CN203990481U - Polymer negative pressure suction dispersal device - Google Patents
Polymer negative pressure suction dispersal device Download PDFInfo
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- CN203990481U CN203990481U CN201420503527.1U CN201420503527U CN203990481U CN 203990481 U CN203990481 U CN 203990481U CN 201420503527 U CN201420503527 U CN 201420503527U CN 203990481 U CN203990481 U CN 203990481U
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Abstract
Polymer negative pressure suction dispersal device of the present utility model belongs to dissolver, by material pot, Material pipeline, jet flow type Water powdery mixer, dissolving tank and control system form, material pot is fixed on bracing frame, below bracing frame, be provided with the high-precision weighing module connecting with control system circuit, the top of material pot is provided with feeding device, below outlet is communicated with frequency conversion screw(-type) feeder entrance, the outlet of frequency conversion screw(-type) feeder is right against loader entrance, and this frequency conversion screw(-type) feeder connects with control system circuit, described loader, Material pipeline, jet flow type Water powdery mixer is communicated with successively, the monosymmetric water inlet of this jet flow type Water powdery mixer is communicated with high service pipe, the pigment mixing head below of jet flow type Water powdery mixer is over against there being dissolving tank, dissolving tank is communicated with the automatic exhaust device connecting with control system circuit.Polymer negative pressure suction dispersal device of the present utility model, simple in structure, easy to use.Reached the adjustable practical purpose of concentration.
Description
Technical field
The utility model relates to a kind of dissolver, refers more particularly to a kind of polymer negative pressure suction dispersal device.
Background technology
Oil is non-renewable resources, and many elephants in east China area are also aging, the remaining viscous crude etc. that is difficult to exploitation that mostly is, this forces people to go more hardy to study new technology in this field of tertiary oil recovery, and having become three, the chemical displacement of reservoir oil adopts one of important stable yields means of stage, and polymer dispersing device is exactly the equipment of standard liquid that the chemical agent for the displacement of reservoir oil is configured to, its character affects the effect of the displacement of reservoir oil.In the view of at present, although there is numerous polymer dispersing devices, mostly cannot allocate as required the solution of different proportionings, be difficult to the object that reaches desirable.
Summary of the invention
The object of the utility model polymer negative pressure suction dispersal device is exactly in order to address the above problem, and propose a kind of fast, configure efficiently and accurately the dispersal device of different proportioning solution.
Polymer negative pressure suction dispersal device of the present utility model, by material pot, Material pipeline, jet flow type Water powdery mixer, dissolving tank and control system form, material pot is fixed on bracing frame, and below bracing frame, be provided with the high-precision weighing module connecting with control system circuit, the top of material pot is provided with feeding device, below outlet is communicated with frequency conversion screw(-type) feeder entrance, the outlet of frequency conversion screw(-type) feeder is right against loader entrance, and this frequency conversion screw(-type) feeder connects with control system circuit, described loader, Material pipeline, jet flow type Water powdery mixer is communicated with successively, the monosymmetric water inlet of this jet flow type Water powdery mixer is communicated with high service pipe, the pigment mixing head below of jet flow type Water powdery mixer faces dissolving tank, dissolving tank is communicated with the automatic exhaust device connecting with control system circuit.
As further improvement of the utility model, the front end of described pigment mixing head is communicated with double helix circulation device, and this double helix flow slowing device is comprised of two parallel spiral pipelines.
As further improvement of the utility model, described dissolving tank is a closing cylinder tank body, and it on binding, has manhole and adaptation has port lid.
As further improvement of the utility model, on the binding of described dissolving tank, be fixed with agitator, agitator through bind and enter in dissolving tank abdomen, it connects with control system circuit.
According to the polymer negative pressure suction dispersal device described in claim 1 or 3, the back cover that it is characterized in that described dissolving tank is turbination, the discharging opening of this back cover is communicated with transmission screw pump, and transmission screw pump connects with transmission motor circuit, and transmission motor connects with control system circuit.
As further improvement of the utility model, described high service pipe is provided with electrical ball valve, electric control valve and the flowmeter being connected with control system circuit respectively.
Polymer negative pressure suction dispersal device of the present utility model, reasonable in design, utilizes venturi principle, and the water flow velocity of nozzle ejection is high, at nozzle exit, formed negative pressure, by polymer suction apparatus, because the effect of negative pressure forms an eddy current, instantaneous with water in pigment mixing head, fully mix, prevented that powder is coalescent, can not form " flake " and glutinous group, and pigment mixing head inclination certain angle, Zai You double helix mechanism imports mixed liquid in dissolving tank; This device in performance, kept dispersibility and matched proportion density adjustable, reducing noise, the output pump life-span increases, operation management is simple and convenient.This device can be realized the accurate outfit of water and material with it to the control of various systems by the parameter setting of control system, has reached the adjustable practical purpose of concentration.
Accompanying drawing explanation
Accompanying drawing 1 is the structure chart of the utility model polymer negative pressure suction dispersal device;
Accompanying drawing 2 is the structure chart of the jet flow type Water powdery mixer of the utility model polymer negative pressure suction dispersal device.
The specific embodiment
Below in conjunction with accompanying drawing 1 and 2 pairs of the utility model polymer negative pressure suction dispersal devices of accompanying drawing, be described further:
Polymer negative pressure suction dispersal device of the present utility model, to be formed by material pot 1, Material pipeline 2, jet flow type Water powdery mixer 3, dissolving tank 4 and control system, material pot 1 is fixed on bracing frame 19 and these bracing frame 19 belows are provided with a plurality of high-precision weighing modules 20 that connect with control system circuit, chemical agent in material pot is by Weighing module 20 meterings on lower margin, and measure by the level meter of installing on material pot and connects with control system circuit, while guaranteeing the quantity not sufficient when material, point out staff to feed in raw material.
The top of material pot 1 is provided with feeding device 8, below outlet is communicated with frequency conversion screw(-type) feeder 5 entrances, frequency conversion screw(-type) feeder outlet 6 is right against loader 7 entrances and this frequency conversion screw(-type) feeder 5 connects with control system circuit, and described loader 7, Material pipeline 2, jet flow type Water powdery mixer 3 are communicated with successively.Described feeding device, can also can have concurrently for auto feed or both for hand stock.
Described jet flow type Water powdery mixer 3 is for having the device of venturi tube structure, and its monosymmetric water inlet 9 is communicated with high service pipe 10, and pigment mixing head 11 is communicated with a double helix flow slowing device 16.Because jet flow type Water powdery mixer 3 utilizes venturi principle, the water flow velocity of nozzle 21 ejections is high, in nozzle 22 exits, formed negative pressure, material is sucked, an eddy current of effect formation due to negative pressure, instantaneous with water, fully mix, prevented that material is coalescent, and pigment mixing head 11 certain angle that can tilt, the double helix unhurried current mechanism 16 being comprised of two parallel spiral pipelines again cushions the mixed liquid penetrating at a high speed, can import in dissolving tank 4, according to different proportioning situations, adopt different parameters, thereby greatly improved the effect being mixed.
Pigment mixing head 11 belows of jet flow type Water powdery mixer 3 are over against there being dissolving tank 4, dissolving tank 4 is communicated with the automatic exhaust device 13 connecting with control system circuit, this dissolving tank 4 is a closing cylinder tank body, it binds and has manhole on 12 and adaptation has port lid 14 and is fixed with agitator 15, agitator 15 through bind 12 and enter in dissolving tank 4 abdomens, it connects with control system circuit; The back cover 17 of dissolving tank 4 is turbination, is communicated with transmission screw pump 18 on the discharging opening of this back cover 17, and transmission screw pump 18 connects with transmission motor circuit, and transmission motor connects with control system circuit.
Polymer negative pressure suction dispersal device of the present utility model, its using method is as follows, the parameter that use need to configure solution arranges control system, after starting device, the frequency conversion screw batcher 5 meeting spiral pushing materials of material pot 1 below are to Material pipeline 2, when pusher is carried out, control system is opened the high pressure electrical ball valve that water pipe 10 is provided with altogether, after electric control valve and flowmeter, supply water again, current at a high speed enter jet flow type Water powdery mixer 3 from water inlet 9 and make and in it, form negative pressure and material is drawn in the cavity of jet flow type Water powdery mixer 3, now material mixes with water, because mixed liquor is from the 3 high speed ejections of jet flow type Water powdery mixer, thereby prevent that in order to slow down its speed splash need to be used for slowing down flow rate of water flow in double helix unhurried current mechanism 16 of pigment mixing head 11 places connection mixed liquid is imported to dissolving tank 4.
Because electrical ball valve, electric control valve and flowmeter are all connected with control system circuit, so flowmeter and electric control valve can link by control system, by the interlock of flowmeter and electric control valve, control and can realize the object that regulates the rate of influx of water according to mass transport amount, reach the water setting, material ratio.The device that linker or other detection liquid level positions can be installed in dissolving tank 4 simultaneously connects with control system circuit, while making liquid level reach certain value, control system can start agitator 15, until solution, mix and reach after the liquid level of setting, restart the transmission screw pump 18 that dissolving tank below discharging opening is communicated with, the solution being mixed is transferred to the device that other utilize this solution, can according to the liquid level of solution, regulate the rotating speed of transmission motor, make within liquid level remains on certain scope.In the process of operation, because weight and the material position of material pot 1 are measured by Weighing module 20 and level meter, when material reaches the minimum of a value of setting, can remind reinforced.
Polymer negative pressure suction dispersal device flowmeter of the present utility model can be selected electromagnetic flowmeter; By the interlock of flowmeter and control valve, control and can realize the object that regulates the rate of influx of water according to dry powder conveying capacity, while starting, control valve standard-sized sheet is guaranteed to the sufficient water yield, while reaching certain flow value, control valve regulates the rate of influx of water to make water, dry powder can enter in proportion agitating device, adjustable dispersibility and matched proportion density.
On polymer negative pressure suction dispersal device dissolving tank of the present utility model, can install anti-return and anti-spilled pipeline or device additional; Below material pot 1, vibrator can be installed, prevent that the material in material pot 1 from hardening; At Material pipeline 4 and loader 7, can add heating device, be used for to material dehumidifying, prevent that the proportioning of material and moisture is inaccurate, the concentration of solution is had a negative impact.
Claims (6)
1. polymer negative pressure is aspirated dispersal device, by material pot (1), Material pipeline (2), jet flow type Water powdery mixer (3), dissolving tank (4) and control system form, it is characterized in that material pot (1) is fixed on bracing frame (19), and be provided with in bracing frame (19) below the high-precision weighing module (20) connecting with control system circuit, the top of material pot (1) is provided with feeding device (8), below outlet is communicated with frequency conversion screw(-type) feeder (5) entrance, the outlet (6) of frequency conversion screw(-type) feeder (5) is right against loader (7) entrance, and this frequency conversion screw(-type) feeder (5) connects with control system circuit, described loader (7), Material pipeline (2), jet flow type Water powdery mixer (3) is communicated with successively, this monosymmetric water inlet of jet flow type Water powdery mixer (3) (9) is communicated with high service pipe (10), pigment mixing head (11) below of jet flow type Water powdery mixer (3) faces dissolving tank (4), dissolving tank (4) is communicated with the automatic exhaust device (13) connecting with control system circuit.
2. polymer negative pressure suction dispersal device according to claim 1, is characterized in that the front end of described pigment mixing head (11) is communicated with double helix circulation device (16), and this double helix flow slowing device (16) is comprised of two parallel spiral pipelines.
3. polymer negative pressure according to claim 1 suction dispersal device, is characterized in that described dissolving tank (4) is a closing cylinder tank body, has manhole and adaptation has port lid (14) on its bind (12).
4. polymer negative pressure according to claim 3 is aspirated dispersal device, it is characterized in that being fixed with agitator (15) on described bind (12), agitator (15) through bind (12) and enter in dissolving tank (4) abdomen, it connects with control system circuit.
5. polymer negative pressure according to claim 1 is aspirated dispersal device, the back cover (17) that it is characterized in that described dissolving tank (4) is turbination, the discharging opening of this back cover (17) is communicated with transmission screw pump (18), transmission screw pump (18) connects with transmission motor circuit, and transmission motor connects with control system circuit.
6. polymer negative pressure suction dispersal device according to claim 1, is characterized in that described high service pipe (10) is provided with electrical ball valve, electric control valve and the flowmeter being connected with control system circuit respectively.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420503527.1U CN203990481U (en) | 2014-09-03 | 2014-09-03 | Polymer negative pressure suction dispersal device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420503527.1U CN203990481U (en) | 2014-09-03 | 2014-09-03 | Polymer negative pressure suction dispersal device |
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| Publication Number | Publication Date |
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| CN203990481U true CN203990481U (en) | 2014-12-10 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN201420503527.1U Active CN203990481U (en) | 2014-09-03 | 2014-09-03 | Polymer negative pressure suction dispersal device |
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Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105854660A (en) * | 2016-06-14 | 2016-08-17 | 钦州市创华工控设备有限公司 | Automatic material dilution system |
| CN109999679A (en) * | 2019-05-05 | 2019-07-12 | 安徽理工大学 | A kind of mealy medicine is evenly dispersed in the liquid phase and mixed dissolution system |
| CN110015738A (en) * | 2019-05-05 | 2019-07-16 | 安徽理工大学 | A kind of mealy medicine quantifies add-on system |
| CN110015737A (en) * | 2019-05-05 | 2019-07-16 | 安徽理工大学 | A kind of quantitative automatic add-on system of powdery flocculation medicament and treatment process |
| CN110026123A (en) * | 2019-05-27 | 2019-07-19 | 安徽理工大学 | A kind of flocculation medicament quantitatively dissolves and uniformly mixes add-on system |
| CN110038476A (en) * | 2019-05-05 | 2019-07-23 | 安徽理工大学 | A kind of jet stream-stirring manifold type powdery flocculation medicament quantifies dispersion mixing system |
| CN112474095A (en) * | 2020-11-24 | 2021-03-12 | 中国海洋大学 | Automatic environment-friendly medicament spraying system, control method and application |
-
2014
- 2014-09-03 CN CN201420503527.1U patent/CN203990481U/en active Active
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105854660A (en) * | 2016-06-14 | 2016-08-17 | 钦州市创华工控设备有限公司 | Automatic material dilution system |
| CN109999679A (en) * | 2019-05-05 | 2019-07-12 | 安徽理工大学 | A kind of mealy medicine is evenly dispersed in the liquid phase and mixed dissolution system |
| CN110015738A (en) * | 2019-05-05 | 2019-07-16 | 安徽理工大学 | A kind of mealy medicine quantifies add-on system |
| CN110015737A (en) * | 2019-05-05 | 2019-07-16 | 安徽理工大学 | A kind of quantitative automatic add-on system of powdery flocculation medicament and treatment process |
| CN110038476A (en) * | 2019-05-05 | 2019-07-23 | 安徽理工大学 | A kind of jet stream-stirring manifold type powdery flocculation medicament quantifies dispersion mixing system |
| CN110026123A (en) * | 2019-05-27 | 2019-07-19 | 安徽理工大学 | A kind of flocculation medicament quantitatively dissolves and uniformly mixes add-on system |
| CN112474095A (en) * | 2020-11-24 | 2021-03-12 | 中国海洋大学 | Automatic environment-friendly medicament spraying system, control method and application |
| CN112474095B (en) * | 2020-11-24 | 2022-01-11 | 中国海洋大学 | Automatic environment-friendly medicament spraying system, control method and application |
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