CN110038476A - A kind of jet stream-stirring manifold type powdery flocculation medicament quantifies dispersion mixing system - Google Patents

A kind of jet stream-stirring manifold type powdery flocculation medicament quantifies dispersion mixing system Download PDF

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CN110038476A
CN110038476A CN201910367943.0A CN201910367943A CN110038476A CN 110038476 A CN110038476 A CN 110038476A CN 201910367943 A CN201910367943 A CN 201910367943A CN 110038476 A CN110038476 A CN 110038476A
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stirring
mixing
liquid level
annular jet
dispersion
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周伟
冯岸岸
朱金波
张勇
闵凡飞
蔡川川
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Anhui University of Science and Technology
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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F21/00Dissolving
    • B01F21/10Dissolving using driven stirrers
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F33/00Other mixers; Mixing plants; Combinations of mixers
    • B01F33/80Mixing plants; Combinations of mixers
    • B01F33/82Combinations of dissimilar mixers
    • B01F33/821Combinations of dissimilar mixers with consecutive receptacles
    • B01F33/8212Combinations of dissimilar mixers with consecutive receptacles with moving and non-moving stirring devices
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F35/00Accessories for mixers; Auxiliary operations or auxiliary devices; Parts or details of general application
    • B01F35/20Measuring; Control or regulation
    • B01F35/22Control or regulation
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F35/00Accessories for mixers; Auxiliary operations or auxiliary devices; Parts or details of general application
    • B01F35/71Feed mechanisms
    • B01F35/717Feed mechanisms characterised by the means for feeding the components to the mixer
    • B01F35/71745Feed mechanisms characterised by the means for feeding the components to the mixer using pneumatic pressure, overpressure, gas or air pressure in a closed receptacle or circuit system
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F35/00Accessories for mixers; Auxiliary operations or auxiliary devices; Parts or details of general application
    • B01F35/71Feed mechanisms
    • B01F35/717Feed mechanisms characterised by the means for feeding the components to the mixer
    • B01F35/7176Feed mechanisms characterised by the means for feeding the components to the mixer using pumps
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F35/00Accessories for mixers; Auxiliary operations or auxiliary devices; Parts or details of general application
    • B01F35/71Feed mechanisms
    • B01F35/717Feed mechanisms characterised by the means for feeding the components to the mixer
    • B01F35/71775Feed mechanisms characterised by the means for feeding the components to the mixer using helical screws
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F35/00Accessories for mixers; Auxiliary operations or auxiliary devices; Parts or details of general application
    • B01F35/71Feed mechanisms
    • B01F35/717Feed mechanisms characterised by the means for feeding the components to the mixer
    • B01F35/71815Feed mechanisms characterised by the means for feeding the components to the mixer using vibrations, e.g. standing waves or ultrasonic vibrations
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F35/00Accessories for mixers; Auxiliary operations or auxiliary devices; Parts or details of general application
    • B01F35/80Forming a predetermined ratio of the substances to be mixed
    • B01F35/83Forming a predetermined ratio of the substances to be mixed by controlling the ratio of two or more flows, e.g. using flow sensing or flow controlling devices
    • B01F35/831Forming a predetermined ratio of the substances to be mixed by controlling the ratio of two or more flows, e.g. using flow sensing or flow controlling devices using one or more pump or other dispensing mechanisms for feeding the flows in predetermined proportion, e.g. one of the pumps being driven by one of the flows
    • B01F35/8311Forming a predetermined ratio of the substances to be mixed by controlling the ratio of two or more flows, e.g. using flow sensing or flow controlling devices using one or more pump or other dispensing mechanisms for feeding the flows in predetermined proportion, e.g. one of the pumps being driven by one of the flows with means for controlling the motor driving the pumps or the other dispensing mechanisms
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F35/00Accessories for mixers; Auxiliary operations or auxiliary devices; Parts or details of general application
    • B01F35/80Forming a predetermined ratio of the substances to be mixed
    • B01F35/88Forming a predetermined ratio of the substances to be mixed by feeding the materials batchwise
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F35/00Accessories for mixers; Auxiliary operations or auxiliary devices; Parts or details of general application
    • B01F35/80Forming a predetermined ratio of the substances to be mixed
    • B01F35/894Measuring receptacles therefor
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/52Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities
    • C02F1/5281Installations for water purification using chemical agents
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/52Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities
    • C02F1/54Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities using organic material
    • C02F1/56Macromolecular compounds
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F2101/00Mixing characterised by the nature of the mixed materials or by the application field
    • B01F2101/305Treatment of water, waste water or sewage
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F2101/00Mixing characterised by the nature of the mixed materials or by the application field
    • B01F2101/48Mixing water in water-taps with other ingredients, e.g. air, detergents or disinfectants

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  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Hydrology & Water Resources (AREA)
  • Engineering & Computer Science (AREA)
  • Environmental & Geological Engineering (AREA)
  • Water Supply & Treatment (AREA)
  • Organic Chemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Mixers Of The Rotary Stirring Type (AREA)
  • Accessories For Mixers (AREA)

Abstract

本发明涉及煤泥水处理工艺中絮凝药剂添加的领域,具体涉及一种射流‑搅拌耦合式粉状絮凝药剂定量分散混合系统。本发明至少包括环空射流装置,还包括药剂储存系统、药剂定量输送及添加系统、射流‑搅拌耦合式分散系统和PLC智能控制系统。射流‑搅拌耦合式分散系统是本发明的核心子系统,包括环空射流装置和搅拌分散装置,其中环空射流装置由螺杆泵、压力水管、引射气管、混合室、喷嘴和稳压喉管组成;搅拌分散装置包含搅拌机构和混合搅拌桶,搅拌机构由定子、套筒、轴和双层叶轮组成,混合搅拌桶底部设计有假底,桶壁布置若干挡板,在桶壁上方布置有液位测量装置;本系统充分考虑絮凝药剂的添加和溶解特点,可做到粉状药剂与溶液同时精准定量添加。

The invention relates to the field of flocculation agent addition in a coal slime water treatment process, in particular to a jet-stirring coupled powder flocculation agent quantitative dispersion mixing system. The invention at least includes an annular jet device, and also includes a medicine storage system, a medicine quantitative delivery and addition system, a jet-stirring coupled dispersion system and a PLC intelligent control system. The jet-stirring coupled dispersion system is the core subsystem of the present invention, including an annular jet device and a stirring and dispersing device, wherein the annular jet device consists of a screw pump, a pressure water pipe, an ejector gas pipe, a mixing chamber, a nozzle and a pressure-stabilizing throat. Composition; The stirring and dispersing device includes a stirring mechanism and a mixing and stirring barrel. The stirring mechanism is composed of a stator, a sleeve, a shaft and a double-layer impeller. The bottom of the mixing and stirring barrel is designed with a false bottom, and several baffles are arranged on the barrel wall. Above the barrel wall are arranged Liquid level measurement device; this system fully considers the addition and dissolution characteristics of flocculation agents, and can accurately and quantitatively add powder agents and solutions at the same time.

Description

一种射流-搅拌耦合式粉状絮凝药剂定量分散混合系统A jet-stirring coupled powder flocculant quantitative dispersion mixing system

技术领域technical field

本发明涉及煤泥水处理工艺中絮凝药剂添加的领域,具体涉及一种射流-搅拌耦合式粉状絮凝药剂定量分散混合系统。The invention relates to the field of flocculation agent addition in a coal slime water treatment process, in particular to a jet-stirring coupled powder flocculation agent quantitative dispersion mixing system.

背景技术Background technique

我国绝大多数选煤厂都采用湿法选煤,煤泥水处理是湿法选煤工艺流程中的重要环节,从经济和环保方面考虑,均要求煤泥水深度澄清,洗水闭路循环。选煤厂通常采用混凝法来处理煤泥水,所谓混凝法就是向煤泥水体系中添加混凝剂,使得煤泥水体系中的颗粒发生团聚后靠重力沉降。混凝剂常用的是有机高分子絮凝剂,如聚丙烯酰胺,由于有机高分子絮凝剂具有分子量大,侧链长等特点,因此存在溶解时间较长、溶解不充分等弊端,若药剂在水中添加及分散混合不均匀,则会造成药剂在规定时间内溶解不彻底,药剂水溶液浓度偏低、药剂浪费等现象,情况严重时还会直接影响煤泥水的处理效果。选煤厂传统的絮凝剂配制方法是通过人工直接把粉状絮凝剂加到混合搅拌桶中直接搅拌,但由于给料不均匀、混合不充分经常会造成药剂结团、溶解不充分等问题,而且需要设置专门岗位司机来观测液位和按时添加粉状絮凝剂,存在一定的滞后性且加药量有人为偏差。虽然实用新型201721157662.5提出采用螺旋给料机给料来解决给料不均匀的问题,发明专利201410260122.4提出采用药剂分散筛来达给料过程中药剂均匀分散的目的,但却无法解决混合不充分、搅拌过程结团和储料仓结拱结块等问题,因而丞需一种粉状絮凝药剂定量分散混合装置或系统来解决药剂混合不充分、溶解过程“溶胀”结团导致粉状药剂溶解不充分的问题。(溶胀是指粉状颗粒的高分子絮凝剂若几个颗粒聚在一起再落入水中,某个颗粒表层膨胀后,包裹其它颗粒,导制颗粒不能分开,造成溶解不完全的现象。)The vast majority of coal preparation plants in my country use wet coal preparation. Coal slime water treatment is an important part of the wet coal preparation process. From the perspective of economy and environmental protection, it is required that the slime water be deeply clarified and the washing water be closed in a closed circuit. Coal preparation plants usually use the coagulation method to treat the slime water. The so-called coagulation method is to add a coagulant to the slime water system to make the particles in the slime water system agglomerate and then settle by gravity. The commonly used coagulants are organic polymer flocculants, such as polyacrylamide. Since organic polymer flocculants have the characteristics of large molecular weight and long side chains, there are disadvantages such as long dissolution time and insufficient dissolution. Uneven addition and dispersion and mixing will result in incomplete dissolution of the agent within the specified time, low concentration of the agent in the aqueous solution, and waste of the agent. In severe cases, it will directly affect the treatment effect of coal slime water. The traditional method of flocculant preparation in coal preparation plants is to manually add powdered flocculant to the mixing and stirring tank for direct stirring. Moreover, it is necessary to set up a special post driver to observe the liquid level and add the powdered flocculant on time. There is a certain hysteresis and the amount of dosing is artificially biased. Although the utility model 201721157662.5 proposes to use a screw feeder for feeding to solve the problem of uneven feeding, and the invention patent 201410260122.4 proposes to use a drug dispersing sieve to achieve the purpose of uniform dispersion of the drug during the feeding process, it cannot solve the problem of insufficient mixing and stirring. Process agglomeration and storage silo arch and agglomeration. Therefore, a powdery flocculating agent quantitative dispersing mixing device or system is needed to solve the problem of insufficient mixing of the agent, "swelling" agglomeration during the dissolution process, and insufficient dissolution of the powdery agent. The problem. (Swelling refers to the phenomenon that if several particles of the polymer flocculant of powdery particles are gathered together and then fall into the water, after the surface of a particle swells, it wraps other particles, and the particles cannot be separated, resulting in incomplete dissolution.)

发明内容SUMMARY OF THE INVENTION

本发明的目的在于克服上述现有技术的不足,设计射流-搅拌耦合式药剂定量分散混合系统,其核心子系统是射流-搅拌耦合式分散系统,包括环空射流装置和搅拌分散装置;其它子系统还有药剂储存系统、药剂定量输送及添加系统和PLC智能控制系统,做到单位体积的液体水中分散混合定量的粉状药剂,保证粉状药剂按需要量添加,在水溶液中均匀分散和快速溶解,杜绝加药量偏差和粉状絮凝药剂“溶胀”结团,溶解困难等问题,本发明集储料、定量螺旋给料、自动喷吹加药和射流-搅拌耦合分散混合于一体,具有装置结构合理和自动化程度高等优点,能在储料、输送和添加过程中杜绝人为因素造成的偏差,同时保证粉状药剂在水溶液中高效分散,为后续的煤泥水处理工作提供良好的絮凝药剂条件。The purpose of the present invention is to overcome the above-mentioned deficiencies of the prior art, and design a jet-stirring coupled pharmaceutical quantitative dispersion mixing system, the core subsystem of which is a jet-stirring coupled dispersion system, including an annular jet device and a stirring and dispersing device; other components The system also has a pharmaceutical storage system, a pharmaceutical quantitative conveying and adding system, and a PLC intelligent control system, which can disperse and mix a quantitative powdered pharmaceutical in a unit volume of liquid water to ensure that the powdered pharmaceutical is added according to the required amount, and is uniformly dispersed and quickly dispersed in the aqueous solution. Dissolution, to avoid problems such as deviation of dosing dosage, “swelling” agglomeration of powdery flocculation agents, difficulty in dissolving, etc. The device has the advantages of reasonable structure and high degree of automation, which can eliminate the deviation caused by human factors in the process of material storage, transportation and addition, and at the same time ensure the efficient dispersion of the powdered agent in the aqueous solution, providing good flocculation agent conditions for the subsequent coal slime water treatment work. .

为实现上述目的,本发明采用了以下技术方案:To achieve the above object, the present invention has adopted the following technical solutions:

一种射流-搅拌耦合式粉状絮凝药剂定量分散混合系统,至少包括环空射流装置,还包括如下组成部分:A jet-stirring coupled powder flocculating agent quantitative dispersion mixing system, at least including an annular jet device, and also includes the following components:

射流-搅拌耦合式分散系统,该分散系统包括环空射流装置和搅拌分散装置;所述环空射流装置主要包括入料螺杆泵、压力水管、引射气管、混合室、喷嘴和稳压喉管;所述入料螺杆泵将需要补加的液体水经压力水管输送至环空射流装置内,由喷嘴高速喷出,在混合室内形成负压,从引射气管吸入外界流体,引射气管与药剂定量输送及添加系统的气力输送管道相连接,粉状药剂在气力输送管道吹力和混合室吸力的共同作用下,以分散状态进入环空射流装置的混合室,在喷嘴射出流体的射流冲击和切割作用下,实现药剂在水中的初步分散,药剂水溶液经稳压喉管进入搅拌分散装置的套筒与轴之间的中空通道;所述的搅拌分散装置包括搅拌机构和混合搅拌桶,搅拌机构由定子、套筒、轴和双层叶轮组成,其中定子上方设有循环孔,混合搅拌桶内的部分药剂水溶液从循环孔重新进入叶轮,再一次被搅拌分散,定子下方设有导向片,能稳定流体的运动方向,套筒与轴之间采用中空设计,是环空射流装置的出料进入搅拌分散装置的通道,药剂水溶液在中空通道内以螺旋下降流的方式进入双层叶轮,轴带动双层叶轮旋转,实现水溶液在混合搅拌桶内持续分散混合及溶解;所述混合搅拌桶底部设计有假底,防止药剂水溶液从出料口直接“串料”,混合搅拌桶桶壁布置若干挡板,消除桶内“圆柱状回转区”,提高搅拌器的搅拌性能,在桶壁上方还设计有液位测量装置;所述液位测量装置主要包括超声波探头和浮球,浮球安装于挡板外边缘的浮球通道中,浮球随液位的高低垂直上下运动,消除搅拌作用引起的液面波动对测量结果的影响,液位测量装置将测得的液位数据传输至PLC智能控制系统,PLC智能控制系统通过数据分析,如发现液位低于设定值的下限,则开启环空射流装置入料螺杆泵,待液位高于设定值的上限,则停止环空射流装置入料螺杆泵作业,在此过程中搅拌机构持续作业,最终实现药剂的高效溶解。A jet-stirring coupled dispersion system, the dispersion system includes an annular jet device and a stirring and dispersing device; the annular jet device mainly includes a feeding screw pump, a pressure water pipe, an ejector gas pipe, a mixing chamber, a nozzle and a pressure-stabilizing throat The feeding screw pump transports the liquid water that needs to be added to the annular jet device through the pressure water pipe, and is ejected by the nozzle at a high speed, forming a negative pressure in the mixing chamber, and sucking the external fluid from the ejector gas pipe, and the ejector gas pipe and the Quantitative drug delivery and the pneumatic conveying pipeline of the adding system are connected. Under the combined action of the blowing force of the pneumatic conveying pipeline and the suction of the mixing chamber, the powdered drug enters the mixing chamber of the annular jet device in a dispersed state, and the jet of the fluid ejected from the nozzle impacts. Under the action of cutting and cutting, the preliminary dispersion of the medicine in the water is realized, and the aqueous solution of the medicine enters the hollow channel between the sleeve and the shaft of the stirring and dispersing device through the pressure-stabilizing throat; the stirring and dispersing device includes a stirring mechanism and a mixing and stirring bucket. The mechanism consists of a stator, a sleeve, a shaft and a double-layered impeller. There is a circulation hole above the stator. Part of the chemical solution in the mixing tank re-enters the impeller from the circulation hole, and is stirred and dispersed again. There is a guide plate below the stator. It can stabilize the moving direction of the fluid. The hollow design between the sleeve and the shaft is the channel for the discharge of the annular jet device to enter the stirring and dispersing device. The double-layer impeller is driven to rotate to realize the continuous dispersion, mixing and dissolution of the aqueous solution in the mixing and stirring barrel; the bottom of the mixing and stirring barrel is designed with a false bottom to prevent the pharmaceutical aqueous solution from being directly "stringed" from the discharge port. The wall of the mixing and stirring barrel is arranged with several The baffle plate eliminates the "cylindrical rotation area" in the barrel and improves the stirring performance of the agitator. A liquid level measuring device is also designed above the barrel wall; the liquid level measuring device mainly includes an ultrasonic probe and a floating ball. The floating ball is installed in In the floating ball channel on the outer edge of the baffle, the floating ball moves vertically up and down with the liquid level, eliminating the influence of the liquid level fluctuation caused by stirring on the measurement results, and the liquid level measuring device transmits the measured liquid level data to the PLC intelligent Control system, PLC intelligent control system through data analysis, if it is found that the liquid level is lower than the lower limit of the set value, the annular jet device feeding screw pump will be turned on, and the annular jet will be stopped when the liquid level is higher than the upper limit of the set value. The device feeds the screw pump, and the stirring mechanism continues to operate during this process, finally realizing the efficient dissolution of the drug.

环空射流装置的引射气管与药剂定量输送及添加系统的气力输送管道相连接;所述药剂定量输送及添加系统主要由螺旋给料机、鼓风机和气力输送管道组成;所述螺旋给料机包括螺旋给料溜槽、螺旋推杆和变频驱动电机,螺旋推杆与变频驱动电机相连,螺旋推杆的转速可调,从而达到定量控制粉状絮凝药剂添加量的目的,螺旋给料机出料口与气力输送管道相连接;所述气力输送管道连接的动力源装置-鼓风机,鼓风机鼓风作业将螺旋给料机定量给入的粉状絮凝药剂,吹入至环空射流装置的引射气管。The ejector gas pipe of the annular jet device is connected with the pneumatic conveying pipeline of the quantitative conveying and adding system of the medicine; the quantitative conveying and adding system of the medicine is mainly composed of a screw feeder, a blower and a pneumatic conveying pipeline; the screw feeder It includes screw feed chute, screw push rod and variable frequency drive motor. The screw push rod is connected with the variable frequency drive motor. The speed of the screw push rod is adjustable, so as to achieve the purpose of quantitatively controlling the amount of powder flocculant added. The screw feeder discharges the material. The port is connected to the pneumatic conveying pipeline; the power source device connected to the pneumatic conveying pipeline is a blower, and the blower blowing operation blows the powder flocculating agent quantitatively fed by the screw feeder into the ejection air pipe of the annular jet device .

PLC智能控制系统,所述的液位测量装置、环空射流装置入料螺杆泵、螺旋给料机的变频驱动电机和鼓风机由PLC智能控制系统智能关联,同时启动或停止动作。PLC intelligent control system, the liquid level measuring device, the annular jet device feeding screw pump, the variable frequency drive motor of the screw feeder and the blower are intelligently linked by the PLC intelligent control system, and start or stop actions at the same time.

本发明的有益效果在于:The beneficial effects of the present invention are:

1)、本发明的射流-搅拌耦合式分散系统、药剂储存系统、药剂定量输送及添加系统和PLC智能控制系统共同配合构成射流-搅拌耦合式粉状絮凝药剂定量分散混合系统,与该装置适配的添加方法自动化程度大大提高,极大地减少了人力物力的投入,同时避免人为因素造成的药剂添加量偏差,且药剂在水溶液中分散混合更加均匀,药剂溶解速度更快,更完全,进而降低药剂消耗量。1) The jet-stirring coupled dispersion system, the pharmaceutical storage system, the pharmaceutical quantitative delivery and addition system and the PLC intelligent control system of the present invention cooperate together to form a jet-stirring coupled powder flocculant quantitative dispersion mixing system, which is suitable for the device. The degree of automation of the addition method of the preparation is greatly improved, which greatly reduces the input of manpower and material resources, and at the same time avoids the deviation of the addition amount of the medicine caused by human factors, and the dispersion and mixing of the medicine in the aqueous solution are more uniform, and the dissolution rate of the medicine is faster and more complete, thereby reducing the Pharmacy consumption.

2)、本发明的药剂储存系统的储料仓顶部设计为敞开式进料口,方便粉状物料的倒入和观察物料仓位情况,工作人员只要将储料仓填满后,就可以参与其它岗位巡查;储料仓下料实现自动控制,储料仓下部倒锥体两侧设有电磁激振器可将粉状絮凝药剂均匀振落,防止仓内结拱现象的发生,储料仓底部的出料口连接星型卸料器,能保证粉状絮凝药剂卸料均匀,防止卸料过程中发生堵塞、结团现象。2) The top of the storage bin of the pharmaceutical storage system of the present invention is designed as an open feed port, which is convenient for the pouring of powdered materials and the observation of the material storage. Post inspection; automatic control of the unloading of the storage bin, electromagnetic vibration exciters on both sides of the inverted cone at the lower part of the storage bin can vibrate the powdered flocculant evenly, preventing the occurrence of arching in the bin, and the bottom of the storage bin is The discharge port is connected to a star discharger, which can ensure the uniform discharge of powder flocculation agents and prevent blockage and agglomeration during the discharge process.

3)、本发明的药剂定量输送及添加系统主要由螺旋给料机、鼓风机和气力输送管道组成,螺旋给料机包括螺旋给料溜槽、螺旋推杆和变频驱动电机,螺旋推杆与变频驱动电机相连,螺旋给料溜槽的横截面积S一定,单位面积储存的药剂量M一定,螺旋给料机单位时间的给料量取决于螺旋推杆的转速,单位时间药剂给料量Q=S×M×υ,通过控制螺旋推杆的转速,从而达到定量控制粉状絮凝药剂添加量的目的;螺旋给料机出料口与气力输送管道相连接,气力输送的动力源装置是鼓风机,鼓风机通过鼓风将螺旋给料机输送来的粉状絮凝药剂吹到药剂分散装置中的环空射流装置内。3), the pharmaceutical quantitative conveying and adding system of the present invention is mainly composed of a screw feeder, a blower and a pneumatic conveying pipeline. The screw feeder includes a screw feed chute, a screw push rod and a variable frequency drive motor. The motor is connected, the cross-sectional area S of the screw feeding chute is constant, and the amount of medicine stored per unit area M is constant. ×M×υ, by controlling the rotational speed of the screw push rod, the purpose of quantitatively controlling the amount of powdered flocculant added is achieved; the discharge port of the screw feeder is connected with the pneumatic conveying pipeline, and the power source device of the pneumatic conveying is the blower, the blower The powdery flocculation agent conveyed by the screw feeder is blown into the annular jet device in the agent dispersing device by blowing air.

4)、本发明的射流-搅拌耦合式分散系统,该分散系统包括环空射流装置和搅拌分散装置;所述环空射流装置主要包括入料螺杆泵、压力水管、引射气管、混合室、喷嘴和稳压喉管,液体水在螺杆泵的作用下通过压力水管进入环空射流装置,在混合室内形成负压,抽吸引射气管中的粉状絮凝剂,粉状絮凝剂在鼓风机吹力和混合室吸力的共同作用下进入环空射流装置,粉状絮凝剂在射流作用的冲击和切割下,均匀的分散在液体水中,与液体水混合后由稳压喉管进入搅拌分散装置的套筒与轴之间的中空通道;搅拌分散装置保证混合药剂的水溶液在混合搅拌桶内持续湍流运动,搅拌分散装置主要包括混合搅拌桶和搅拌机构,搅拌机构由定子、套筒、轴和双层叶轮组成,定子可以维持液面稳定,定子上方设有循环孔,混合搅拌桶内的部分药剂水溶液从循环孔重新进入叶轮,再一次被搅拌分散,定子下方设有导向片,能稳定流体的运动方向,套筒与轴之间采用中空设计,是环空射流装置的出料进入搅拌分散装置的通道,药剂水溶液在中空通道内以螺旋下降流的方式进入双层叶轮,轴带动双层叶轮旋转,叶轮与定子(导向片)、假底配合使液体形成W形流动形式,增强液体的紊流度,实现水溶液在混合搅拌桶内持续分散混合及溶解;混合搅拌桶底部设计有假底,防止药剂水溶液从出料口直接“串料”,混合搅拌桶桶壁布置若干挡板,消除桶内“圆柱状回转区”,提高搅拌器的搅拌性能,在桶壁上方还设计有液位测量装置;液位测量装置主要包括超声波探头和浮球,浮球安装于挡板外边缘的浮球通道中,浮球随液位的高低垂直上下运动,消除搅拌作用引起的液面波动对测量结果的影响,液位测量装置将测得的液位数据传输至PLC智能控制系统,PLC智能控制系统通过数据分析,如发现液位低于设定值的下限,则开启环空射流装置入料螺杆泵,待液位高于设定值的上限,则停止环空射流装置入料螺杆泵作业,在此过程中搅拌机构持续作业,最终实现药剂的高效溶解。4), the jet-stirring coupled dispersion system of the present invention, the dispersion system includes an annular jet device and a stirring and dispersing device; the annular jet device mainly includes a feeding screw pump, a pressure water pipe, an ejector gas pipe, a mixing chamber, Nozzle and pressure-stabilizing throat, the liquid water enters the annular jet device through the pressure water pipe under the action of the screw pump, and forms a negative pressure in the mixing chamber to suck the powder flocculant in the jet pipe, and the powder flocculant is blown by the blower. Under the combined action of the suction of the mixing chamber, it enters the annular jet device, and the powdery flocculant is uniformly dispersed in the liquid water under the impact and cutting of the jet, and after mixing with the liquid water, it enters the jacket of the stirring and dispersing device through the pressure-stabilizing throat. The hollow channel between the barrel and the shaft; the stirring and dispersing device ensures the continuous turbulent motion of the aqueous solution of the mixed agent in the mixing and stirring barrel. The stirring and dispersing device mainly includes the mixing and stirring barrel and the stirring mechanism. The stirring mechanism consists of a stator, a sleeve, a shaft and a double layer. The stator is composed of an impeller, the stator can keep the liquid level stable, and there is a circulation hole above the stator. Part of the chemical solution in the mixing tank re-enters the impeller from the circulation hole, and is stirred and dispersed again. There is a guide plate under the stator, which can stabilize the movement of the fluid. The hollow design is adopted between the sleeve and the shaft, which is the channel for the discharge of the annular jet device to enter the stirring and dispersing device. The medicinal solution enters the double-layer impeller in a spiral downward flow in the hollow channel, and the shaft drives the double-layer impeller to rotate. , The impeller cooperates with the stator (guide plate) and the false bottom to form a W-shaped flow form of the liquid, enhance the turbulence of the liquid, and realize the continuous dispersion, mixing and dissolution of the aqueous solution in the mixing tank; the bottom of the mixing tank is designed with a false bottom to prevent The aqueous solution of the chemical is directly "stringed" from the discharge port, and several baffles are arranged on the wall of the mixing and stirring barrel to eliminate the "cylindrical rotation area" in the barrel and improve the stirring performance of the agitator. A liquid level measuring device is also designed above the barrel wall. The liquid level measuring device mainly includes an ultrasonic probe and a floating ball, which is installed in the floating ball channel on the outer edge of the baffle. The liquid level measuring device transmits the measured liquid level data to the PLC intelligent control system. The PLC intelligent control system analyzes the data. If the liquid level is found to be lower than the lower limit of the set value, the annular jet device feeds the screw pump. , when the liquid level is higher than the upper limit of the set value, the operation of the feeding screw pump of the annular jet device is stopped. During this process, the stirring mechanism continues to operate, and finally the efficient dissolution of the drug is realized.

5)、本发明的PLC智能控制系统可以将电磁激振器、星型卸料器、螺旋给料机、鼓风机和环空射流装置联动作业,实现精准定量给药和药剂的均匀分散;液位测量装置将混合搅拌桶的液位数据传输给PLC智能控制系统,智能控制装置通过数据分析,如液位低于设定值的下限,则开启环空射流装置的入料螺杆泵向混合搅拌桶补加液体水,同时开启电磁激振器、星型卸料器、螺旋给料机和鼓风机向环空射流装置的引射管中吹入与液体水流量相对应的定量粉状絮凝剂,实现粉状絮凝剂在液体水中的均匀分散,待液位高于设定值的上限,同时停止电磁激振器、星型卸料器、螺旋给料机、鼓风机和环空射流装置的入料螺杆泵作业,在此过程中搅拌叶轮持续作业,最终实现药剂的高效溶解。5), the PLC intelligent control system of the present invention can link the electromagnetic vibration exciter, the star discharger, the screw feeder, the blower and the annular jet device to achieve precise quantitative dosing and uniform dispersion of the medicament; The measuring device transmits the liquid level data of the mixing tank to the PLC intelligent control system. The intelligent control device analyzes the data. If the liquid level is lower than the lower limit of the set value, the feeding screw pump of the annular jet device is turned on to the mixing tank. Add liquid water, and at the same time open the electromagnetic exciter, star discharger, screw feeder and blower to blow the quantitative powdery flocculant corresponding to the liquid water flow into the ejection tube of the annular jet device to achieve The powdery flocculant is uniformly dispersed in the liquid water. When the liquid level is higher than the upper limit of the set value, stop the feeding screw of the electromagnetic exciter, star discharger, screw feeder, blower and annular jet device at the same time. During the pump operation, the stirring impeller continues to operate, and finally the efficient dissolution of the agent is realized.

6)环空射流装置入料螺杆泵是一种容积泵,其单位时间输送的流体流量稳定;螺旋给料机输送的粉状药剂量与螺旋推杆的转速相关,也可实现定量控制,两者配合实现粉状药剂在水中的精准定量添加。6) The feeding screw pump of the annular jet device is a positive displacement pump, and its fluid flow per unit time is stable; the amount of powder medicine conveyed by the screw feeder is related to the speed of the screw push rod, and it can also achieve quantitative control. It can realize accurate quantitative addition of powdered chemicals in water.

附图说明Description of drawings

图1为本发明的正面示意图;Fig. 1 is the front schematic diagram of the present invention;

图2为本发明的各系统逻辑关系图;Fig. 2 is each system logical relation diagram of the present invention;

图3为图1结构中,环空射流装置的正面示意图;3 is a schematic front view of the annular jet device in the structure of FIG. 1;

图示各结构与本发明的部件名称对应关系如下:The corresponding relationship between each structure shown in the figure and the name of the component of the present invention is as follows:

A-药剂储存系统 B-药剂定量输送及添加系统 C-射流-搅拌耦合式分散系统A-drug storage system B-drug quantitative delivery and addition system C-jet-stirring coupled dispersion system

D-PLC智能控制系统 1-仓盖 2-储料仓 3-电磁激振器 4-星型卸料器D-PLC intelligent control system 1-silo cover 2-storage bin 3-electromagnetic vibration exciter 4-star discharger

5-变频驱动电机 6-螺旋给料机 6A-螺旋推杆 6B-螺旋给料溜槽5- Frequency conversion drive motor 6- Screw feeder 6A- Screw push rod 6B- Screw feed chute

7-鼓风机 8-气力输送管道 9-螺杆泵 10-压力水管7-Blower 8-Pneumatic conveying pipeline 9-Screw pump 10-Pressure water pipe

11-环空射流装置 12-皮带轮 13-搅拌分散装置 14-搅拌机构11-annular jet device 12-belt pulley 13-stirring and dispersing device 14-stirring mechanism

15-套筒 16-定子 16A-导向片 16B-循环孔 17-中空通道15-Sleeve 16-Stator 16A-Guide piece 16B-Circulation hole 17-Hollow channel

18-轴 19-双层叶轮 20-吸药室 21-假底 22-出料口18-shaft 19-double impeller 20-suction chamber 21-false bottom 22-discharge port

23-液位测量装置 23A-超声波探头 23B-浮球 23C-浮球通道23-Liquid level measuring device 23A-Ultrasonic probe 23B-Float ball 23C-Float ball channel

24-混合搅拌桶 25-挡板 26-压力水管 27-引射气管 28-混合室24-mixing bucket 25-baffle plate 26-pressure water pipe 27-injection gas pipe 28-mixing chamber

29-喷嘴 30-稳压喉管29-Nozzle 30-Regulatory Throat

具体实施方式Detailed ways

下面将结合本发明实施例中的附图,对本发明中的技术方案进行清楚、完整地描述。基于本发明中的实施例,本领域普通技术人员在没有做出创造性劳动前提下所获得的所有其他实施例,都属于本发明保护的范围。The technical solutions in the present invention will be clearly and completely described below with reference to the accompanying drawings in the embodiments of the present invention. Based on the embodiments of the present invention, all other embodiments obtained by those of ordinary skill in the art without creative efforts shall fall within the protection scope of the present invention.

实施例.本发明应用在煤泥水处理工艺中粉状絮凝药剂添加系统中Example. The present invention is applied in the powdery flocculation agent adding system in the coal slime water treatment process

如图1-3所示,一种射流-搅拌耦合式粉状絮凝药剂定量分散混合系统包括如下组成部分:As shown in Figure 1-3, a jet-stirring coupled powder flocculant quantitative dispersion mixing system includes the following components:

药剂储存系统(A),该储存系统包括依次顺连的储料仓(2)、电磁激振器(3)、星型卸料阀(4);储料仓上部为圆桶形,下部为倒锥形,储料仓顶部为敞开式进料口,进料口设有仓盖(1),防止粉状絮凝药吸水结团,底部设有出料口,在储料仓(2)下部倒锥体两侧设有电磁激振器(3),电磁激振器(3)可将储料仓(2)的粉状絮凝药剂均匀振落,防止仓内结拱现象的发生,振落的物料由储料仓底部的出料口排出,储料仓底部的出料口连接星型卸料器(4),能保证粉状絮凝药剂卸料均匀,防止卸料过程中发生堵塞、结团现象,星型卸料器出口外接螺旋给料机(6);A pharmaceutical storage system (A), the storage system comprises a storage bin (2), an electromagnetic exciter (3), and a star-shaped discharge valve (4) that are connected in sequence; the upper part of the storage bin is cylindrical, and the lower part is Inverted cone shape, the top of the storage bin is an open feed port, the feed port is provided with a bin cover (1) to prevent the powdery flocculants from absorbing water and agglomerating, and a discharge port is provided at the bottom, at the lower part of the storage bin (2). Electromagnetic vibration exciters (3) are arranged on both sides of the inverted cone, and the electromagnetic vibration exciters (3) can evenly vibrate the powdery flocculating agent of the storage bin (2), so as to prevent the occurrence of arching in the bin and vibrate and fall off. The raw material is discharged from the discharge port at the bottom of the storage bin, and the discharge port at the bottom of the storage bin is connected to the star discharger (4), which can ensure the uniform discharge of the powder flocculation agent and prevent blockage and stagnation during the discharge process. If the group phenomenon occurs, the screw feeder (6) is connected to the outlet of the star discharger;

药剂定量输送及添加系统(B),该系统主要由螺旋给料机(6)、鼓风机(7)和气力输送管道(8)组成;螺旋给料机包括螺旋给料溜槽(6B)、螺旋推杆(6A)和变频驱动电机(5),螺旋推杆(6A)与变频驱动电机(5)相连,星型卸料器(4)将粉状絮凝药剂卸到螺旋给料溜槽(6B)中,在螺旋推杆(6A)的推动作用下向螺旋给料机出料口方向运动,螺旋推杆(6A)的转速可调,从而达到定量控制粉状絮凝药剂添加量的目的,螺旋给料机出料口与气力输送管道(8)相连接,气力输送管道(8)分别连接气力输送的动力源装置-鼓风机(7)和环空射流装置(11),螺旋给料机(6)定量给入的粉状絮凝药剂,通过鼓风机(7)鼓风作业,气力输送至环空射流装置(11);Quantitative drug delivery and addition system (B), which is mainly composed of a screw feeder (6), a blower (7) and a pneumatic conveying pipeline (8); the screw feeder includes a screw feed chute (6B), a screw pusher The rod (6A) is connected with the variable frequency drive motor (5), the screw push rod (6A) is connected with the variable frequency drive motor (5), and the star discharger (4) discharges the powdery flocculant into the screw feed chute (6B) , under the pushing action of the screw push rod (6A), it moves towards the discharge port of the screw feeder, and the speed of the screw push rod (6A) is adjustable, so as to achieve the purpose of quantitatively controlling the amount of powder flocculant added. The discharge port of the machine is connected with the pneumatic conveying pipeline (8), and the pneumatic conveying pipeline (8) is respectively connected with the power source devices of pneumatic conveying-the blower (7) and the annular jet device (11), and the screw feeder (6) is quantitative The fed powdery flocculating agent is blasted by the blower (7) and pneumatically transported to the annular jet device (11);

射流-搅拌耦合式分散系统(C),该系统主要由环空射流装置(11)、搅拌分散装置(13)和液位测量装置(23)组成;环空射流装置主要包括压力水管(26)、引射气管(27)、混合室(28)、喷嘴(29)和稳压喉管(30);搅拌分散装置主要包括搅拌机构(14)和混合搅拌桶(24),搅拌机构由定子(16)、套筒(15),、轴(18)和双层叶轮(19)组成,其中定子上方设有循环孔(16B),溶解不充分的药剂借助循环孔重新进入双层叶轮(19)搅拌区,再一次被搅拌分散,定子下方设有导向片(16A),能稳定流体的运动方向,套筒(15)与轴(18)之间采用中空设计,中空通道(17)内的药剂溶液以螺旋下降流的方式进入双层叶轮(19)上方的吸药室(20),轴(18)带动双层叶轮(19)旋转,实现药剂在水溶液中持续分散混合,最终实现药剂的快速高效溶解,混合搅拌桶底部设计有假底(21),防止药剂水溶液从出料口(22)直接“串料”,混合搅拌桶桶壁布置若干挡板(25),消除桶内“圆柱状回转区”,提高搅拌机构的搅拌性能,在桶壁上方还设计有液位测量装置(23);液位测量装置(23)主要包括超声波探头(23A)和浮球(23B),浮球(23B)安装于挡板(25)外边缘的浮球通道(23C)中,浮球随液位的高低垂直上下运动,消除搅拌作用引起的液面波动对测量结果的影响,液位测量装置(23)将测得的液位数据传输至PLC智能控制系统(D),PLC智能控制系统通过数据分析,如发现液位低于设定值的下限,则开启环空射流装置(11)的入料螺杆泵(9),待液位高于设定值的上限,则停止环空射流装置(11)的入料螺杆泵(9)作业,在此过程中搅拌机构(14)持续作业,最终实现药剂的高效溶解。A jet-stirring coupled dispersion system (C), the system mainly consists of an annular jet device (11), a stirring and dispersing device (13) and a liquid level measuring device (23); the annular jet device mainly includes a pressure water pipe (26) , ejection gas pipe (27), mixing chamber (28), nozzle (29) and pressure-stabilizing throat (30); the stirring and dispersing device mainly includes a stirring mechanism (14) and a mixing and stirring tank (24), and the stirring mechanism is composed of a stator ( 16), a sleeve (15), a shaft (18) and a double-layer impeller (19), wherein a circulation hole (16B) is arranged above the stator, and the insufficiently dissolved medicament re-enters the double-layer impeller (19) through the circulation hole The stirring area is stirred and dispersed again. There is a guide plate (16A) under the stator, which can stabilize the movement direction of the fluid. A hollow design is used between the sleeve (15) and the shaft (18), and the medicine in the hollow channel (17) The solution enters the drug suction chamber (20) above the double-layer impeller (19) in a spiral downward flow, and the shaft (18) drives the double-layer impeller (19) to rotate, so as to realize the continuous dispersion and mixing of the drug in the aqueous solution, and finally realize the rapid High-efficiency dissolution, the bottom of the mixing and stirring barrel is designed with a false bottom (21) to prevent the pharmaceutical aqueous solution from being directly "strained" from the discharge port (22), and several baffles (25) are arranged on the wall of the mixing and stirring barrel to eliminate "cylindrical" Rotation area" to improve the stirring performance of the stirring mechanism, and a liquid level measuring device (23) is also designed above the barrel wall; the liquid level measuring device (23) mainly includes an ultrasonic probe (23A) and a floating ball (23B). 23B) is installed in the floating ball channel (23C) on the outer edge of the baffle plate (25), the floating ball moves vertically up and down with the height of the liquid level, eliminating the influence of the liquid level fluctuation caused by the stirring action on the measurement results, the liquid level measuring device ( 23) The measured liquid level data is transmitted to the PLC intelligent control system (D). The PLC intelligent control system analyzes the data, and if it is found that the liquid level is lower than the lower limit of the set value, the inlet of the annular jet device (11) is turned on. When the liquid level is higher than the upper limit of the set value, the feeding screw pump (9) of the annular jet device (11) is stopped. During this process, the stirring mechanism (14) continues to operate, and finally Achieve efficient dissolution of pharmaceuticals.

PLC智能控制系统(D),液位测量装置(23)将混合搅拌桶的液位数据传输给PLC智能控制系统,智能控制装置通过数据分析,如液位低于设定值的下限,则同时开启电磁激振器(3)、星型卸料器(4)、螺旋给料机(6)、鼓风机(7)和环空射流装置(11)的入料螺杆泵(9),待液位高于设定值的上限,同时停止电磁激振器(3)、星型卸料器(4)、螺旋给料机(6)、鼓风机(7)和环空射流装置(11)的入料螺杆泵(9)作业。The PLC intelligent control system (D), the liquid level measuring device (23) transmits the liquid level data of the mixing tank to the PLC intelligent control system, and the intelligent control device analyzes the data, if the liquid level is lower than the lower limit of the set value, then at the same time Turn on the electromagnetic vibration exciter (3), the star discharger (4), the screw feeder (6), the blower (7) and the feeding screw pump (9) of the annular jet device (11). Above the upper limit of the set value, stop the feeding of the electromagnetic exciter (3), star discharger (4), screw feeder (6), blower (7) and annular jet device (11) at the same time The screw pump (9) works.

综上,本发明的射流-搅拌耦合式粉状絮凝药剂定量自动添加装置充分考虑煤泥水絮凝药剂的添加和溶解特点,做到液体水和粉状药剂的同时精准定量添加,具有装置结构合理和自动化程度高等优点,能在储料、输送和添加过程中杜绝人为因素造成的偏差,同时保证粉状药剂在水溶液中高效分散及溶解,为后续的煤泥水处理工作提供良好的絮凝药剂条件,药剂消耗成本的降低也极为明显。To sum up, the jet-stirring coupling type powdery flocculating agent quantitative automatic adding device of the present invention fully considers the addition and dissolution characteristics of the coal slime water flocculating agent, achieves accurate and quantitative addition of liquid water and powdery agent at the same time, and has a reasonable device structure and It has the advantages of high degree of automation, which can eliminate the deviation caused by human factors in the process of material storage, transportation and addition, and at the same time ensure the efficient dispersion and dissolution of powdered chemicals in the aqueous solution, and provide good flocculation conditions for the subsequent coal slime water treatment. The reduction in consumption costs is also very significant.

Claims (3)

1.一种射流-搅拌耦合式粉状絮凝药剂定量分散混合系统,至少包括环空射流装置(11),其特征在于还包括如下组成部分:药剂储存系统(A)、药剂定量输送及添加系统(B)、射流-搅拌耦合式分散系统(C)和PLC智能控制系统(D);所述射流-搅拌耦合式分散系统(C)包括环空射流装置(11)和搅拌分散装置(13);所述环空射流装置(11)主要包括入料的螺杆泵(9)、压力水管(10)、引射气管(27)、混合室(28)、喷嘴(29)和稳压喉管(30);所述入料的螺杆泵(9)将需要补加的液体水经压力水管(10)输送至环空射流装置(11)内,由喷嘴(29)高速喷出,在混合室(28)内形成负压,从引射气管(27)吸入外界流体,引射气管(27)与药剂定量输送及添加系统(B)的气力输送管道(8)相连接,粉状药剂在气力输送管道(8)吹力和混合室吸力的共同作用下,以分散状态进入环空射流装置(11)的混合室(28),在喷嘴(29)射出流体的射流冲击和切割作用下,实现药剂在水中的初步分散,药剂水溶液经稳压喉管(30)进入搅拌分散装置(13)的套筒(15)与轴(18)之间的中空通道(17);所述的搅拌分散装置(13)包括搅拌机构(14)和混合搅拌桶(24),搅拌机构(14)由定子(16)、套筒(15)、轴(18)和双层叶轮(19)组成,其中定子(16)上方设有循环孔(16B),混合搅拌桶(24)内的部分药剂水溶液从循环孔(16B)重新进入双层叶轮(19)搅拌区域,定子(16)下方设有导向片(16A),能稳定流体的运动方向,套筒(15)与轴(18)之间采用中空设计,是环空射流装置(11)中混合物料进入搅拌分散装置(13)的通道,药剂水溶液在中空通道(17)内以螺旋下降流的方式进入双层叶轮(19),轴(18)带动双层叶轮(19)旋转,实现水溶液在混合搅拌桶(24)内持续分散混合及溶解;所述混合搅拌桶(24)底部设计有假底(21),防止药剂水溶液从出料口(22)直接“串料”,混合搅拌桶(24)桶壁布置若干挡板(25),消除桶内“圆柱状回转区”,在桶壁上方还设计有液位测量装置(23);所述液位测量装置(23)主要包括超声波探头(23A)和浮球(23B),浮球(23B)安装于挡板外边缘的浮球通道(23C)中,浮球随液位的高低垂直上下运动,液位测量装置将测得的液位数据传输至PLC智能控制系统(D),PLC智能控制系统(D)通过数据分析,如发现液位低于设定值的下限,则开启环空射流装置(11)入料的螺杆泵(9),待液位高于设定值的上限,则停止环空射流装置(11)入料的螺杆泵(9)作业,在此过程中搅拌机构(14)持续作业,最终实现药剂的高效溶解。1. A jet-stirring coupling type powdery flocculation medicament quantitative dispersion mixing system, comprising at least an annular jet device (11), is characterized in that also comprising the following components: medicament storage system (A), medicament quantitative delivery and adding system (B), a jet-stirring coupled dispersion system (C) and a PLC intelligent control system (D); the jet-stirring coupled dispersion system (C) includes an annular jet device (11) and a stirring and dispersing device (13) ; The annular jet device (11) mainly includes a feeding screw pump (9), a pressure water pipe (10), an ejector gas pipe (27), a mixing chamber (28), a nozzle (29) and a pressure-stabilizing throat (27). 30; 28) Negative pressure is formed in the inside, and the external fluid is sucked from the ejector trachea (27), and the ejector trachea (27) is connected with the pneumatic conveying pipeline (8) of the medicament quantitative conveying and adding system (B), and the powdered medicament is pneumatically conveyed. Under the combined action of the blowing force of the pipe (8) and the suction of the mixing chamber, it enters the mixing chamber (28) of the annular jet device (11) in a dispersed state. For preliminary dispersion in water, the aqueous solution of the chemical enters the hollow channel (17) between the sleeve (15) and the shaft (18) of the stirring and dispersing device (13) through the pressure-stabilizing throat (30); the stirring and dispersing device ( 13) Including a stirring mechanism (14) and a mixing and stirring tank (24), the stirring mechanism (14) is composed of a stator (16), a sleeve (15), a shaft (18) and a double-layer impeller (19), wherein the stator (16) ) is provided with a circulation hole (16B) above, and part of the chemical aqueous solution in the mixing and stirring barrel (24) re-enters the mixing area of the double impeller (19) from the circulation hole (16B), and a guide plate (16A) is provided below the stator (16). , which can stabilize the movement direction of the fluid. The hollow design is adopted between the sleeve (15) and the shaft (18), which is the channel for the mixed material in the annular jet device (11) to enter the stirring and dispersing device (13). (17) enters the double-layer impeller (19) in a spiral downward flow, and the shaft (18) drives the double-layer impeller (19) to rotate, so as to realize the continuous dispersion, mixing and dissolution of the aqueous solution in the mixing and stirring barrel (24); the mixing The bottom of the mixing bucket (24) is designed with a false bottom (21) to prevent the aqueous solution of the chemical from being directly “strained” from the discharge port (22). "Cylindrical rotary area", a liquid level measuring device (23) is also designed above the barrel wall; the liquid level measuring device (23) mainly includes an ultrasonic probe (23A) and a floating ball (23B), and the floating ball (23B) is installed In the floating ball channel (23C) on the outer edge of the baffle, the floating ball moves vertically up and down with the liquid level, and the liquid level measuring device transmits the measured liquid level data to the PLC intelligent control system (D), which is controlled by the PLC intelligently. System (D) through data analysis, if it is found that the liquid level is lower than the lower limit of the set value, the screw pump (9) feeding the annular jet device (11) is turned on, and when the liquid level is higher than the upper limit of the set value, then The operation of the screw pump (9) feeding the annular jet device (11) is stopped, and the stirring mechanism (14) continues to operate during this process, finally realizing the efficient dissolution of the medicament. 2.根据权利要求1所述的一种射流-搅拌耦合式粉状絮凝药剂定量分散混合系统,其特征在于:所述药剂定量输送及添加系统(B)主要由螺旋给料机(6)、鼓风机(7)和气力输送管道(8)组成;所述螺旋给料机(6)包括螺旋给料溜槽(6B)、螺旋推杆(6A)和变频驱动电机(5),螺旋推杆(6A)与变频驱动电机(5)相连,螺旋推杆(6A)的转速可调,从而达到定量控制粉状絮凝药剂添加量的目的,螺旋给料机(6)出料口与气力输送管道(8)相连接;所述气力输送管道(8)连接的动力源装置-鼓风机(7),鼓风机(7)鼓风作业将螺旋给料机定量给入的粉状絮凝药剂,吹入至环空射流装置(11)的引射气管(27)。2. A jet-stirring coupled powder flocculation agent quantitative dispersion mixing system according to claim 1, characterized in that: the agent quantitative conveying and adding system (B) is mainly composed of a screw feeder (6), A blower (7) and a pneumatic conveying pipeline (8) are composed; the screw feeder (6) includes a screw feed chute (6B), a screw push rod (6A), a variable frequency drive motor (5), and a screw push rod (6A) ) is connected with the variable frequency drive motor (5), the speed of the screw push rod (6A) is adjustable, so as to achieve the purpose of quantitatively controlling the amount of powder flocculant added. ) is connected; the power source device connected by the pneumatic conveying pipeline (8) - the blower (7), the blower (7) blows the powdery flocculating agent quantitatively fed by the screw feeder into the annular jet The ejector gas tube (27) of the device (11). 3.根据权利要求1所述的一种射流-搅拌耦合式粉状絮凝药剂定量分散混合系统,其特征在于:所述的液位测量装置(23)、环空射流装置(11)入料的螺杆泵(9)、螺旋给料机(6)的变频驱动电机(5)和鼓风机(7)由PLC智能控制系统(D)智能关联,同时启动或停止动作。3. A jet-stirring coupling type powdery flocculating agent quantitative dispersion mixing system according to claim 1, characterized in that: the liquid level measuring device (23), the annular jet device (11) feeding The variable frequency drive motor (5) and the blower (7) of the screw pump (9), the screw feeder (6) and the blower (7) are intelligently associated by the PLC intelligent control system (D), and simultaneously start or stop actions.
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Application publication date: 20190723