CN111825183A - A sewage treatment fluid control equipment - Google Patents
A sewage treatment fluid control equipment Download PDFInfo
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- CN111825183A CN111825183A CN202010700539.3A CN202010700539A CN111825183A CN 111825183 A CN111825183 A CN 111825183A CN 202010700539 A CN202010700539 A CN 202010700539A CN 111825183 A CN111825183 A CN 111825183A
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- 239000012530 fluid Substances 0.000 title claims abstract description 16
- 239000010865 sewage Substances 0.000 title claims abstract description 16
- 238000003756 stirring Methods 0.000 claims description 25
- 238000011144 upstream manufacturing Methods 0.000 claims description 13
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 13
- 230000000903 blocking effect Effects 0.000 claims description 10
- 238000007789 sealing Methods 0.000 claims description 10
- 239000007788 liquid Substances 0.000 claims description 6
- 238000000034 method Methods 0.000 description 10
- 238000005189 flocculation Methods 0.000 description 9
- 230000016615 flocculation Effects 0.000 description 9
- 238000010276 construction Methods 0.000 description 6
- 230000000694 effects Effects 0.000 description 5
- 238000010586 diagram Methods 0.000 description 4
- 239000003814 drug Substances 0.000 description 4
- 238000005516 engineering process Methods 0.000 description 4
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
- 239000003795 chemical substances by application Substances 0.000 description 2
- 239000000701 coagulant Substances 0.000 description 2
- 238000004062 sedimentation Methods 0.000 description 2
- 239000002689 soil Substances 0.000 description 2
- PWHULOQIROXLJO-UHFFFAOYSA-N Manganese Chemical compound [Mn] PWHULOQIROXLJO-UHFFFAOYSA-N 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 239000003673 groundwater Substances 0.000 description 1
- 230000002452 interceptive effect Effects 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- 229910052748 manganese Inorganic materials 0.000 description 1
- 239000011572 manganese Substances 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 238000005192 partition Methods 0.000 description 1
- 230000000717 retained effect Effects 0.000 description 1
- 239000002893 slag Substances 0.000 description 1
- 230000009466 transformation Effects 0.000 description 1
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/52—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities
- C02F1/5281—Installations for water purification using chemical agents
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F33/00—Other mixers; Mixing plants; Combinations of mixers
- B01F33/80—Mixing plants; Combinations of mixers
- B01F33/82—Combinations of dissimilar mixers
- B01F33/821—Combinations of dissimilar mixers with consecutive receptacles
- B01F33/8212—Combinations of dissimilar mixers with consecutive receptacles with moving and non-moving stirring devices
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F35/00—Accessories for mixers; Auxiliary operations or auxiliary devices; Parts or details of general application
- B01F35/20—Measuring; Control or regulation
- B01F35/22—Control or regulation
- B01F35/221—Control or regulation of operational parameters, e.g. level of material in the mixer, temperature or pressure
- B01F35/2211—Amount of delivered fluid during a period
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- E—FIXED CONSTRUCTIONS
- E21—EARTH OR ROCK DRILLING; MINING
- E21F—SAFETY DEVICES, TRANSPORT, FILLING-UP, RESCUE, VENTILATION, OR DRAINING IN OR OF MINES OR TUNNELS
- E21F16/00—Drainage
- E21F16/02—Drainage of tunnels
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- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Mining & Mineral Resources (AREA)
- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Organic Chemistry (AREA)
- General Chemical & Material Sciences (AREA)
- General Life Sciences & Earth Sciences (AREA)
- Geochemistry & Mineralogy (AREA)
- Geology (AREA)
- Accessories For Mixers (AREA)
Abstract
Description
技术领域technical field
本发明涉及隧洞工程排水领域,具体涉及一种污水处理流体控制设备。The invention relates to the field of tunnel engineering drainage, in particular to a sewage treatment fluid control device.
背景技术Background technique
现有技术的隧洞施工工程部分位于流域水环境敏感区,线路跨度大,强岩溶化地层范围广,水环境交互影响深远,其中存在的影响包括:隧洞排水对流域水环境的影响、隧洞建成后地表工程建设施工污水通过隧洞排水孔可能的渗漏影响、隧洞部分地段可能存在地下水铁锰超标影响;此外,由于工程施工渣场、施工场地等区域水土保持要求高。工程环境保护、水土保持要求高,也存在对隧洞施工工程的要求,因此隧洞施工中排水就变得尤为重要。The tunnel construction project of the prior art is partly located in the water environment sensitive area of the watershed, with a large line span, a wide range of strongly karstified strata, and a far-reaching interactive impact on the water environment. Surface engineering construction sewage may seepage through the tunnel drainage holes, and some sections of the tunnel may have the influence of excessive iron and manganese in groundwater; in addition, due to the high requirements for soil and water conservation in areas such as engineering construction slag yards and construction sites. Engineering environmental protection, soil and water conservation requirements are high, and there are also requirements for tunnel construction projects, so drainage in tunnel construction becomes particularly important.
现有技术隧洞排水方案的不足如下:The deficiencies of the prior art tunnel drainage schemes are as follows:
1、现有技术加药房对絮凝反应池通药时,由于絮凝反应池范围大,通药时难以对整个反应池进行均匀覆盖,从而难以起到均匀反应絮凝的效果。1. When adding medicine to the flocculation reaction tank in the prior art, due to the large scope of the flocculation reaction tank, it is difficult to uniformly cover the entire reaction tank when the medicine is poured, so that it is difficult to achieve the effect of uniform reaction and flocculation.
、现有技术加药房对絮凝反应池通药时,往往施加不止一种药剂,药剂充分混合后絮凝效果提升,然而现有技术往往是将两种药剂倒入一个反应罐里再混合,自动化程度差且流量控制繁琐。2. In the prior art, when the pharmacy is used to pass the medicine to the flocculation reaction tank, more than one agent is often applied, and the flocculation effect is improved after the agent is fully mixed. Poor and cumbersome flow control.
、现有技术加药房对絮凝反应池通药时,往往采用普通球阀对通流量进行控制,然而球阀的开度控制并不精准且不能定量,原因如下:球阀的阀口开度变换不是一个线性的变化,随着球阀转动,开口面积变化并不是线性递增/递减的,而是曲线或阶跃变化,因此虽然能控制开度大小和流量大小,并不能精量控制和定量控制。. In the prior art, when the pharmacy is used to pass the medicine to the flocculation reaction tank, the ordinary ball valve is often used to control the flow rate. However, the opening degree control of the ball valve is not accurate and cannot be quantified. The reasons are as follows: the valve opening of the ball valve is not a linear transformation. As the ball valve rotates, the change of the opening area is not linearly increasing/decreasing, but a curve or step change, so although the opening and flow can be controlled, it cannot be precisely controlled and quantitatively controlled.
、现有技术的单向阀,存在回位弹簧,使得压力不足以打开单向阀时关闭单向阀,然而这容易造成无法流出的液体残留,严重的会造成一定水击,而且液体残留的话对于精量控制也是一种损害。, The one-way valve of the prior art has a return spring, so that the one-way valve is closed when the pressure is not enough to open the one-way valve. However, this is easy to cause the residual liquid that cannot flow out, and in serious cases, it will cause a certain water hammer, and if the liquid remains It is also a detriment to precision control.
、现有技术的汇流,往往呈拉链式汇流,造成一定水击,影响设备寿命。. The confluence of the prior art is often in the form of a zipper confluence, which causes a certain water hammer and affects the life of the equipment.
、现有技术的旋流盘,汇流效果较弱,混合效果也相对比较弱。. The swirl disk of the prior art has a weak confluence effect and a relatively weak mixing effect.
发明内容SUMMARY OF THE INVENTION
为了克服上述问题,本发明提出同时解决上述多种问题的方案。In order to overcome the above-mentioned problems, the present invention proposes solutions to solve the above-mentioned various problems at the same time.
本发明解决其技术问题所采用的技术方案是:一种污水处理流体控制设备,包括:旋流盘、第一加药管、第二加药管、控制球阀、汇流锥管、搅拌杆、搅拌叶、漏斗、斜流通道、单向阀球、排流通道、封堵块、入流管、让位管头;其中所述控制球阀包括阀体、球体、阀杆、密封阀座、阀颈,所述球体包括小流量通道、大流量通道、第一区、第二区、第三区、第四区、第五区、第六区、第七区、第八区、所述大流量通道包括第一口、第二口,所述小流量通道包括第三口、第四口;The technical scheme adopted by the present invention to solve the technical problem is: a sewage treatment fluid control device, comprising: a swirl plate, a first dosing pipe, a second dosing pipe, a control ball valve, a converging cone pipe, a stirring rod, a stirring rod, a Leaf, funnel, oblique flow channel, one-way valve ball, discharge channel, blocking block, inflow pipe, yield pipe head; wherein the control ball valve includes a valve body, a sphere, a valve stem, a sealing valve seat, and a valve neck, The sphere includes a small flow channel, a large flow channel, a first area, a second area, a third area, a fourth area, a fifth area, a sixth area, a seventh area, and an eighth area. The large flow channel includes a first port and a second port, and the small flow channel includes a third port and a fourth port;
其中所述第一加药管和第二加药管的一部分平行设置,所述第一加药管和第二加药管中都设有所述控制球阀,所述旋流盘中包括螺旋通道;所述第一加药管与所述螺旋通道的外圈在第一位置连通,在螺旋通道的所述外圈第一位置下游位置的外侧设有所述汇流锥管,所述汇流锥管与所述第二加药管连通;Wherein the first dosing pipe and a part of the second dosing pipe are arranged in parallel, the control ball valve is provided in both the first dosing pipe and the second dosing pipe, and the swirl disk includes a spiral channel ; the first dosing pipe is communicated with the outer ring of the helical channel at a first position, and the confluence conical pipe is provided on the outside of the downstream position of the first position of the outer ring of the helical channel. communicated with the second dosing pipe;
所述旋流盘的中央下方设有所述漏斗,所述漏斗上方设置所述搅拌杆,所述搅拌杆下端设有所述搅拌叶;所述漏斗下方连接所述斜流通道,所述斜流通道下方连接所述入流管,所述入流管将液体排入下游,所述入流管的直径大于所述斜流通道的直径,所述单向阀球的直径大于所述斜流通道的直径,所述封堵块位于所述入流管中,所述封堵块中设有所述排流通道,所述入流管上方设有让位管头,让位管头一端封闭,所述让位管头包括倾斜段与水平段,所述倾斜段与所述斜流通道连通,所述水平段底部支撑面的长度小于所述单向阀球的直径;The funnel is provided under the center of the swirl plate, the stirring rod is provided above the funnel, and the stirring blade is provided at the lower end of the stirring rod; the oblique flow channel is connected below the funnel, and the oblique flow channel is The inflow pipe is connected to the bottom of the flow channel, the inflow pipe discharges the liquid into the downstream, the diameter of the inflow pipe is larger than the diameter of the oblique flow channel, and the diameter of the one-way valve ball is larger than the diameter of the oblique flow channel , the blocking block is located in the inflow pipe, the discharge channel is provided in the blocking block, the abdication pipe head is arranged above the inflow pipe, one end of the abdication pipe head is closed, and the abdication pipe head is The pipe head includes an inclined section and a horizontal section, the inclined section is communicated with the diagonal flow channel, and the length of the bottom support surface of the horizontal section is smaller than the diameter of the one-way valve ball;
所述控制球阀的阀体上设有所述阀颈,所述阀杆驱动所述球体转动,通过球体转动,球体表面等分为八个分区围绕球体中心转动,转动到关闭位置时,第一区、第二区面向上游构成封闭区阻断水流,当第二区、第三区面向上游时,所述第六区、第七区面向下游,其中所述第一口位于所述第三区,所述第二口位于所述第六区,当第四区、第五区面向上游时,第八区、第一区面向下游,所述第三口位于所述第四区,所述第四口位于所述第八区;其中所述小流量通道贯穿所述球体,所述大流量通道贯穿所述球体且位于所述小流量通道的下方;所述小流量通道为弧形通道。The valve body of the control ball valve is provided with the valve neck, and the valve stem drives the ball to rotate. Through the rotation of the ball, the surface of the ball is divided into eight divisions and rotates around the center of the ball. When it rotates to the closed position, the first The area and the second area face upstream to form a closed area to block water flow. When the second area and the third area face upstream, the sixth area and the seventh area face downstream, and the first port is located in the third area. , the second port is located in the sixth zone, when the fourth zone and the fifth zone face upstream, the eighth zone and the first zone face downstream, the third port is located in the fourth zone, the first zone The four ports are located in the eighth area; wherein the small flow channel penetrates the sphere, the large flow channel penetrates the sphere and is located below the small flow channel; the small flow channel is an arc-shaped channel.
进一步的,所述搅拌叶数量为四。Further, the number of the stirring blades is four.
进一步的,所述第二加药管包括相互垂直的两段。Further, the second dosing pipe includes two sections perpendicular to each other.
进一步的,所述阀颈与阀体为一体结构。Further, the valve neck and the valve body have an integral structure.
进一步的,所述球体的水平中心线穿过所述大流量通道的管壁。Further, the horizontal centerline of the sphere passes through the pipe wall of the large flow channel.
进一步的,所述密封阀座外侧设有补偿弹簧。Further, a compensation spring is provided outside the sealing valve seat.
进一步的,所述球体下侧设有下阀杆辅助驱动。Further, the lower side of the sphere is provided with a lower valve stem for auxiliary driving.
进一步的,所述球体的直径大于阀体管道的直径。Further, the diameter of the sphere is larger than the diameter of the valve body pipeline.
进一步的,球体表面的八个分区被密封阀座限定范围。Further, the eight subregions of the spherical surface are bounded by the sealing valve seat.
进一步的,所述旋流盘对应漏斗的位置上方开口以接纳所述搅拌叶。Further, the swirling disk is opened above the position corresponding to the funnel to receive the stirring blade.
本发明的有益效果是:The beneficial effects of the present invention are:
1、针对背景技术的第1点,在絮凝池中采用了旋转搅拌叶对助凝剂和混凝剂以及池水进行混合,提高了混合效率,加快了混合速度。1. In view of the first point of the background technology, a rotating stirring blade is used in the flocculation tank to mix the coagulant aid, the coagulant and the pool water, which improves the mixing efficiency and speeds up the mixing speed.
、针对背景技术的第2点,对两个加药管进行了汇流设计,汇流后在旋流盘中预备混合,在漏斗中经过旋流进行混合。. In view of the second point of the background art, the two dosing pipes are designed to be confluent. After the confluence, the mixing is prepared in the swirl plate, and the mixing is carried out through the swirl in the funnel.
、针对背景技术的第3点,对球阀表面进行了精细化设计,巧妙的仅仅凭借单个球阀的旋转就可以实现精确、定量的流量调整,且保留正常通断功能。. In view of the third point of the background technology, the surface of the ball valve is finely designed, and the precise and quantitative flow adjustment can be realized only by the rotation of a single ball valve, and the normal on-off function is retained.
、针对背景技术的第4点,设计了避免残留的步骤,通过斜流通道使得液体更容易迅速通过单向口,设计了让位管头可以实现短暂支撑,避免单向阀球迅速落下。. In view of the fourth point of the background technology, the steps to avoid residue are designed, the diagonal flow channel makes it easier and faster for the liquid to pass through the one-way port, and the design of the escape pipe head can achieve short-term support and prevent the one-way valve ball from falling rapidly.
、针对背景技术的第5点,设计了切向汇流方案,使得汇流的水击更小,汇流更均匀。. In view of the fifth point of the background art, a tangential confluence scheme is designed, so that the water hammer of the confluence is smaller and the confluence is more uniform.
、针对背景技术的第6点,设计了旋流盘、搅拌叶、汇流锥管等多个混合方案,大大提高了混合效果。. In view of the sixth point of the background technology, multiple mixing schemes such as swirl disc, stirring blade, converging conical tube, etc. are designed, which greatly improves the mixing effect.
注:上述设计不分先后,每一条都使得本发明相对现有技术具有区别和显著的进步。Note: The above designs are in no particular order, each of which makes the present invention different and significantly improved compared to the prior art.
附图说明Description of drawings
下面结合附图和实施例对本发明进一步说明。The present invention will be further described below with reference to the accompanying drawings and embodiments.
图1是本发明排水整流程示意图Fig. 1 is the schematic diagram of the drainage whole process of the present invention
图2是本发明旋流盘系统俯视图Fig. 2 is the top view of the swirl disk system of the present invention
图3是本发明汇流系统示意图Fig. 3 is the schematic diagram of the confluence system of the present invention
图4是本发明控制球阀结构图Fig. 4 is the structure diagram of the control ball valve of the present invention
图5是本发明球体分区示意图Fig. 5 is the schematic diagram of the sphere partition of the present invention
图中,附图标记如下:In the figure, the reference numerals are as follows:
1、预沉池2、絮凝反应池3、沉淀池4、加药房5、旋流盘6、第一加药管7、第二加药管8、控制球阀9、汇流锥管10、螺旋通道外圈11、搅拌杆12、搅拌叶13、漏斗14、斜流通道15、单向阀球16、排流通道17、封堵块18、入流管19、让位管头20、阀体21、球体22、阀杆23、阀颈24、小流量通道25、密封阀座26、大流量通道27、第一区28、第二区29、第三区30、第四区31、第五区32、第六区33、第七区34、第八区35、第一口36、第四口37、第三口38、第二口。1.
具体实施方式Detailed ways
如图所示:一种污水处理流体控制设备,包括:旋流盘、第一加药管、第二加药管、控制球阀、汇流锥管、搅拌杆、搅拌叶、漏斗、斜流通道、单向阀球、排流通道、封堵块、入流管、让位管头;其中所述控制球阀包括阀体、球体、阀杆、密封阀座、阀颈,所述球体包括小流量通道、大流量通道、第一区、第二区、第三区、第四区、第五区、第六区、第七区、第八区、所述大流量通道包括第一口、第二口,所述小流量通道包括第三口、第四口;As shown in the figure: a sewage treatment fluid control equipment, including: a swirl plate, a first dosing pipe, a second dosing pipe, a control ball valve, a converging cone, a stirring rod, a stirring blade, a funnel, an oblique flow channel, One-way valve ball, discharge channel, blocking block, inflow pipe, and yield pipe head; wherein the control ball valve includes a valve body, a ball, a valve stem, a sealing valve seat, and a valve neck, and the ball includes a small flow channel, Large flow channel, first area, second area, third area, fourth area, fifth area, sixth area, seventh area, eighth area, the large flow channel includes a first port and a second port, The small flow channel includes a third port and a fourth port;
其中所述第一加药管和第二加药管的一部分平行设置,所述第一加药管和第二加药管中都设有所述控制球阀,所述旋流盘中包括螺旋通道;所述第一加药管与所述螺旋通道的外圈在第一位置连通,在螺旋通道的所述外圈第一位置下游位置的外侧设有所述汇流锥管,所述汇流锥管与所述第二加药管连通;Wherein the first dosing pipe and a part of the second dosing pipe are arranged in parallel, the control ball valve is provided in both the first dosing pipe and the second dosing pipe, and the swirl disk includes a spiral channel ; the first dosing pipe is communicated with the outer ring of the helical channel at a first position, and the confluence conical pipe is provided on the outside of the downstream position of the first position of the outer ring of the helical channel. communicated with the second dosing pipe;
如图所示:所述旋流盘的中央下方设有所述漏斗,所述漏斗上方设置所述搅拌杆,所述搅拌杆下端设有所述搅拌叶;所述漏斗下方连接所述斜流通道,所述斜流通道下方连接所述入流管,所述入流管将液体排入下游,所述入流管的直径大于所述斜流通道的直径,所述单向阀球的直径大于所述斜流通道的直径,所述封堵块位于所述入流管中,所述封堵块中设有所述排流通道,所述入流管上方设有让位管头,让位管头一端封闭,所述让位管头包括倾斜段与水平段,所述倾斜段与所述斜流通道连通,所述水平段底部支撑面的长度小于所述单向阀球的直径;As shown in the figure: the funnel is provided under the center of the swirl plate, the stirring rod is provided above the funnel, and the stirring blade is provided at the lower end of the stirring rod; the bottom of the funnel is connected to the oblique flow The bottom of the diagonal flow channel is connected to the inflow pipe, the inflow pipe discharges the liquid into the downstream, the diameter of the inflow pipe is larger than that of the diagonal flow channel, and the diameter of the one-way valve ball is larger than that of the one-way valve ball. Diameter of the oblique flow channel, the blocking block is located in the inflow pipe, the draining channel is arranged in the blocking block, and the inflow pipe is provided with a side pipe head, and one end of the side pipe head is closed , the abdication pipe head comprises an inclined section and a horizontal section, the inclined section is communicated with the diagonal flow channel, and the length of the bottom support surface of the horizontal section is smaller than the diameter of the one-way valve ball;
如图所示:所述控制球阀的阀体上设有所述阀颈,所述阀杆驱动所述球体转动,通过球体转动,球体表面等分为八个分区围绕球体中心转动,转动到关闭位置时,第一区、第二区面向上游构成封闭区阻断水流,当第二区、第三区面向上游时,所述第六区、第七区面向下游,其中所述第一口位于所述第三区,所述第二口位于所述第六区,当第四区、第五区面向上游时,第八区、第一区面向下游,所述第三口位于所述第四区,所述第四口位于所述第八区;其中所述小流量通道贯穿所述球体,所述大流量通道贯穿所述球体且位于所述小流量通道的下方;所述小流量通道为弧形通道。As shown in the figure: the valve body of the control ball valve is provided with the valve neck, and the valve stem drives the ball to rotate. Through the rotation of the ball, the surface of the ball is divided into eight divisions and rotates around the center of the ball until it is closed. When in position, the first zone and the second zone face upstream to form a closed zone to block water flow. When the second zone and the third zone face upstream, the sixth zone and the seventh zone face downstream, and the first port is located at The third zone, the second port is located in the sixth zone, when the fourth zone and the fifth zone face upstream, the eighth zone and the first zone face downstream, and the third port is located in the fourth zone area, the fourth port is located in the eighth area; wherein the small flow channel penetrates the sphere, the large flow channel penetrates the sphere and is located below the small flow channel; the small flow channel is Arc channel.
如图所示:所述搅拌叶数量为四。所述第二加药管包括相互垂直的两段。所述阀颈与阀体为一体结构。所述球体的水平中心线穿过所述大流量通道的管壁。所述密封阀座外侧设有补偿弹簧。所述球体下侧设有下阀杆辅助驱动。所述球体的直径大于阀体管道的直径。球体表面的八个分区被密封阀座限定范围。所述旋流盘对应漏斗的位置上方开口以接纳所述搅拌叶。As shown in the figure: the number of the stirring blades is four. The second dosing pipe includes two sections perpendicular to each other. The valve neck and the valve body are integral structures. The horizontal centerline of the sphere passes through the wall of the large flow channel. A compensation spring is provided on the outer side of the sealing valve seat. The lower side of the sphere is provided with a lower valve stem for auxiliary drive. The diameter of the sphere is larger than the diameter of the valve body pipe. Eight divisions of the spherical surface are bounded by the sealing valve seat. The swirling disk is opened above the position of the funnel to receive the stirring blade.
所述流体控制设备的工作原理及过程如下:控制球阀通流控制方法包括:开启方法、调节方法、关闭方法:所述开启方法包括:关闭位置时所述第一区、第二区面向上游,开启时沿着第一旋向旋转所述球体45度,达到第一开启位,使得第二区、第三区面向上游,从而第六区、第七区面向下游使得所述大流量通道贯通;所述调节方法包括:当絮凝反应池水位下降,使得球体从所述第一开启位起沿着所述第一旋向旋转90度,达到第二开启位使得所述第四区、第五区面向上游,第八区、第一区面向下游,从而使得所述小流量通道贯通;所述关闭方法包括:使得球体从所述第二开启位起沿着第二旋向旋转135度从而使得第一区、第二区面向上游阻断水流,所述第二旋向与第一旋向相反。The working principle and process of the fluid control device are as follows: the control method for controlling the flow of the ball valve includes: an opening method, an adjusting method, and a closing method: the opening method includes: when the first area and the second area are in the closed position, the first area and the second area face upstream, When opening, rotate the sphere 45 degrees along the first rotational direction to reach the first opening position, so that the second area and the third area face upstream, so that the sixth area and the seventh area face downstream so that the large flow channel is connected; The adjustment method includes: when the water level of the flocculation reaction tank drops, the sphere rotates 90 degrees along the first rotation direction from the first open position, and reaches the second open position, so that the fourth zone and the fifth zone are Facing upstream, the eighth zone and the first zone face downstream, so that the small flow channel passes through; the closing method includes: rotating the sphere 135 degrees along the second rotation direction from the second opening position to make the first The first area and the second area face upstream to block water flow, and the second rotation direction is opposite to the first rotation direction.
上列详细说明是针对本发明可行实施例的具体说明,该实施例并非用以限制本发明的专利范围,凡未脱离本发明所为的等效实施或变更,均应包含于本案的专利范围中。The above detailed description is a specific description of a feasible embodiment of the present invention, and the embodiment is not intended to limit the patent scope of the present invention. Any equivalent implementation or modification without departing from the present invention should be included in the patent scope of this case middle.
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Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2010259991A (en) * | 2009-05-01 | 2010-11-18 | Kikosha Co Ltd | Flocculator |
| CN205412714U (en) * | 2016-03-15 | 2016-08-03 | 山东科技大学 | Shunting static mixer |
| CN105964179A (en) * | 2016-06-27 | 2016-09-28 | 江苏中超环保股份有限公司 | Pipeline mixer |
| CN109534468A (en) * | 2018-12-19 | 2019-03-29 | 嘉峪关大友嘉能化工有限公司 | A kind of sewage treatment eddy flow mixing medicine system |
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Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2010259991A (en) * | 2009-05-01 | 2010-11-18 | Kikosha Co Ltd | Flocculator |
| CN205412714U (en) * | 2016-03-15 | 2016-08-03 | 山东科技大学 | Shunting static mixer |
| CN105964179A (en) * | 2016-06-27 | 2016-09-28 | 江苏中超环保股份有限公司 | Pipeline mixer |
| CN109534468A (en) * | 2018-12-19 | 2019-03-29 | 嘉峪关大友嘉能化工有限公司 | A kind of sewage treatment eddy flow mixing medicine system |
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