CN102814139B - Dual-pump circulating stirring dispensing process - Google Patents
Dual-pump circulating stirring dispensing process Download PDFInfo
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- CN102814139B CN102814139B CN201210312357.4A CN201210312357A CN102814139B CN 102814139 B CN102814139 B CN 102814139B CN 201210312357 A CN201210312357 A CN 201210312357A CN 102814139 B CN102814139 B CN 102814139B
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- 238000003756 stirring Methods 0.000 title abstract description 96
- 238000000034 method Methods 0.000 title description 17
- 239000007788 liquid Substances 0.000 abstract description 66
- 239000003814 drug Substances 0.000 abstract description 61
- 238000003860 storage Methods 0.000 abstract description 30
- 239000010865 sewage Substances 0.000 abstract description 29
- 239000000701 coagulant Substances 0.000 abstract description 17
- 239000012530 fluid Substances 0.000 abstract description 12
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract description 10
- 238000012423 maintenance Methods 0.000 abstract description 9
- 239000008399 tap water Substances 0.000 abstract description 7
- 235000020679 tap water Nutrition 0.000 abstract description 7
- 239000007787 solid Substances 0.000 abstract description 5
- 239000002245 particle Substances 0.000 abstract description 4
- 239000006228 supernatant Substances 0.000 abstract description 4
- 239000000126 substance Substances 0.000 abstract 1
- 239000003638 chemical reducing agent Substances 0.000 description 4
- 238000007789 sealing Methods 0.000 description 4
- 238000013019 agitation Methods 0.000 description 3
- 238000005265 energy consumption Methods 0.000 description 3
- 238000005189 flocculation Methods 0.000 description 3
- 230000016615 flocculation Effects 0.000 description 3
- 230000009286 beneficial effect Effects 0.000 description 2
- 230000005540 biological transmission Effects 0.000 description 2
- 230000007547 defect Effects 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 238000001556 precipitation Methods 0.000 description 2
- 238000004140 cleaning Methods 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 238000004090 dissolution Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 238000005188 flotation Methods 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 239000000047 product Substances 0.000 description 1
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Abstract
双口并进泵循环搅拌配药装置属于污水处理的配药领域,其特征在于在配药罐中加入自来水的同时加入污水处理所用的混凝剂,加水至液位传感器,停止加水。打开电磁阀A,开启塑料泵,配药罐中的上清液进入上吸入管,配药罐底部固体颗粒被吸入下吸入管二吸入管中的流体共同通过塑料泵吸入管、塑料泵、搅拌管和搅拌喷嘴进入配药罐中,循环的流体进入配药罐中使罐中流体旋转,对混凝剂进行搅拌,均匀充分溶解后,关闭电磁阀A,打开电磁阀B药液进入药液储箱备用。污水处理设施的所需单元需要药液时,开启离计量泵药液通过计量泵出口管输送至污水处理设施的所需单元。具有设备投资少、结构简单、不易堵塞预防泵过载、维修更换容易的特点。
The dual-port parallel pump circulating stirring dispensing device belongs to the dispensing field of sewage treatment, and is characterized in that tap water is added to the dispensing tank and coagulant used for sewage treatment is added at the same time, water is added to the liquid level sensor, and water addition is stopped. Open the solenoid valve A, turn on the plastic pump, the supernatant in the dispensing tank enters the upper suction pipe, and the solid particles at the bottom of the dispensing tank are sucked into the lower suction pipe. The fluid in the second suction pipe passes through the plastic pump suction pipe, plastic pump, stirring pipe and The stirring nozzle enters the dispensing tank, and the circulating fluid enters the dispensing tank to rotate the fluid in the tank, stir the coagulant, and after it is evenly and fully dissolved, close the solenoid valve A, open the solenoid valve B, and the liquid enters the liquid medicine storage tank for standby. When the required unit of the sewage treatment facility needs liquid medicine, the chemical liquid from the metering pump is transported to the required unit of the sewage treatment facility through the outlet pipe of the metering pump. It has the characteristics of less investment in equipment, simple structure, not easy to block and prevent pump overload, and easy maintenance and replacement.
Description
技术领域 technical field
本发明的双口并进泵循环搅拌配药工艺涉及泵循环搅拌配药技术领域。The double-port parallel pump circulation stirring dispensing process of the present invention relates to the technical field of pump circulation stirring medicine dispensing.
背景技术 Background technique
目前市场上普遍销售的以及一般污水站正在使用的电机变速驱动的搅拌器搅拌配药方式。The mixing and dispensing method of the agitator driven by the variable speed of the motor that is generally sold on the market and is being used in general sewage stations.
搅拌形式主要是由搅拌电机、高传动比减速器、搅拌叶片、配药罐、支撑台架等组成,高传动比减速器一般采用摆线针轮减速器,该减速器结构复杂、制造精度要求高、造价高、维修难度大、对维修工人的技术水平要求很高,一般该种减速机有故障时都是换新,造成维护维修成本高。The mixing form is mainly composed of a stirring motor, a high transmission ratio reducer, a mixing blade, a dispensing tank, a support stand, etc. The high transmission ratio reducer generally adopts a cycloidal pinwheel reducer, which has a complex structure and high manufacturing precision requirements , high cost, difficult maintenance, and high technical requirements for maintenance workers. Generally, when this kind of reducer fails, it will be replaced with a new one, resulting in high maintenance and repair costs.
长期以来环保设备公司样本上各种尺寸规格和正在使用的配药装置搅拌电机的额定功率一般都远大于实际搅拌所需功率,电机功率因数低,造成大马拉小车,效能很低。主要原因在于行业内设计人员已经习惯于类比同尺寸规格的搅拌电机功率,本着再放大一、再保险一点的思路确定新设计产品的电机功率。For a long time, the rated power of the various sizes and specifications of the mixing motors in the catalogs of environmental protection equipment companies and the dispensing devices in use is generally much greater than the actual power required for mixing. The main reason is that designers in the industry have become accustomed to comparing the power of stirring motors of the same size and specifications, and determine the motor power of newly designed products based on the idea of amplifying and reassuring.
配药装置安装到污水站后需要将自来水管引至加药装置上口,工作时,按所需配置浓度,计量混凝剂投放量,先将所需相应量的混凝剂加入到配药罐中,再开启自来水加入到配药罐中,水至配药罐上液位刻度线处关闭自来水阀,然后开启搅拌电机带动叶片进行搅拌,搅拌均匀后,全部排入药液储箱中,再进行下一循环,等待下一次排入药液储箱;药液储箱里的已配置好的药液经由计量泵输出至污水处理设施的所需单元。因此,搅拌电机的闲置率高,如:污水处理采用气浮处理工艺方式情况下,一般搅拌一箱药液,搅拌电机需要工作1小时,一箱子药液可供计量泵工作8~12小时,搅拌电机的闲置率87.5%至91.7%。After the dispensing device is installed in the sewage station, it is necessary to lead the tap water pipe to the top of the dosing device. When working, measure the coagulant dosage according to the required configuration concentration, and first add the required corresponding amount of coagulant to the dispensing tank , then turn on the tap water and add it to the dispensing tank, close the tap water valve when the water reaches the liquid level scale line on the dispensing tank, and then turn on the stirring motor to drive the blades to stir. Circulation, waiting for the next discharge into the liquid medicine storage tank; the configured liquid medicine in the liquid medicine storage tank is output to the required unit of the sewage treatment facility through the metering pump. Therefore, the idle rate of the stirring motor is high. For example, when the sewage treatment adopts the air flotation treatment process, generally a box of liquid medicine is stirred, and the stirring motor needs to work for 1 hour, and a box of liquid medicine can be used for the metering pump to work for 8 to 12 hours. The idle rate of the stirring motor is 87.5% to 91.7%.
这种以电机搅拌为动力的缺陷是:效能低、结构复杂、制造精度要求高、造价高、维修难度大、对维修工人的技术水平要求很高、搅拌时间长、耗能大、设备闲置率高。The disadvantages of this kind of motor stirring are: low efficiency, complex structure, high manufacturing precision requirements, high cost, difficult maintenance, high technical level requirements for maintenance workers, long stirring time, large energy consumption, equipment idle rate high.
申请号:200910039415.9的中国专利申请自动投药射流混合及水泵搅拌污水处理系统文献中公开了用泵做搅拌动力的配药装置,但该装置存在的缺陷:配药水来自污水池,污水将会使配制的药液产生絮凝沉淀,而使药效下降,且絮凝沉淀的物,再经泵的输送循环后,絮凝的污物被重新搅拌而失去絮凝的作用。Application number: 200910039415.9 Chinese patent application for automatic dosing jet mixing and pump stirring sewage treatment system discloses a dispensing device using a pump as a stirring power, but the device has a defect: the dispensing water comes from a sewage pool, and the sewage will make the prepared The medicine liquid produces flocculation and precipitation, which reduces the efficacy of the medicine, and the flocculation and precipitation are transported and circulated by the pump, and the flocculated dirt is re-stirred to lose the effect of flocculation.
发明内容 Contents of the invention
为了克服上述现有技术存在的缺陷,本发明的目的在于提供一种降低机能耗、节省机械搅拌设备投资、提高搅拌效率、维修方便的泵动力搅拌污水处理配药工艺。In order to overcome the above-mentioned defects in the prior art, the object of the present invention is to provide a pump-powered agitation sewage treatment dispensing process that reduces energy consumption, saves investment in mechanical agitation equipment, improves agitation efficiency, and is easy to maintain.
本发明的技术方案为双口并进泵循环搅拌配药工艺包括:配药罐1、液位传感器2、上吸入管3、下吸入管4、塑料泵吸入管5、工作台6、排空阀7、排空管8、电磁阀A9、塑料泵10、止回阀11、搅拌管12、药液储箱出料管13、计量泵14、计量泵出口管15、药液储箱16、电磁阀B17、药液输送管18、搅拌喷嘴19、紧定丝母21、紧定垫圈22、搅拌喷嘴进口管23、搅拌喷嘴出口管24、锥管螺纹25、普通细牙螺纹26,上吸入管3管口和下吸入管4管口置于配药罐1圆心部,上吸入管3、下吸入管4连接塑料泵吸入管5,塑料泵吸入管5接入塑料泵10进口,塑料泵10连接搅拌管12,搅拌管12连接搅拌喷嘴19,搅拌管12上装止回阀11;所述的配药罐1底部连接药液输送管18,药液输送管18上装电磁阀B17;所述的配药罐1下侧部装搅拌喷嘴19;所述的上吸入管3管口置于配药罐1中心,管口高度安装于配药罐1总高的1/2~1/3处,上吸入管3呈水平状。The technical solution of the present invention is a two-port parallel pump circulation stirring dispensing process including:
所述的药液储箱16安装在配药罐1下部,药液储箱16上部连接药液输送管18,药液储箱16前壁连接药液储箱出料管13。The liquid medicine storage tank 16 is installed in the lower part of the
所述的计量泵14进口连接药液储箱出料管13,计量泵14出口连接计量泵出口管15。The inlet of the metering pump 14 is connected to the discharge pipe 13 of the liquid medicine storage tank, and the outlet of the metering pump 14 is connected to the outlet pipe 15 of the metering pump.
所述的下吸入管4,其特征在于管口端向下倾斜,下吸入管4的中心线与配药罐1的中心线夹角为75°。The lower suction pipe 4 is characterized in that the nozzle end is inclined downward, and the angle between the center line of the lower suction pipe 4 and the center line of the
所述的搅拌喷嘴19其特征在于搅拌喷嘴进口管23和搅拌喷嘴24出口管中心线的夹角为60°。The stirring
所述的搅拌喷嘴19通过普通细牙螺纹26与配药罐1连接,配药罐1壁外有密封垫圈22、紧定丝母21和锥管螺纹25与配药罐1紧定。The stirring
所述的配药罐1底部中心处连接排空管8,排空阀7置于排空管8上。The center of the bottom of the
所述的搅拌管12上装止回阀11。Described stirring tube 12 is equipped with check valve 11.
所述的上吸入管3和下吸入管4的管径之比为2∶1。The diameter ratio of the
所述的塑料泵10用塑料离心泵The plastic pump 10 is a plastic centrifugal pump
双口并进泵循环搅拌配药工艺包括以下步骤其特征在于:The double-port parallel pump circulating stirring dispensing process includes the following steps and is characterized in that:
a、在配药罐1中加入自来水的同时加入污水处理所用的混凝剂,加水至液位传感器2,停止加水;a. Add the coagulant used for sewage treatment while adding tap water to the dispensing
b、打开电磁阀A9,开启塑料泵10,配药罐1中的上清液进入上吸入管3,配药罐1底部固体颗粒被吸入下吸入管4二吸入管中的流体共同通过塑料泵吸入管5、塑料泵10、搅拌管12和搅拌喷嘴19进入配药罐1中,搅拌喷嘴进口管23和搅拌喷嘴24出口管中心线的夹角为60°循环的流体进入配药罐1中使罐中流体旋转,对污水处理混凝剂进行搅拌;b. Open the solenoid valve A9, turn on the plastic pump 10, the supernatant in the dispensing
c、待污水处理混凝剂搅拌均匀充分溶解后,关闭电磁阀A9,打开电磁阀B17药液进入药液储箱6备用;c. After the sewage treatment coagulant is stirred evenly and fully dissolved, close the solenoid valve A9, open the solenoid valve B17 and enter the medicinal solution into the medicinal solution storage tank 6 for standby;
d、污水处理设施的所需单元需要药液时,开启离计量泵14药液通过计量泵出口管15输送至污水处理设施的所需单元。d. When the required unit of the sewage treatment facility needs liquid medicine, open the metering pump 14 and transport the liquid medicine to the required unit of the sewage treatment facility through the outlet pipe 15 of the metering pump.
步骤b中所述的上吸入管3与下吸入管4吸入量之比为2∶1。The ratio of the suction volume of the
步骤b中所述的搅拌过程的搅拌时间为30~40min。The stirring time of the stirring process described in step b is 30-40min.
步骤b中所述的下吸入管4,管口端向下倾斜,下吸入管4的中心线与配药罐1的中心线夹角为75°。For the lower suction pipe 4 described in step b, the nozzle end is inclined downward, and the included angle between the centerline of the lower suction pipe 4 and the centerline of the medicine dispensing
有益效果Beneficial effect
比较电机搅拌为动力的搅拌装置,设备投资少、结构简单、维修更换容易。Compared with the stirring device powered by motor stirring, the equipment investment is less, the structure is simple, and the maintenance and replacement are easy.
配制好的药液排放入药液储箱16,可随时对污水处理设施的所需单元供药液。不受配药罐1配药时间的限制。The prepared medicinal liquid is discharged into the medicinal liquid storage tank 16, and the medicinal liquid can be supplied to the required units of the sewage treatment facility at any time. Not limited by the dispensing time of the dispensing
所述的塑料泵10为塑料离心泵,耐腐蚀、造价低、功率小、能耗低、操作简单、使用维护成本低。The plastic pump 10 is a plastic centrifugal pump with corrosion resistance, low cost, low power, low energy consumption, simple operation and low maintenance cost.
下吸入管4管口向下倾斜可利于配药罐1底部中心处的颗粒状混凝剂吸入塑料泵10,在塑料泵10叶轮的高速旋转下加速混凝剂的溶解,提高搅拌效率。The downward inclination of the lower suction pipe 4 nozzles can facilitate the suction of the granular coagulant at the bottom center of the
上吸入管3管口位于配药罐1中心在配药罐1总高的1/2~1/3处,上吸入管3和下吸入管4的管径之比为2∶1,保证上吸入管3流量大于下吸入管的流量,避免固体颗粒状混凝剂吸入过多,预防泵堵塞过载烧坏塑料泵。The nozzle of the
所述的搅拌喷嘴19其特征在于搅拌喷嘴进口管23和搅拌喷嘴24出口管中心线的夹角为60°,循环的液体在进入配药罐1中使罐中液体旋转,对污水处理混凝剂进行搅拌。Described
搅拌喷嘴19通过普通细牙螺纹26与配药罐1连接,配药罐1壁外有密封垫圈22、紧定丝母21和锥管螺纹25与配药罐1紧定在配药罐1外部即可安装,安装维修方便。Stirring
配药罐1底部中心处连接排空管8,排空管8上装有排空阀7利于对配药罐1的排空和清洗。The center of the bottom of the
附图说明 Description of drawings
图1:双口并进泵循环搅拌配药工艺主视图;Figure 1: The front view of the dual-port parallel pump circulation stirring dispensing process;
图2:双口并进泵循环搅拌配药工艺俯视图;Figure 2: The top view of the dual-port parallel pump circulation stirring dispensing process;
图3:I局部放大图;Figure 3: Partial enlarged view of I;
图4:搅拌喷嘴剖视图。Figure 4: Sectional view of the stirring nozzle.
图中:1配药罐、2液位传感器、3上吸入管4下吸入管、5塑料泵吸入管、6工作台、7排空阀、8排空管、9电磁阀A、10塑料泵、11止回阀、12搅拌管、13药液储箱出料管、14计量泵、15计量泵出口管、16药液储箱、17电磁阀B、18药液输送管、19搅拌喷嘴、21紧定丝母、22紧定垫圈、23搅拌喷嘴进口管、24搅拌喷嘴出口管、25锥管螺纹、26普通细牙螺纹。In the figure: 1 dispensing tank, 2 liquid level sensor, 3 upper suction pipe, 4 lower suction pipe, 5 plastic pump suction pipe, 6 working table, 7 emptying valve, 8 emptying pipe, 9 solenoid valve A, 10 plastic pump, 11 Check valve, 12 Stirring pipe, 13 Discharge pipe of liquid medicine storage tank, 14 Metering pump, 15 Outlet pipe of metering pump, 16 Liquid medicine storage tank, 17 Solenoid valve B, 18 Liquid medicine delivery pipe, 19 Stirring nozzle, 21 Tightening screw nut, 22 tight washer, 23 stirring nozzle inlet pipe, 24 stirring nozzle outlet pipe, 25 taper pipe thread, 26 ordinary fine thread.
具体实施方式 Detailed ways
下面结合附图和具体实施例对本发明做进一步说明。The present invention will be further described below in conjunction with the accompanying drawings and specific embodiments.
实施例1Example 1
双口并进泵循环搅拌配药工艺包括:配药罐1、液位传感器2、上吸入管3、下吸入管4、塑料泵吸入管5、工作台6、排空阀7、排空管8、电磁阀A9、塑料泵10、止回阀11、搅拌管12、药液储箱出料管13、计量泵14、计量泵出口管15、药液储箱16、电磁阀B17、药液输送管18、搅拌喷嘴19、紧定丝母21、紧定垫圈22、搅拌喷嘴进口管23、搅拌喷嘴出口管24、锥管螺纹25、普通细牙螺纹26,上吸入管3管口和下吸入管4管口置于配药罐1圆心部,上吸入管3、下吸入管4连接塑料泵吸入管5,塑料泵吸入管5接入塑料泵10进口,塑料泵10连接搅拌管12,搅拌管12连接搅拌喷嘴19,搅拌管12上装止回阀11;所述的配药罐1底部连接药液输送管18,药液输送管18上装电磁阀B17;所述的配药罐1下侧部装搅拌喷嘴19;所述的上吸入管3管口置于配药罐1中心,管口高度安装于配药罐1总高的1/2~1/3处,上吸入管3呈水平状。The double-port parallel pump circulation stirring dispensing process includes: dispensing tank 1, liquid level sensor 2, upper suction pipe 3, lower suction pipe 4, plastic pump suction pipe 5, workbench 6, emptying valve 7, emptying pipe 8, electromagnetic Valve A9, plastic pump 10, check valve 11, stirring pipe 12, liquid medicine storage tank outlet pipe 13, metering pump 14, metering pump outlet pipe 15, medicine liquid storage tank 16, solenoid valve B17, medicine liquid delivery pipe 18 , agitating nozzle 19, tightening screw nut 21, tightening washer 22, agitating nozzle inlet pipe 23, agitating nozzle outlet pipe 24, taper pipe thread 25, ordinary fine thread 26, upper suction pipe 3 nozzles and lower suction pipe 4 The nozzle is placed in the center of the dispensing tank 1, the upper suction pipe 3 and the lower suction pipe 4 are connected to the suction pipe 5 of the plastic pump, the suction pipe 5 of the plastic pump is connected to the inlet of the plastic pump 10, the plastic pump 10 is connected to the stirring pipe 12, and the stirring pipe 12 is connected to A stirring nozzle 19, a check valve 11 is installed on the stirring tube 12; the bottom of the dispensing tank 1 is connected to a liquid medicine delivery pipe 18, and a solenoid valve B17 is installed on the medicine liquid delivery pipe 18; a stirring nozzle 19 is installed on the lower side of the medicine dispensing tank 1 The mouth of the upper suction pipe 3 is placed in the center of the dispensing tank 1, the height of the nozzle is installed at 1/2~1/3 of the total height of the dispensing tank 1, and the upper suction pipe 3 is horizontal.
所述的药液储箱16安装在配药罐1下部,药液储箱16上部连接药液输送管18,药液储箱16前壁连接药液储箱出料管13。The liquid medicine storage tank 16 is installed in the lower part of the
所述的计量泵14进口连接药液储箱出料管13,计量泵14出口连接计量泵出口管15。The inlet of the metering pump 14 is connected to the discharge pipe 13 of the liquid medicine storage tank, and the outlet of the metering pump 14 is connected to the outlet pipe 15 of the metering pump.
所述的下吸入管4,管口端向下倾斜,下吸入管4的中心线与配药罐1的中心线夹角为75°。Described lower suction pipe 4, nozzle end is inclined downward, and the center line of lower suction pipe 4 and the center line angle of dispensing
所述的搅拌喷嘴19搅拌喷嘴进口管23和搅拌喷嘴24出口管中心线的夹角为60°。The included angle between the centerlines of the stirring
所述的搅拌喷嘴19通过普通细牙螺纹26与配药罐1连接,配药罐1壁外有密封垫圈22、紧定丝母21和锥管螺纹25与配药罐1紧定。The stirring
所述的配药罐1底部中心处连接排空管8,排空阀7置于排空管8上。The center of the bottom of the
所述的搅拌管12上装止回阀11。Described stirring tube 12 is equipped with check valve 11.
所述的上吸入管3和下吸入管4的管径之比为2∶1。The diameter ratio of the
所述的塑料泵10用塑料离心泵The plastic pump 10 is a plastic centrifugal pump
双口并进泵循环搅拌配药工艺包括以下步骤:The double-port parallel pump circulating stirring dispensing process includes the following steps:
a、在配药罐1中加入自来水的同时加入污水处理所用的混凝剂,加水至液位传感器2,停止加水;a. Add the coagulant used for sewage treatment while adding tap water to the
b、打开电磁阀A9,开启塑料泵10,配药罐1中的上清液进入上吸入管3,配药罐1底部固体颗粒被吸入下吸入管4二吸入管中的流体共同通过塑料泵吸入管5、塑料泵10、搅拌管12和搅拌喷嘴19进入配药罐1中,搅拌喷嘴进口管23和搅拌喷嘴24出口管中心线的夹角为60°循环的流体进入配药罐1中使罐中流体旋转,对污水处理混凝剂进行搅拌;b. Open the solenoid valve A9, turn on the plastic pump 10, the supernatant in the
c、待污水处理混凝剂搅拌均匀充分溶解后,关闭电磁阀A9,打开电磁阀B17药液进入药液储箱6备用;c. After the sewage treatment coagulant is stirred evenly and fully dissolved, close the solenoid valve A9, open the solenoid valve B17 and enter the medicinal solution into the medicinal solution storage tank 6 for standby;
d、污水处理设施的所需单元需要药液时,开启离计量泵14药液通过计量泵出口管15输送至污水处理设施的所需单元。d. When the required unit of the sewage treatment facility needs liquid medicine, open the metering pump 14 and transport the liquid medicine to the required unit of the sewage treatment facility through the outlet pipe 15 of the metering pump.
步骤b中所述的上吸入管3与下吸入管4吸入量之比为2∶1。The ratio of the suction volume of the
步骤b中所述的搅拌过程的搅拌时间为30min。The stirring time of the stirring process described in step b is 30min.
步骤b中所述的下吸入管4,管口端向下倾斜,下吸入管4的中心线与配药罐1的中心线夹角为75°。For the lower suction pipe 4 described in step b, the nozzle end is inclined downward, and the included angle between the centerline of the lower suction pipe 4 and the centerline of the
实施例2Example 2
双口并进泵循环搅拌配药工艺包括:配药罐1、液位传感器2、上吸入管3、下吸入管4、塑料泵吸入管5、工作台6、排空阀7、排空管8、电磁阀A9、塑料泵10、止回阀11、搅拌管12、药液储箱出料管13、计量泵14、计量泵出口管15、药液储箱16、电磁阀B17、药液输送管18、搅拌喷嘴19、紧定丝母21、紧定垫圈22、搅拌喷嘴进口管23、搅拌喷嘴出口管24、锥管螺纹25、普通细牙螺纹26,上吸入管3管口和下吸入管4管口置于配药罐1圆心部,上吸入管3、下吸入管4连接塑料泵吸入管5,塑料泵吸入管5接入塑料泵10进口,塑料泵10连接搅拌管12,搅拌管12连接搅拌喷嘴19,搅拌管12上装止回阀11;所述的配药罐1底部连接药液输送管18,药液输送管18上装电磁阀B17;所述的配药罐1下侧部装搅拌喷嘴19;所述的上吸入管3管口置于配药罐1中心,管口高度安装于配药罐1总高的1/2~1/3处,上吸入管3呈水平状。The double-port parallel pump circulation stirring dispensing process includes: dispensing tank 1, liquid level sensor 2, upper suction pipe 3, lower suction pipe 4, plastic pump suction pipe 5, workbench 6, emptying valve 7, emptying pipe 8, electromagnetic Valve A9, plastic pump 10, check valve 11, stirring pipe 12, liquid medicine storage tank outlet pipe 13, metering pump 14, metering pump outlet pipe 15, medicine liquid storage tank 16, solenoid valve B17, medicine liquid delivery pipe 18 , agitating nozzle 19, tightening screw nut 21, tightening washer 22, agitating nozzle inlet pipe 23, agitating nozzle outlet pipe 24, taper pipe thread 25, ordinary fine thread 26, upper suction pipe 3 nozzles and lower suction pipe 4 The nozzle is placed in the center of the dispensing tank 1, the upper suction pipe 3 and the lower suction pipe 4 are connected to the suction pipe 5 of the plastic pump, the suction pipe 5 of the plastic pump is connected to the inlet of the plastic pump 10, the plastic pump 10 is connected to the stirring pipe 12, and the stirring pipe 12 is connected to A stirring nozzle 19, a check valve 11 is installed on the stirring tube 12; the bottom of the dispensing tank 1 is connected to a liquid medicine delivery pipe 18, and a solenoid valve B17 is installed on the medicine liquid delivery pipe 18; a stirring nozzle 19 is installed on the lower side of the medicine dispensing tank 1 The mouth of the upper suction pipe 3 is placed in the center of the dispensing tank 1, the height of the nozzle is installed at 1/2~1/3 of the total height of the dispensing tank 1, and the upper suction pipe 3 is horizontal.
所述的药液储箱16安装在配药罐1下部,药液储箱16上部连接药液输送管18,药液储箱16前壁连接药液储箱出料管13。The liquid medicine storage tank 16 is installed in the lower part of the
所述的计量泵14进口连接药液储箱出料管13,计量泵14出口连接计量泵出口管15。The inlet of the metering pump 14 is connected to the discharge pipe 13 of the liquid medicine storage tank, and the outlet of the metering pump 14 is connected to the outlet pipe 15 of the metering pump.
所述的下吸入管4,管口端向下倾斜,下吸入管4的中心线与配药罐1的中心线夹角为75°。Described lower suction pipe 4, nozzle end is inclined downward, and the center line of lower suction pipe 4 and the center line angle of dispensing
所述的搅拌喷嘴19搅拌喷嘴进口管23和搅拌喷嘴24出口管中心线的夹角为60°。The included angle between the centerlines of the stirring
所述的搅拌喷嘴19通过普通细牙螺纹26与配药罐1连接,配药罐1壁外有密封垫圈22、紧定丝母21和锥管螺纹25与配药罐1紧定。The stirring
所述的配药罐1底部中心处连接排空管8,排空阀7置于排空管8上。The center of the bottom of the
所述的搅拌管12上装止回阀11。Described stirring tube 12 is equipped with check valve 11.
所述的上吸入管3和下吸入管4的管径之比为2∶1。The diameter ratio of the
所述的塑料泵10用塑料离心泵The plastic pump 10 is a plastic centrifugal pump
双口并进泵循环搅拌配药工艺包括以下步骤:The double-port parallel pump circulating stirring dispensing process includes the following steps:
a、在配药罐1中加入自来水的同时加入污水处理所用的混凝剂,加水至液位传感器2,停止加水;a. Add the coagulant used for sewage treatment while adding tap water to the
b、打开电磁阀A9,开启塑料泵10,配药罐1中的上清液进入上吸入管3,配药罐1底部固体颗粒被吸入下吸入管4二吸入管中的流体共同通过塑料泵吸入管5、塑料泵10、搅拌管12和搅拌喷嘴19进入配药罐1中,搅拌喷嘴进口管23和搅拌喷嘴24出口管中心线的夹角为60°循环的流体进入配药罐1中使罐中流体旋转,对污水处理混凝剂进行搅拌;b. Open the solenoid valve A9, turn on the plastic pump 10, the supernatant in the
c、待污水处理混凝剂搅拌均匀充分溶解后,关闭电磁阀A9,打开电磁阀B17药液进入药液储箱6备用;c. After the sewage treatment coagulant is stirred evenly and fully dissolved, close the solenoid valve A9, open the solenoid valve B17 and enter the medicinal solution into the medicinal solution storage tank 6 for standby;
d、污水处理设施的所需单元需要药液时,开启离计量泵14药液通过计量泵出口管15输送至污水处理设施的所需单元。d. When the required unit of the sewage treatment facility needs liquid medicine, open the metering pump 14 and transport the liquid medicine to the required unit of the sewage treatment facility through the outlet pipe 15 of the metering pump.
步骤b中所述的上吸入管3与下吸入管4吸入量之比为2∶1。The ratio of the suction volume of the
步骤b中所述的搅拌过程的搅拌时间为40min。The stirring time of the stirring process described in step b is 40min.
步骤b中所述的下吸入管4,管口端向下倾斜,下吸入管4的中心线与配药罐1的中心线夹角为75°。For the lower suction pipe 4 described in step b, the nozzle end is inclined downward, and the included angle between the centerline of the lower suction pipe 4 and the centerline of the
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| CN101468300A (en) * | 2007-12-28 | 2009-07-01 | 亚泰半导体设备股份有限公司 | Barrel tank swirling flow mixing device and method |
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