋流器腔内高速旋转,旋转的液体清洗了过滤体(也就是旋流器壁——微孔管)内壁,阻止了油相介质对微孔的堵塞。同时旋转的液体在微孔管内外压差的作用下,液体中的水通过微孔管的微孔流出腔体体壁,从而实现了油水混合液的过滤,得到满足实践要求的合格水。旋流器溢流口排出高浓度的油水回到污水处理工艺前端,底流低浓度的含油污水返回到旋流器式过滤器前端的缓冲罐或缓冲池。 In this technical solution, the microporous tube is made into a cone structure of a conical cyclone, and its inlet is made of wear-resistant material in a tangential form. When the pressurized oil-water mixture enters the tangential inlet, the liquid rotates at high speed in the cyclone chamber, and the rotating liquid cleans the inner wall of the filter body (that is, the wall of the cyclone—microporous tube), preventing the oil phase Clogging of micropores by media. At the same time, the rotating liquid is under the action of the pressure difference inside and outside the microporous tube, and the water in the liquid flows out of the cavity wall through the micropores of the microporous tube, thereby realizing the filtration of the oil-water mixture and obtaining qualified water that meets the practical requirements. The high-concentration oily water discharged from the cyclone overflow port returns to the front end of the sewage treatment process, and the low-concentration oily sewage returns to the buffer tank or buffer pool at the front end of the cyclone filter.
使用时,油水混合液经来液管线从入口腔的总进口3进入来液洗壁无反冲过滤器入口腔4,在压力的作用下,经入口盘11的切向流道进入旋流器锥管6,旋流器锥管6材料由微孔管做成,选用材料代号为PE-3至PE-8的刚性微孔管。 When in use, the oil-water mixture enters the incoming liquid wall washing non-recoil filter inlet 4 through the incoming liquid pipeline from the general inlet 3 of the inlet port, and enters the cyclone through the tangential flow channel of the inlet plate 11 under the action of pressure Conical tube 6, the material of cyclone conical tube 6 is made of microporous tube, and the rigid microporous tube whose material code is PE-3 to PE-8 is selected for use.
由于混合液在旋流腔内产生高速旋转,因此液流经过旋流器的入口盘11后形成高速旋转的涡流。涡流在沿旋流体下行的过程中,高速的旋流转动又在锥体内得到加速,轻质相——油在离心力作用下运移到旋流体6的中心,形成油核,油核经溢流口12排至溢流腔2,由溢流出口排出;同时重质相——水被甩旋流器锥管6内边壁且继续向下运动,在清洗微孔管内壁的同时,一小部分沿旋流器锥管6的底流口9排至底流水出口腔7,最后由底流总出口8排出;另一大部分沿旋流器锥管6的管壁上的微孔排出至滤后水收集腔5,经过收集腔的出口10排出。 Due to the high-speed rotation of the mixed liquid in the swirl chamber, the liquid flow forms a high-speed rotating vortex after passing through the inlet plate 11 of the swirler. When the vortex flows down the swirl body, the high-speed swirl rotation is accelerated in the cone, and the light phase—oil moves to the center of the swirl body 6 under the action of centrifugal force, forming an oil nucleus, which is overflowed The port 12 is discharged to the overflow chamber 2, and discharged from the overflow outlet; at the same time, the heavy phase—water is thrown off the inner wall of the conical tube 6 of the cyclone and continues to move downward. While cleaning the inner wall of the microporous tube, a small Part of it is discharged along the bottom flow port 9 of the cyclone cone 6 to the bottom flow water outlet 7, and finally discharged from the bottom flow outlet 8; the other part is discharged along the micropores on the wall of the cyclone cone 6 to the post-filtration The water collecting chamber 5 is discharged through the outlet 10 of the collecting chamber.
从旋流分离的原理可知,溢流腔内液体中含油的浓度较高,底流水出口腔7中液体的含油浓度较低。因此溢流腔的液体在设备实际使用过程中可以返回到污水处理的前端工艺管线内,底流水出口腔的液体可返回到来液洗壁无反冲过滤器的入口端。来液洗壁无反冲过滤器滤后水收集腔经出口排出来的水,才是我们要求的过滤后的合格水。 It can be seen from the principle of cyclone separation that the oil concentration in the liquid in the overflow cavity is relatively high, and the oil concentration in the liquid in the underflow water outlet cavity 7 is relatively low. Therefore, the liquid in the overflow chamber can be returned to the front-end process pipeline of sewage treatment during the actual use of the equipment, and the liquid in the underflow water outlet can be returned to the inlet port of the incoming liquid wall washing non-backflushing filter. The incoming liquid washes the wall without recoil filter and the water discharged from the water collection chamber through the outlet is the qualified filtered water we require.
在使用过程中,处理介质含油浓度是不同的,但处理后的合格水却不受介质含油浓度的影响,因为过滤指标是由来液洗壁无反冲过滤器中的微孔管的孔径决定的。 During use, the oil concentration of the treatment medium is different, but the qualified water after treatment is not affected by the oil concentration of the medium, because the filtration index is determined by the pore size of the microporous tube in the wall-washing non-backflushing filter of the incoming liquid. .
试验证明,在来液含油1000~5000mg/L左右,来液洗壁无反冲过滤器分流比控制在60%左右时,旋流体材料选用PE-8,孔径在30~40微米时,滤后水中含油小于5mg/L;旋流体材料选用PE-5,孔径在80~64微米时,滤后水中含油小于10mg/L,旋流器压力损失约为0.40Mpa左右。 The test proves that when the oil content of the incoming liquid is about 1000-5000mg/L, and the split ratio of the incoming liquid wall washing non-recoil filter is controlled at about 60%, the material of the swirling fluid is PE-8, and the pore size is 30-40 microns. The oil content in the water is less than 5mg/L; the material of the cyclone is PE-5, and when the pore size is 80-64 microns, the oil content in the filtered water is less than 10mg/L, and the pressure loss of the cyclone is about 0.40Mpa.
Claims (1)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201320823034.1U CN203577382U (en) | 2013-12-13 | 2013-12-13 | Flowing liquid wall-washing recoilless filter |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201320823034.1U CN203577382U (en) | 2013-12-13 | 2013-12-13 | Flowing liquid wall-washing recoilless filter |
Publications (1)
Publication Number | Publication Date |
---|---|
CN203577382U true CN203577382U (en) | 2014-05-07 |
Family
ID=50575360
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201320823034.1U Expired - Fee Related CN203577382U (en) | 2013-12-13 | 2013-12-13 | Flowing liquid wall-washing recoilless filter |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN203577382U (en) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN106861296A (en) * | 2017-04-13 | 2017-06-20 | 中国石油大学(华东) | A kind of duct type NGL cyclone separator |
CN107261654A (en) * | 2017-07-05 | 2017-10-20 | 中国石油大学(华东) | A kind of two-stage duct type gas-liquid cyclone separator |
CN108079789A (en) * | 2017-12-21 | 2018-05-29 | 刘振民 | A kind of separation method and device of auto-flushing medium |
CN114132993A (en) * | 2022-01-10 | 2022-03-04 | 陕西雷光环保科技有限公司 | Centrifugal oil-water separation rod device |
-
2013
- 2013-12-13 CN CN201320823034.1U patent/CN203577382U/en not_active Expired - Fee Related
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN106861296A (en) * | 2017-04-13 | 2017-06-20 | 中国石油大学(华东) | A kind of duct type NGL cyclone separator |
CN106861296B (en) * | 2017-04-13 | 2019-02-12 | 中国石油大学(华东) | A pipeline type natural gas condensate liquid cyclone separator |
CN107261654A (en) * | 2017-07-05 | 2017-10-20 | 中国石油大学(华东) | A kind of two-stage duct type gas-liquid cyclone separator |
CN108079789A (en) * | 2017-12-21 | 2018-05-29 | 刘振民 | A kind of separation method and device of auto-flushing medium |
CN108079789B (en) * | 2017-12-21 | 2024-01-02 | 益可美(广州)生态科技有限责任公司 | Separation method and device for automatic flushing medium |
CN114132993A (en) * | 2022-01-10 | 2022-03-04 | 陕西雷光环保科技有限公司 | Centrifugal oil-water separation rod device |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
WO2022105698A1 (en) | Processing system and method for offshore gas field complex production fluid | |
CN105664538B (en) | A kind of multi-stage reducing spiral oil water separator | |
CN203577382U (en) | Flowing liquid wall-washing recoilless filter | |
CN110513062B (en) | Vehicular well-flushing liquid processing apparatus | |
CN200945382Y (en) | Liquid-liquid separation microporous cyclone filter | |
CN101259348A (en) | A gas-liquid-solid three-phase separator | |
CN202398157U (en) | Double-sleeve combined solid-liquid separator | |
CN202117635U (en) | Multistage self-circulation well flushing truck for oilfield water injection well | |
CN105833569A (en) | Outer rotational flow limited flow channel membrane separator and method for demulsifying emulsion membrane through same | |
CN107551615A (en) | Lamination cycle dynamic back-flushing filtering device and back-flushing method | |
CN205398327U (en) | Modularization oil -containing sewage treatment system | |
CN100457227C (en) | Rotational flow microporous filter | |
CN102166479A (en) | Improved antipollution membrane device | |
CN102861479B (en) | Self-cleaning cyclone compound precision sand remover | |
CN108862688A (en) | A kind of central tube cyclonic separation settler | |
CN108097060A (en) | A kind of ceramic membrane of good filtration effect | |
CN102698477B (en) | Filter | |
CN208414026U (en) | A kind of separation of Multi-stage spiral and filter device | |
CN204429515U (en) | A kind of hydrocyclone desander | |
CN209302989U (en) | A cyclone with filter function | |
CN103638733B (en) | Ceramic disc type filter | |
CN203634924U (en) | Ceramic disc type filter | |
CN104310527A (en) | Device and method for cyclone filter treatment of oily sludge | |
CN111762904A (en) | A high-efficiency cyclone multi-stage purification device for mine wastewater treatment | |
CN210683401U (en) | Cross-flow filtering type hydraulic cyclone structure |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20140507 Termination date: 20141213 |
|
EXPY | Termination of patent right or utility model |