CN106110924A - Viscous polymer on-line dilution device - Google Patents
Viscous polymer on-line dilution device Download PDFInfo
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- CN106110924A CN106110924A CN201610493796.8A CN201610493796A CN106110924A CN 106110924 A CN106110924 A CN 106110924A CN 201610493796 A CN201610493796 A CN 201610493796A CN 106110924 A CN106110924 A CN 106110924A
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- rotating plate
- rectangle rotating
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- rectangle
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Classifications
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F25/00—Flow mixers; Mixers for falling materials, e.g. solid particles
- B01F25/40—Static mixers
- B01F25/42—Static mixers in which the mixing is affected by moving the components jointly in changing directions, e.g. in tubes provided with baffles or obstructions
- B01F25/43—Mixing tubes, e.g. wherein the material is moved in a radial or partly reversed direction
- B01F25/431—Straight mixing tubes with baffles or obstructions that do not cause substantial pressure drop; Baffles therefor
- B01F25/4315—Straight mixing tubes with baffles or obstructions that do not cause substantial pressure drop; Baffles therefor the baffles being deformed flat pieces of material
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F23/00—Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
- B01F23/40—Mixing liquids with liquids; Emulsifying
- B01F23/47—Mixing liquids with liquids; Emulsifying involving high-viscosity liquids, e.g. asphalt
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F23/00—Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
- B01F23/40—Mixing liquids with liquids; Emulsifying
- B01F23/47—Mixing liquids with liquids; Emulsifying involving high-viscosity liquids, e.g. asphalt
- B01F23/471—Mixing liquids with liquids; Emulsifying involving high-viscosity liquids, e.g. asphalt using a very viscous liquid and a liquid of low viscosity
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F35/00—Accessories for mixers; Auxiliary operations or auxiliary devices; Parts or details of general application
- B01F35/10—Maintenance of mixers
- B01F35/145—Washing or cleaning mixers not provided for in other groups in this subclass; Inhibiting build-up of material on machine parts using other means
- B01F35/1452—Washing or cleaning mixers not provided for in other groups in this subclass; Inhibiting build-up of material on machine parts using other means using fluids
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F35/00—Accessories for mixers; Auxiliary operations or auxiliary devices; Parts or details of general application
- B01F35/80—Forming a predetermined ratio of the substances to be mixed
- B01F35/83—Forming 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
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F2101/00—Mixing characterised by the nature of the mixed materials or by the application field
- B01F2101/2805—Mixing plastics, polymer material ingredients, monomers or oligomers
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- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Engineering & Computer Science (AREA)
- Civil Engineering (AREA)
- Structural Engineering (AREA)
- Dispersion Chemistry (AREA)
Abstract
The invention belongs to production material mixing release field, particularly relate to a kind of viscous polymer on-line dilution device, including housing, described enclosure interior is provided with polymer glue pipeline, waterpipe and mixing duct, pipeline-type high-shearing blender it is provided with in mixing duct, the present invention has can arbitrarily set mixed proportion, automatic cleaning function, this mixing apparatus volume is little, conveniently moving, invest little, without heating, mix homogeneously, achieve online how many mixing how many perfect conditions, thoroughly solve water solublity height and glue the problem that material is difficult to on-line mixing dilution use, save space, investment reduction, energy efficient, can the most arbitrarily regulate mixed proportion, and mix highly uniform.
Description
Technical field
The invention belongs to production material mixing release field, particularly relate to a kind of viscous polymer on-line dilution device.
Background technology
Water-soluble polymer, particularly high viscosity water soluble polymer, water content is highly convenient for transport less, can be significantly
Reduction cost of transportation, it is possible to reduce storage space, but the fewest viscosity of water is the biggest, the biggest dilution mixture of viscosity is the most difficult, has
Employing autoclave mixing method, in whipping process, polymer glue is with liquid in rotation, it is difficult to smash, and incorporation time is long, weak effect,
Heat and can accelerate dilution mixture speed, but be the increase in energy consumption；The employing static mixer mixing also having, but existing market
On static mixer can not mix more than polymer more than 110 centipoises and water, SV type static state therein by blending viscosity well
Clutch, SV type unit is the cylinder assembled by the corrugated plating of certain specification, technical characteristic: best result dissipates degree and is: 1-2
μm, it is adaptable to the liquid-liquid of viscosity≤102 centipoise, liquid-gas, the mixing and emulsifying of gas-gas, reacts, absorbs, extracts, augmentation of heat transfer mistake
Journey.SK type static mixer, unit is formed by the flight assembly welding of the left and right torsion of one channel, its technical performance: best result dissipates
Degree≤10um, is suitable for the high-viscous media of viscosity≤106 centipoise.SX type static mixer, unit by the horizontal stripe intersected by one
Set pattern rule constitutes many X-type unit, technical characteristic: mixing the uneven number of degrees is s X≤1 ~ 5%.It is applicable to viscosity≤104 centipoise
Medium-high viscosity liquid-liquid reactions, mixing, absorption process or produce the mixing of high polymer fluid, course of reaction, when treating capacity is bigger
Using effect is more preferably.SH type static mixer, unit is made up of double hole channel, places flight, adjacent cells diplopore in duct
The orientation in road misplaces 90 °, is provided with fluid reallocation room between unit.Technical characteristic is: best result dissipates degree and is: 1-2mm, liquid-
The unevenness of liquid phase is: s X≤1 ~ 5%.It is applicable to retrofit, plastics, synthetic fibers, the mixing of Kuang Zhideng department, breast
Changing, match colors, be molded the process such as spinning, heat transfer, mixing little to flow requires that the cleaning of high medium-high viscosity (≤106 centipoise) is situated between
Matter is particularly suitable.SL type static mixer, unit is made up of single X-shaped unit according to certain rules the horizontal stripe intersected, and technical characteristic is
Liquid-liquid, liquid-solid phase mix, unevenness coefficient s X≤5%.It is applicable to industry viscosity amount≤106 li such as chemical industry, oil, oils and fats
Pool or the mixing with high polymer medium.Equipment investment is little, energy consumption is low to use static mixer mixing to have, it is possible to achieve online
The advantages such as production, but the on-line dilution that static mixer in the market can not meet big viscosity water-soluble polymer mixes
Close.
Summary of the invention
The present invention is directed to above-mentioned problem of the prior art, it is provided that a kind of high-viscosity polymer on-line dilution device.
In order to achieve the above object, the technical solution used in the present invention is, the invention provides a kind of high-viscosity polymer
On-line dilution device, including housing, described enclosure interior is provided with polymer glue pipeline, waterpipe and mixing duct, described
It is disposed with the first purge valve, high viscosity delivery pump, the first motorized adjustment along glue flow direction on polymer glue pipeline
Valve and the first Intelligent flowmeter, described waterpipe is disposed with in water (flow) direction high-pressure hydraulic pump, the second electric control valve
With the second Intelligent flowmeter, described mixing duct is disposed with pipeline-type high-shearing mixing along mixed liquor flow direction
Device, bifurcated passage and the 3rd purge valve, between pipeline and the first purge valve and the high viscosity delivery pump of described high-pressure hydraulic pump front end
Pipeline on be provided with connecting pipe, described polymer glue tube is additionally provided with first be arranged in parallel with high viscosity delivery pump
Parallel pipeline, described waterpipe is additionally provided with the second parallel pipeline being arranged in parallel with high-pressure hydraulic pump, on described connecting pipe
Be provided with the second purge valve, on described first parallel pipeline and the second parallel pipeline on be respectively arranged with the first pressure-regulating and pressuring-limiting valve and
Second pressure-regulating and pressuring-limiting valve, described enclosure interior is additionally provided with PLC.
As preferably, pipeline-type high-shearing blender includes blender pipeline and is arranged on the spy of blender pipe interior
Metal blade group processed, described special metal blade group includes the first rectangle rotating plate, is arranged on the second of the first rectangle rotating plate top
Rectangle rotating plate, it is arranged on the 3rd rectangle rotating plate at the second rectangle rotating plate top and is arranged on the 4th of the 3rd rectangle rotating plate top
Rectangle rotating plate, described first rectangle rotating plate, the second rectangle rotating plate, the 3rd rectangle rotating plate and the 4th rectangle rotating plate are in structure and size
On the most identical, described second rectangle rotating plate and the first rectangle rotating plate are vertically arranged, described 3rd rectangle rotating plate and the second rectangle rotation
Plate is vertically arranged, and the 4th rectangle rotating plate and the 3rd rectangle rotating plate are vertically arranged.
As preferably, described second rectangle rotating plate rotates clockwise or counter-clockwise 90 ° relative to the first rectangle rotating plate and sets
Putting, the 3rd rectangle rotating plate rotates clockwise or counter-clockwise 90 ° of settings relative to the second rectangle rotating plate, and the 4th rectangle rotating plate is relative
90 ° of settings are rotated clockwise or counter-clockwise in the 3rd rectangle rotating plate.
As preferably, described high-pressure hydraulic pump is that pressure is more than or equal to the centrifugal pump of 0.4MPa, impeller pump, axial-flow pump, plunger
Any one in pump, reciprocating pump and screw pump.
As preferably, it is that pressure is more than the impeller pump of 0.4MPa, plunger displacement pump, reciprocating pump, sieve that described height glues material-handling pump
Any one in thatch pump and screw pump.
As preferably, described Intelligent flowmeter is intelligent gear effusion meter, electromagnetic flowmeter, mass flowmenter, vortex street stream
Any one of gauge and metal pipe float flow meter.
As preferably, described bifurcated passage is provided with the 4th purge valve.
Compared with prior art, advantages of the present invention and good effect are,
The present invention has can arbitrarily set mixed proportion, and automatic cleaning function, this mixing apparatus volume is little, conveniently moving, throwing
Provide little, it is not necessary to heat, mix homogeneously, it is achieved that online by how many mixing how many perfect conditions, thoroughly solve water solublity height and glue
Material is difficult to the problem that on-line mixing dilution uses, and saves space, investment reduction, energy efficient, can the most arbitrarily adjust
Joint mixed proportion, and mix highly uniform.
Accompanying drawing explanation
In order to be illustrated more clearly that the technical scheme of the embodiment of the present invention, required use in embodiment being described below
Accompanying drawing be briefly described, it should be apparent that, below describe in accompanying drawing be some embodiments of the present invention, for ability
From the point of view of the those of ordinary skill of territory, on the premise of not paying creative work, it is also possible to obtain other according to these accompanying drawings
Accompanying drawing.
Fig. 1 is the component locations sketch of the viscous polymer on-line dilution device in embodiment 1；
Fig. 2 is the perspective view of the pipeline-type high-shearing blender in embodiment 1；
Fig. 3 is the perspective view of the special metal blade group (containing four rectangle rotating plates) in embodiment 1；
Fig. 4 is the perspective view of the square metal sheet in embodiment 1；
Fig. 5 to Fig. 8 is respectively the front view of rectangle rotating plate, left view, top view and perspective view；
Fig. 9 is the perspective view of the clearance sheet metal impact style in embodiment 1；
Figure 10 is the perspective view of the clearance sheet metal impact style (another kind of position) in embodiment 1；
In the most each figure, 1, high viscosity delivery pump；2, high-pressure hydraulic pump；3, pipeline-type high-shearing blender；31, blender pipeline；
32, special metal blade group；41, the first Intelligent flowmeter；42, the second Intelligent flowmeter；51, the first purge valve；52, second is clear
Wash valve；53, the first electric controller；54, the 3rd purge valve；55, the 4th purge valve；56, the second pressure-regulating and pressuring-limiting valve；57, first
Pressure-regulating and pressuring-limiting valve；58, the second electric control valve；6, polymer glue pipeline；7, waterpipe；8, PLC；9, square metal
Sheet；91, rectangular channel；10, semi-circular tube mould；11, semicircle mould；12, connecting pipe；13, bifurcated passage；141, first is in parallel
Pipeline；142, the second parallel pipeline.
Detailed description of the invention
In order to be more clearly understood that the above-mentioned purpose of the present invention, feature and advantage, below in conjunction with the accompanying drawings and embodiment
The present invention will be further described.It should be noted that in the case of not conflicting, in embodiments herein and embodiment
Feature can be mutually combined.
Elaborate a lot of detail in the following description so that fully understanding the present invention, but, the present invention also may be used
Being different from other modes described here with employing to implement, therefore, the present invention is not limited to the concrete of description described below
The restriction of embodiment.
Embodiment 1, as it is shown in figure 1, the present invention devises a kind of high-viscosity polymer on-line dilution device, including housing,
Housing plays parcel and the effect of protection internal part, because the device designed by the present invention is to dilute full-bodied polymerization
Thing, the i.e. inside at housing are provided with polymer glue pipeline 6, waterpipe 7 and mixing duct, the connection side of above-mentioned three kinds of pipelines
Formula is, connects with mixing duct after polymer glue pipeline 6 and waterpipe 7 parallel connection again, and wherein mixing duct is high viscosity polymerization
The dilution position of thing core, in order to embody the difference of the present invention and prior art, this just mixing duct this part, for
Make high-viscosity polymer and water at polymer glue pipeline 6 and waterpipe 7 through out-of-date, can have the best condition to enter into mixing
Dilution in pipeline；Inventor has done following design at polymer glue pipeline 6 in polymer glue pipeline 6 and waterpipe 7
On, along glue flowing direction set gradually on polymer glue pipeline 6 first purge valve 51, high viscosity delivery pump 1,
First electric control valve and the first Intelligent flowmeter 41, purge valve be disposed to fixed time cleaning pipeline, make in pipeline always
Keeping clear and be not easily blocked, being provided with of high viscosity delivery pump 1 is to provide power to high-viscosity polymer glue, improves and passes
Defeated effect, the effect of electric control valve is the flow controlling pipe interpolymer glue, and Intelligent flowmeter is then to monitor in pipe
Flow, and by data feedback to PLC, then PLC controls electric control valve, improves or reduces flow；Along water (flow) direction
Waterpipe 7 has set gradually high-pressure hydraulic pump the 2, second electric control valve and the second Intelligent flowmeter 42, the mesh of high-pressure hydraulic pump 2
Be in order to current provide power, relative to being provided with purge valve, waterpipe 7 on polymer glue pipeline 6 less on waterpipe 7
Other parts arrange and polymer glue pipeline 6 other parts arrange that to act on be the same, be only provided in difference
Pipeline on；It is provided with on the pipeline between pipeline and the first purge valve 51 and high viscosity delivery pump 1 in high-pressure hydraulic pump 2 front end
Connecting pipe 12, the purpose arranging connecting pipe 12 is water in waterpipe 7 to be transported to polymer glue pipeline 6 be carried out pipe
Road, is provided with the second purge valve 52 on unicom pipeline；Polymer glue tube is additionally provided with in parallel with high viscosity delivery pump 1
The first parallel pipeline 141 arranged, waterpipe 7 is additionally provided with the second parallel pipeline 142 being arranged in parallel with high-pressure hydraulic pump 2,
The two parallel pipeline is provided with and is provided to alleviate high viscosity delivery pump 1 and high-pressure hydraulic pump 2 and arrange, in order to make setting
Parallel pipeline can work the most automatically, is provided with pressure-regulating and pressuring-limiting valve at parallel pipeline, arranges pressure-regulating and pressuring-limiting valve
Purpose be contemplated to the pressure size monitoring official road from liquid feeding end to high viscosity delivery pump 1, and come according to pressure
Controlling whether to use parallel pipeline, in order to enable this device intelligent and automatization, inventor is also provided with PLC 8,
I.e. control each parts automatically to work.
Due to the core position that mixing duct is this device, say mixing duct in detail below, mixed on mixing duct
Closing liquid flow direction and be disposed with pipeline-type high-shearing blender 3, bifurcated passage 13 and the 3rd purge valve 54, the present invention is at this
In individual core position, focused protection is exactly pipeline-type high-shearing blender 3, as shown in Fig. 2, Fig. 3, Fig. 5, Fig. 6, Fig. 7 and Fig. 8,
Duct type shear mixer (as shown in Figure 2) includes blender pipeline 31 and is arranged on the special gold within blender pipeline 31
Belong to blade group 32(as shown in Figure 3), the effect of blender pipeline 31 has two kinds, and one is to provide blending space to mixed liquor, and two are
Supporting special metal blade group 32, this special metal blade group 32 is the critical component of this device diluted polymer glue, system gold
Belong to blade group to include the first rectangle rotating plate, the second rectangle rotating plate being arranged on the first rectangle rotating plate top, be arranged on the second rectangle
The 3rd rectangle rotating plate at rotating plate top and be arranged on the 4th rectangle rotating plate at the 3rd rectangle rotating plate top, the second rectangle rotating plate with
First rectangle rotating plate is vertically arranged, and the 3rd rectangle rotating plate and the second rectangle rotating plate are vertically arranged, the 4th rectangle rotating plate and the 3rd square
Shape rotating plate is vertically arranged, and the second rectangle rotating plate rotates clockwise or counter-clockwise 90 ° of settings relative to the first rectangle rotating plate, and the 3rd
Rectangle rotating plate rotates clockwise or counter-clockwise 90 ° of settings relative to the second rectangle rotating plate, and the 4th rectangle rotating plate is relative to the 3rd
Rectangle rotating plate rotates clockwise or counter-clockwise 90 ° of settings, and if so arranging, i.e. four rectangle rotating plates are a circulation group,
Rectangle rotating plate is then carried out bending by the square plate (as shown in Figure 4) with rectangular channel 91 along a diagonal and makes.
Say the method for designing of special metal blade group 32 in our company's duct type shear mixer in detail below.
The making of our company's pipeline-type high-shearing blender 3: shear the 304 stainless steel rectangular blocks of 25 pieces of 80*80*2, in side
On shape block, along the direction on parallel one side, a length of 70mm width is opened in the position of distance rectangular edges 8mm is the opening of 8mm, parallel this
Opening is successively toward under shed, and concrete shape as shown in Figure 4, makes 25 pieces.
The making of metal blade: in the diel that square metal sheet 9 is placed on pipeline interior diameter used is 72mm, metal
Be placed as square metal sheet 9 diagonal and semi-circular tube mould 10 diameter of sheet overlap, then with the semicircle mould that external diameter is 72
11 punching presses, impact style is as shown in Figure 9 and Figure 10.
The connection of metal blade: long for first piece of rectangular metal sheet (the first rectangle rotating plate can be referred to as) rectangular top opening
Limit becomes horizontal positioned, and whole sheet metal is vertical, then second piece of rectangular metal sheet (the second rectangle rotating plate can be referred to as) rectangle
The long limit of open top also becomes horizontal positioned, whole sheet metal to be vertical, then makes two panels sheet metal by the opposing placement of flexibility, improves
Second piece, make the center, top at corresponding first piece of the following center of second piece, make the top of first piece and second piece following
Intersection point tangent line projects into an angle of 90 degrees, welds together after good；The placement of the 3rd piece is identical with first piece, and the 3rd piece of raising is made
The central point of the corresponding second piece of top of the following central point of the 3rd piece, makes the top of second piece and the following intersection point of the 3rd piece cut
Line projection becomes an angle of 90 degrees, corresponding good welding；The placement of the 4th piece is identical with second piece, improves the 4th piece and makes in the 4th piece following
The top central point that heart point is corresponding 3rd piece, welds after correspondence, concrete welding effect as it is shown on figure 3, the like, 25 pieces
Connect complete.
In order to make the effect in the present invention more preferable, inventor also has the following description, high-pressure hydraulic pump 2 to be more than or equal to for pressure
Any one in the centrifugal pump of 0.4MPa, impeller pump, axial-flow pump, plunger displacement pump, reciprocating pump and screw pump, high viscous material-handling pump
For pressure more than any one in the impeller pump of 0.4MPa, plunger displacement pump, reciprocating pump, lobe pump and screw pump, Intelligent flowmeter
Any one for intelligent gear effusion meter, electromagnetic flowmeter, mass flowmenter, vortex-shedding meter and metal pipe float flow meter
Kind, above explanation Dou Shi our company is through substantial amounts of test, and a kind of situation being currently in use now；On bifurcated passage 13
It is provided with the 4th purge valve 55.
All of purge valve, electric control valve and the Intelligent flowmeter effect and the size that arrange in the present invention are all identical
, it is intended merely to more preferable demarcation of location, adds the one the second or the 3rd at purge valve, electric control valve and Intelligent flowmeter
Deng.
Will be connected with PLC 8 by each parts, its purpose is contemplated to be that this device can automatically process
Problem.
Say the operation principle of this device, switch on power, PLC 8 inputs control instruction, such as water solublity
Polymer flow rate is 200L/min, and the flow of water is 7300L/min, works 8 hours continuously, press start key after system start-up,
System starts, first purge valve the 51, first electric control valve, the second electric control valve, the 3rd purge valve 54 open simultaneously,
Second purge valve the 52, the 4th purge valve 55 is closed；Water pump is opened, and after 2s time delay, high viscous thing delivery pump starts, and work was by 8 hours
Time, the first purge valve 51 closes, and the 4th purge valve 55 is opened, and continues 3 seconds, and the second purge valve 52 is opened, the 3rd purge valve 54
Close, clean 10 seconds, motor autostop, shut down 3 seconds, all valve Close Alls.
Advantage of the present invention: have rectangular aperture on square metal blade, is striking out curved surface, both can change fluid flowing
Direction, significantly increases again the opening shearing to high viscosity water soluble polymer, and dilution mixture has special effect, diluent
In no longer there is the big viscosity glue of in bulk, dilution mixture very thorough, and blender loss in head is less than existing market
On the various static mixers of same mixed cell number, equipment investment is minimum, and equipment volume is minimum, it is not necessary to reheat, joint
The about energy, reduces producing cost, decreases waste, therefore have fabulous dissemination.
The above, be only presently preferred embodiments of the present invention, is not the restriction that the present invention makees other form, appoints
What those skilled in the art changed possibly also with the technology contents of the disclosure above or be modified as equivalent variations etc.
Effect embodiment is applied to other field, but every without departing from technical solution of the present invention content, according to the technical spirit of the present invention
Any simple modification, equivalent variations and the remodeling being made above example, still falls within the protection domain of technical solution of the present invention.
Claims (7)
1. a viscous polymer on-line dilution device, including housing, described enclosure interior be provided with polymer glue pipeline,
Waterpipe and mixing duct, it is characterised in that on described polymer glue pipeline, be disposed with first along glue flow direction
Purge valve, high viscosity delivery pump, the first electric control valve and the first Intelligent flowmeter, described waterpipe depends in water (flow) direction
Secondary it is provided with high-pressure hydraulic pump, the second electric control valve and the second Intelligent flowmeter, described mixing duct flows along mixed liquor
Direction is disposed with pipeline-type high-shearing blender, bifurcated passage and the 3rd purge valve, the pipeline of described high-pressure hydraulic pump front end
And it is provided with connecting pipe on the pipeline between the first purge valve and high viscosity delivery pump, described polymer glue tube also sets up
There is the first parallel pipeline being arranged in parallel with high viscosity delivery pump, described waterpipe is additionally provided with and is arranged in parallel with high-pressure hydraulic pump
The second parallel pipeline, described connecting pipe is provided with the second purge valve, on described first parallel pipeline and the second parallel transistor
Being respectively arranged with the first pressure-regulating and pressuring-limiting valve and the second pressure-regulating and pressuring-limiting valve on road, described enclosure interior is additionally provided with PLC.
Viscous polymer on-line dilution device the most according to claim 1, it is characterised in that described pipeline-type high-shearing
Blender includes blender pipeline and is arranged on the special metal blade group of blender pipe interior, described special metal blade
Group includes the first rectangle rotating plate, the second rectangle rotating plate being arranged on the first rectangle rotating plate top, is arranged on the second rectangle rotating plate top
The 3rd rectangle rotating plate in portion and be arranged on the 4th rectangle rotating plate at the 3rd rectangle rotating plate top, described first rectangle rotating plate,
Two rectangle rotating plates, the 3rd rectangle rotating plate and the 4th rectangle rotating plate are the most identical in structure with size, described second rectangle rotating plate with
First rectangle rotating plate is vertically arranged, and described 3rd rectangle rotating plate and the second rectangle rotating plate are vertically arranged, the 4th rectangle rotating plate and
Three rectangle rotating plates are vertically arranged.
Viscous polymer on-line dilution device the most according to claim 2, it is characterised in that described second rectangle rotating plate
Rotating clockwise or counter-clockwise 90 ° of settings relative to the first rectangle rotating plate, the 3rd rectangle rotating plate is relative to the second rectangle rotating plate
Rotating clockwise or counter-clockwise 90 ° of settings, the 4th rectangle rotating plate revolves clockwise or counter-clockwise relative to the 3rd rectangle rotating plate
Turn 90 ° of settings.
Viscous polymer on-line dilution device the most according to claim 3, it is characterised in that described high-pressure hydraulic pump is pressure
Power is more than or equal to any one in the centrifugal pump of 0.4MPa, impeller pump, axial-flow pump, plunger displacement pump, reciprocating pump and screw pump.
Viscous polymer on-line dilution device the most according to claim 4, it is characterised in that described height glues material conveying
Pump be pressure be more than in the impeller pump of 0.4MPa, plunger displacement pump, reciprocating pump, lobe pump and screw pump any one.
Viscous polymer on-line dilution device the most according to claim 5, it is characterised in that described Intelligent flowmeter is
Any one of intelligent gear effusion meter, electromagnetic flowmeter, mass flowmenter, vortex-shedding meter and metal pipe float flow meter.
Viscous polymer on-line dilution device the most according to claim 6, it is characterised in that set on described bifurcated passage
It is equipped with the 4th purge valve.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
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| CN201610493796.8A CN106110924A (en) | 2016-06-30 | 2016-06-30 | Viscous polymer on-line dilution device |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610493796.8A CN106110924A (en) | 2016-06-30 | 2016-06-30 | Viscous polymer on-line dilution device |
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| CN106110924A true CN106110924A (en) | 2016-11-16 |
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| CN201610493796.8A Pending CN106110924A (en) | 2016-06-30 | 2016-06-30 | Viscous polymer on-line dilution device |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111729530A (en) * | 2020-05-25 | 2020-10-02 | 西北工业大学 | Hydraulic self-driven resistance-reducing mucus dilution and release device |
| CN114797602A (en) * | 2022-04-08 | 2022-07-29 | 南京工业大学 | Novel mixer suitable for high viscous fluid mixes |
Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3953002A (en) * | 1973-09-21 | 1976-04-27 | England Jr Herbert C | Motionless mixing device |
| US5985045A (en) * | 1994-10-24 | 1999-11-16 | Motorola, Inc. | Process for polishing a semiconductor substrate |
| CN201036734Y (en) * | 2006-12-26 | 2008-03-19 | 黎泽荣 | Continuous unpowered mixer |
| CN203253370U (en) * | 2013-04-22 | 2013-10-30 | 沈阳化工大学 | Parallel double-spiral plate type static mixer |
| CN103446901A (en) * | 2013-08-22 | 2013-12-18 | 北京化工大学 | Hollow rotor provided with grid bars and helical blades |
| CN203764205U (en) * | 2014-01-09 | 2014-08-13 | 北京燕山和成橡塑新材料有限公司 | Material homogenizing system |
| CN203764194U (en) * | 2014-04-04 | 2014-08-13 | 佛山市海天(高明)调味食品有限公司 | Quick mixing device |
-
2016
- 2016-06-30 CN CN201610493796.8A patent/CN106110924A/en active Pending
Patent Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3953002A (en) * | 1973-09-21 | 1976-04-27 | England Jr Herbert C | Motionless mixing device |
| US5985045A (en) * | 1994-10-24 | 1999-11-16 | Motorola, Inc. | Process for polishing a semiconductor substrate |
| CN201036734Y (en) * | 2006-12-26 | 2008-03-19 | 黎泽荣 | Continuous unpowered mixer |
| CN203253370U (en) * | 2013-04-22 | 2013-10-30 | 沈阳化工大学 | Parallel double-spiral plate type static mixer |
| CN103446901A (en) * | 2013-08-22 | 2013-12-18 | 北京化工大学 | Hollow rotor provided with grid bars and helical blades |
| CN203764205U (en) * | 2014-01-09 | 2014-08-13 | 北京燕山和成橡塑新材料有限公司 | Material homogenizing system |
| CN203764194U (en) * | 2014-04-04 | 2014-08-13 | 佛山市海天(高明)调味食品有限公司 | Quick mixing device |
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| Publication number | Priority date | Publication date | Assignee | Title |
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| CN111729530A (en) * | 2020-05-25 | 2020-10-02 | 西北工业大学 | Hydraulic self-driven resistance-reducing mucus dilution and release device |
| CN114797602A (en) * | 2022-04-08 | 2022-07-29 | 南京工业大学 | Novel mixer suitable for high viscous fluid mixes |
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