CN109966963A - Aqueous negative oxygen ion interior wall paint production-process systems and its process recipe - Google Patents
Aqueous negative oxygen ion interior wall paint production-process systems and its process recipe Download PDFInfo
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- CN109966963A CN109966963A CN201910268457.3A CN201910268457A CN109966963A CN 109966963 A CN109966963 A CN 109966963A CN 201910268457 A CN201910268457 A CN 201910268457A CN 109966963 A CN109966963 A CN 109966963A
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- lotion
- dispersion
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- 239000003973 paint Substances 0.000 title claims abstract description 17
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 10
- 239000001301 oxygen Substances 0.000 title claims abstract description 10
- 229910052760 oxygen Inorganic materials 0.000 title claims abstract description 10
- 238000000034 method Methods 0.000 title claims description 23
- 230000008569 process Effects 0.000 title claims description 22
- 238000000576 coating method Methods 0.000 claims abstract description 137
- 239000011248 coating agent Substances 0.000 claims abstract description 136
- 239000007788 liquid Substances 0.000 claims abstract description 123
- 239000006185 dispersion Substances 0.000 claims abstract description 108
- 239000006210 lotion Substances 0.000 claims abstract description 80
- 238000002347 injection Methods 0.000 claims abstract description 40
- 239000007924 injection Substances 0.000 claims abstract description 40
- 230000002045 lasting effect Effects 0.000 claims abstract description 10
- 230000001804 emulsifying effect Effects 0.000 claims abstract description 5
- 238000003756 stirring Methods 0.000 claims description 54
- 239000012530 fluid Substances 0.000 claims description 23
- 230000001360 synchronised effect Effects 0.000 claims description 19
- 238000009826 distribution Methods 0.000 claims description 16
- 230000009471 action Effects 0.000 claims description 9
- 239000007921 spray Substances 0.000 claims description 8
- 239000002518 antifoaming agent Substances 0.000 claims description 7
- 125000004122 cyclic group Chemical group 0.000 claims description 6
- 238000010438 heat treatment Methods 0.000 claims description 6
- 230000010354 integration Effects 0.000 claims description 6
- 230000000694 effects Effects 0.000 claims description 5
- 230000009467 reduction Effects 0.000 claims description 5
- 239000000839 emulsion Substances 0.000 claims description 4
- 238000005516 engineering process Methods 0.000 claims description 4
- 238000007667 floating Methods 0.000 claims description 3
- 238000010008 shearing Methods 0.000 claims description 3
- 230000007613 environmental effect Effects 0.000 claims description 2
- 239000000463 material Substances 0.000 claims description 2
- 230000001681 protective effect Effects 0.000 claims description 2
- 238000010422 painting Methods 0.000 claims 2
- 239000007789 gas Substances 0.000 claims 1
- 238000005086 pumping Methods 0.000 claims 1
- 238000004080 punching Methods 0.000 claims 1
- 238000000926 separation method Methods 0.000 claims 1
- 238000010586 diagram Methods 0.000 description 4
- -1 oxygen ion Chemical class 0.000 description 4
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 2
- 150000001450 anions Chemical class 0.000 description 2
- 150000002500 ions Chemical class 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 230000000149 penetrating effect Effects 0.000 description 2
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 description 1
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical compound [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 150000007513 acids Chemical class 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 229910052791 calcium Inorganic materials 0.000 description 1
- 239000011575 calcium Substances 0.000 description 1
- 150000001785 cerium compounds Chemical class 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 239000007822 coupling agent Substances 0.000 description 1
- 238000005034 decoration Methods 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 235000019441 ethanol Nutrition 0.000 description 1
- GNPVGFCGXDBREM-UHFFFAOYSA-N germanium atom Chemical compound [Ge] GNPVGFCGXDBREM-UHFFFAOYSA-N 0.000 description 1
- 230000036541 health Effects 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
- 229920001909 styrene-acrylic polymer Polymers 0.000 description 1
- 239000011032 tourmaline Substances 0.000 description 1
- 229940070527 tourmaline Drugs 0.000 description 1
- 229910052613 tourmaline Inorganic materials 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Classifications
-
- 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
- B01F25/20—Jet mixers, i.e. mixers using high-speed fluid streams
- B01F25/21—Jet mixers, i.e. mixers using high-speed fluid streams with submerged injectors, e.g. nozzles, for injecting high-pressure jets into a large volume or into mixing chambers
- B01F25/212—Jet mixers, i.e. mixers using high-speed fluid streams with submerged injectors, e.g. nozzles, for injecting high-pressure jets into a large volume or into mixing chambers the injectors being movable, e.g. rotating
-
- 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
- B01F25/50—Circulation mixers, e.g. wherein at least part of the mixture is discharged from and reintroduced into a receptacle
- B01F25/52—Circulation mixers, e.g. wherein at least part of the mixture is discharged from and reintroduced into a receptacle with a rotary stirrer in the recirculation tube
-
- 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
- B01F25/50—Circulation mixers, e.g. wherein at least part of the mixture is discharged from and reintroduced into a receptacle
- B01F25/54—Circulation mixers, e.g. wherein at least part of the mixture is discharged from and reintroduced into a receptacle provided with a pump inside the receptacle to recirculate the material within the receptacle
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F27/00—Mixers with rotary stirring devices in fixed receptacles; Kneaders
- B01F27/21—Mixers with rotary stirring devices in fixed receptacles; Kneaders characterised by their rotating shafts
- B01F27/2122—Hollow shafts
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F27/00—Mixers with rotary stirring devices in fixed receptacles; Kneaders
- B01F27/80—Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a substantially vertical axis
- B01F27/81—Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a substantially vertical axis the stirrers having central axial inflow and substantially radial outflow
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F27/00—Mixers with rotary stirring devices in fixed receptacles; Kneaders
- B01F27/80—Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a substantially vertical axis
- B01F27/84—Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a substantially vertical axis with two or more stirrers rotating at different speeds or in opposite directions about the same axis
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F27/00—Mixers with rotary stirring devices in fixed receptacles; Kneaders
- B01F27/80—Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a substantially vertical axis
- B01F27/90—Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a substantially vertical axis with paddles or arms
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F27/00—Mixers with rotary stirring devices in fixed receptacles; Kneaders
- B01F27/80—Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a substantially vertical axis
- B01F27/94—Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a substantially vertical axis with rotary cylinders or cones
-
- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09D—COATING COMPOSITIONS, e.g. PAINTS, VARNISHES OR LACQUERS; FILLING PASTES; CHEMICAL PAINT OR INK REMOVERS; INKS; CORRECTING FLUIDS; WOODSTAINS; PASTES OR SOLIDS FOR COLOURING OR PRINTING; USE OF MATERIALS THEREFOR
- C09D125/00—Coating compositions based on homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by an aromatic carbocyclic ring; Coating compositions based on derivatives of such polymers
- C09D125/02—Homopolymers or copolymers of hydrocarbons
- C09D125/04—Homopolymers or copolymers of styrene
- C09D125/08—Copolymers of styrene
- C09D125/14—Copolymers of styrene with unsaturated esters
-
- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09D—COATING COMPOSITIONS, e.g. PAINTS, VARNISHES OR LACQUERS; FILLING PASTES; CHEMICAL PAINT OR INK REMOVERS; INKS; CORRECTING FLUIDS; WOODSTAINS; PASTES OR SOLIDS FOR COLOURING OR PRINTING; USE OF MATERIALS THEREFOR
- C09D7/00—Features of coating compositions, not provided for in group C09D5/00; Processes for incorporating ingredients in coating compositions
- C09D7/40—Additives
- C09D7/60—Additives non-macromolecular
- C09D7/61—Additives non-macromolecular inorganic
-
- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09D—COATING COMPOSITIONS, e.g. PAINTS, VARNISHES OR LACQUERS; FILLING PASTES; CHEMICAL PAINT OR INK REMOVERS; INKS; CORRECTING FLUIDS; WOODSTAINS; PASTES OR SOLIDS FOR COLOURING OR PRINTING; USE OF MATERIALS THEREFOR
- C09D7/00—Features of coating compositions, not provided for in group C09D5/00; Processes for incorporating ingredients in coating compositions
- C09D7/40—Additives
- C09D7/60—Additives non-macromolecular
- C09D7/63—Additives non-macromolecular organic
-
- 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
- B01F2101/30—Mixing paints or paint ingredients, e.g. pigments, dyes, colours, lacquers or enamel
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
- C08K3/00—Use of inorganic substances as compounding ingredients
- C08K3/02—Elements
- C08K3/08—Metals
- C08K2003/0831—Gold
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
- C08K2201/00—Specific properties of additives
- C08K2201/011—Nanostructured additives
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Life Sciences & Earth Sciences (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Wood Science & Technology (AREA)
- Organic Chemistry (AREA)
- Inorganic Chemistry (AREA)
- Nozzles (AREA)
Abstract
The invention discloses aqueous negative oxygen ion interior wall paint production-process systems, including vertical columnar coating dispersion tank, the top side of the coating dispersion tank is provided with feed inlet, disperse chamber in the tank of the coating dispersion tank for columnar coating, it further include coating delivery line, the liquid feeding end of the coating delivery line, which is connected to the coating, to be dispersed bottom of chamber portion, to be equipped with solenoid valve and drawing liquid pump on the coating delivery line；The jet stream that the spout of each injection pipe is gushed out first passes through the intracavitary chamber portion of dispersive jet, then it injects again in the intracavitary liquid level of dispersive jet, the jet stream of lasting splashing impact type is formed at the liquid level for keeping dispersive jet intracavitary, the splash jet stream can also collide the lotion at the intracavitary liquid level of dispersive jet repeatedly, and then realize that the fining dispersion of the lotion intracavitary to dispersive jet, emulsifying effectiveness are finer and smoother.
Description
Technical field
The invention belongs to coating process fields.
Background technique
As living standards of the people are continuously improved, living environment constantly improves, and indoor decorating is increasingly luxurious, beautiful
Meanwhile it is more and more because the problem of indoor pollution caused by fitting up influences human health, not only there is negative ion paint decoration to protect
Shield effect, and sustainable release anion achieve the purpose that improve environment to increase the concentration of anion in air；It is negative
Dispersing technology of the ion coating in producing process is most important, and often dispersion effect is bad for existing dispersing apparatus, final to produce
Product are not fine and smooth enough.
Summary of the invention
Goal of the invention: in order to overcome the deficiencies in the prior art, the present invention provides a kind of coating more refinement of dispersion
Greasy aqueous negative oxygen ion interior wall paint production-process systems.
Technical solution: to achieve the above object, aqueous negative oxygen ion interior wall paint production-process systems of the invention, including it is vertical
The columnar coating dispersion tank of formula, the top side of the coating dispersion tank are provided with feed inlet, the tank of the coating dispersion tank
It is interior to disperse chamber for columnar coating, it further include coating delivery line, the liquid feeding end of the coating delivery line is connected to the coating dispersion
Bottom of chamber portion is equipped with solenoid valve and drawing liquid pump on the coating delivery line；The centre of the coating dispersion chamber, which is provided with, to be followed
Ring liquid pump；It further include lateral liquid pump support, one end of the liquid pump support is fixedly connected with the coating dispersion top tank structure, described
Recycle liquid pump is fixedly mounted on the other end of the liquid pump support.
Further, the upper end liquid feeding end of the recycle liquid pump is liquid inlet joint, the lower end outlet end of the recycle liquid pump
For liquid outlet connector；Concentric be provided in the top of the recycle liquid pump is rotated into fluid cylinder, and described be rotated under fluid cylinder brings out liquid
End is socketed by first bearing and liquid inlet joint rotation；The upper end for being rotated into fluid cylinder blocks setting, and the rotation
The concentric integration in the upper end of feed liquor cylinder is connected with shaft, the bearing hole at the top of the shaft and the coating dispersion tank on wall body
Seat is rotatablely connected by second bearing；The top of the shaft is provided with belt synchronizing wheel；Pacify at the top of the coating dispersion tank
Equipped with synchronous translator, the synchronous translator is drivingly connected by synchronous belt and the belt synchronizing wheel；The rotation feed liquor
Circumferentially array is fixedly connected with several lateral stirring cantilevers to the surrounding of cylinder, and the end of each stirring cantilever is curved downward vertically
Song, and the end of each stirring cantilever hangs and is fixedly connected with stirring blade；The inside of each stirring cantilever is all provided with
Be equipped with liquid-conveying ducts, one end of each liquid-conveying ducts be connected to described in be rotated into the tube inner chamber of fluid cylinder；Each stirring cantilever
End be respectively provided with liquid sucting port, each liquid sucting port is respectively communicated with the other end of the liquid-conveying ducts；Each equal position of the liquid sucting port
Disperse in the coating intracavitary；The inner wall of the coating dispersion chamber, which also spirals, is provided with resistance heating wire.
Further, the lower section of the recycle liquid pump is concentric is provided with spin rotor, and the upper end of the spin rotor is same
Axle center integration is connected with feed liquor column casing, and the feed liquor column casing is socketed the liquid outlet connector by 3rd bearing rotation；It is described from
Gyrator is the open cylindricality cover structure in lower end, the spin rotor include plate-like cover top and cricoid faceshield side wall, institute
The bottom of chamber spacing of the bottom end and coating dispersion chamber of stating faceshield side wall is arranged；The also concentric one in the inside of the spin rotor
Change is provided with separator disc, and the diffluence room of plate-like is formed between the separator disc and the cover top, and the lower end of the feed liquor column casing is same
Axle center is connected to the diffluence room；The downside of the separator disc forms columnar dispersive jet chamber, the lower section portion of the faceshield side wall
Circumferentially array hollow out is provided with several liquid pass holes；The injection of several lateral attitudes is fixedly connected on the downside of the separator disc
Pipe, each injection pipe is along the separator disc circumferentially array distribution, and the root of each injection pipe is connected to the shunting
Room, each injection pipe lower end are provided with the spout of inclined injection direction, the recoil strength of the sprayed liquid of each spout
The spin rotor can be driven to rotate clockwise；If circumferentially array stationary distribution has at the top on the cover top of the spin rotor
Vertical blade support is done, middle stirring blade, each middle stirring blade are fixedly connected at the top of each blade support
The upper hollow out that is evenly distributed with is provided with several first drag reductions hole, if circumferentially array distribution has in the outside of the faceshield side wall of the spin rotor
Vertical lower stirring blade is done, uniformly distributed hollow out is provided with several second drag reductions hole on each lower stirring blade.
Further, the downside integrated coaxial heart of the separator disc is provided with lower column casing, the coating dispersion chamber
Bottom of chamber is also vertically fixedly installed with air column, and the upper end with air column is rotated by the inner wall of fourth bearing and the lower column casing
It is socketed, formation plate-like cavity between the fourth bearing and the separator disc, in the upper end sidewall bodies of the lower column casing circumferentially
Array distribution has several exhaust passages, and the top of the dispersive jet chamber is connected to the plate-like cavity by each exhaust passage；
The lower end with air column is connected with air supply pipe and exhaust pipe；Solenoid valve is mounted on the air supply pipe and exhaust pipe；It is described
If the outlet side of air supply pipe is connected to the dry air leadout hole of distribution column bottom side wall distribution；The inlet end of the exhaust pipe exists
The top with air column is connected to the plate-like cavity；Supercharging air pump is installed on the air supply pipe, is installed on the exhaust pipe
There is negative pressure air pump.
Further, the dispersing technology of the process system of aqueous, environmental protective reflecting coating:
Step 1 simultaneously closes off the solenoid valve on exhaust pipe and air supply pipe, then will configure according to a certain ratio and tentatively mixed
Close to dispersion paints lotion by feed inlet be persistently directed into coating disperse it is intracavitary, until coating disperse it is intracavitary wait disperse to apply
The liquid level of material lotion is totally submerged each stirring cantilever；Resistance heating wire is powered at this time, maintains intracavitary 38 DEG C to 45 of coating dispersion
DEG C temperature constant state, so that coating dispersion intracavitary is remained optimal dispersion temperature；The electromagnetism on air supply pipe is opened at the same time
Valve, supercharging air pump continue air is pumped into air supply pipe, if the pressurized air in air supply pipe continue through dry air leadout hole with
The form of bubble spills into the bottom of chamber medium position of coating dispersion chamber, if persistently exporting bubble floating from dry air leadout hole immediately
It is intracavitary to dispersive jet, so make dispersive jet it is intracavitary be partially formed the cavity full of air, and make dispersive jet chamber
Interior liquid level is consistently lower than height where the spout of each injection pipe, and the jet stream for making the spout of each injection pipe be gushed out is necessary
The intracavitary chamber portion of dispersive jet is first passed through, is then injected again in the intracavitary liquid level of dispersive jet；
Step 2 opens recycle liquid pump, and circulating pump is made to be in continuously running duty, and coating disperses intracavitary upper at this time
Partial emulsion is sucked in liquid-conveying ducts by several liquid sucting ports, and then the lotion in liquid-conveying ducts, which is inhaled into, is rotated into fluid cylinder,
It is rotated into the lotion in fluid cylinder to suck in recycle liquid pump by liquid inlet joint, the lotion in recycle liquid pump is extruded by liquid outlet connector
In feed liquor column casing, the lotion in feed liquor column casing is pressed into diffluence room, and then lotion shunts under the action of pump pressure in diffluence room
Into each injection pipe, and then the jet stream that the spout of each injection pipe is gushed out first passes through the intracavitary chamber portion of dispersive jet, so
It is injected again in the intracavitary liquid level of dispersive jet afterwards, forms penetrating for lasting splashing impact type at the liquid level for keeping dispersive jet intracavitary
Stream, which can also collide the lotion at the intracavitary liquid level of dispersive jet repeatedly, and then realize intracavitary to dispersive jet
The fining dispersion of lotion, emulsifying effectiveness it is finer and smoother；And then the lotion for injecting the intracavitary liquid level of dispersive jet is overflowed downwards
Lotion to the bottom of chamber position of coating dispersion chamber, and then coating dispersion chamber bottom of chamber gradually travel up to coating disperse it is intracavitary upper
Part, the lotion that coating disperses intracavitary upper part continue to be sucked in liquid-conveying ducts again by several liquid sucting ports, and then make entire
Coating disperses the intracavitary interior circulation for forming constant flow；In above-mentioned inner cyclic process, it is equal that coating disperses intracavitary all lotions
Can be by the spray dispersion process of the intracavitary splashing impact type of dispersive jet, and then realize that refinement dispersion process is uniform；It is same with this
When each injection pipe the recoil strength of the sprayed liquid of spout drive the spin rotor to rotate clockwise；And then spin rotor
It rotates clockwise and drives several middle stirring blades and lower stirring blade synchronous rotary, and then make the middle-lower part shape of coating dispersion chamber
At lasting eddy flow clockwise, and then play stirring action；Start synchronous translator at the same time, synchronous translator passes through synchronization
Band drives belt synchronizing wheel to rotate counterclockwise, and then rotates shaft counterclockwise, and then the rotation counterclockwise of shaft drives on each
Stirring blade stirs the lotion of part on coating dispersion chamber counterclockwise, and then the lotion of part on coating dispersion chamber is made to form the inverse time
The eddy flow of needle；And the middle-lower part of the chamber of coating dispersion at this time forms lasting eddy flow clockwise, which disperses middle and lower part in chamber
Divide the boundary position of eddy flow clockwise and upper part eddy flow counterclockwise to form the shearing thinning effect arranged by force to lotion, and then promotes
The further refinement of lotion disperses；
Step 3 is dispersed after the completion of intracavitary lotion is completely dispersed after coating, since the coating dispersion in step 2 is intracavitary
Lotion by during the spray dispersion of the intracavitary splashing impact type of dispersive jet in the process for carrying out refinement dispersion to lotion
It can also be to the bubble for bringing part additional in lotion；These bubbles need to eliminate；The solenoid valve on air supply pipe is closed at this time, with this
The solenoid valve on exhaust pipe is opened simultaneously, and starts the negative pressure pump on exhaust pipe, and then exhaust pipe makes to be formed in plate-like cavity
Negative pressure, and then several exhaust passages is made to siphon away the air of the intracavitary ullage of dispersive jet rapidly, until dispersive jet chamber quilt
Lotion is filled up completely, and then each injection pipe and spout is made to be in the state submerged by lotion, intracavitary to dispersive jet
The air of ullage closes the solenoid valve on exhaust pipe after being sucked away, the jet stream that the spout of each injection pipe is gushed out at this time is not
The intracavitary chamber portion of dispersive jet can be first passed through, but is emitted directly toward in the intracavitary lotion of dispersive jet, and then injection pipe at this time
The jet stream that is gushed out of spout will not bring air into and enter in lotion；Then suitable defoaming agent is persistently led by feed inlet
Enter to coating to disperse intracavitary, and maintains the inner cyclic process in step 2, coating dispersion at this time is intracavitary to be still within stirring shape
State, at this time under the action of defoaming agent, coating, which disperses intracavitary bubble, to be gradually eliminated during stirring；
Step 4 opens the solenoid valve on coating delivery line, and starts the drawing liquid pump on coating delivery line, and coating is dispersed
The good coating export of intracavitary dispersing and disintegrating.
The utility model has the advantages that structure of the invention is simple, the jet stream that the spout of each injection pipe is gushed out first passes through dispersive jet
Then intracavitary chamber portion is injected again in the intracavitary liquid level of dispersive jet, formed and continued at the liquid level for keeping dispersive jet intracavitary
Splashing impact type jet stream, which can also collide the lotion at the intracavitary liquid level of dispersive jet, Jin Ershi repeatedly
The fining dispersion of lotion now intracavitary to dispersive jet, emulsifying effectiveness are finer and smoother.
Detailed description of the invention
Attached drawing 1 is the overall structure diagram of the device；
Attached drawing 2 just cuts open structural schematic diagram for the device；
Attached drawing 3 is the perspective cross-sectional graph structure of the device；
Attached drawing 4 is that the device conceals the structural schematic diagram after external coating dispersion tank；
Attached drawing 5 is the bottom view of attached drawing 4；
Attached drawing 6 is the three-dimensional cut-away diagram of spin rotor.
Specific embodiment
The present invention will be further explained with reference to the accompanying drawing.
The aqueous negative oxygen ion interior wall paint production-process systems as shown in attached drawing 1 to 6, it is characterised in that: including vertical
Columnar coating dispersion tank 23, the top side of the coating dispersion tank 23 are provided with feed inlet 26, the coating dispersion tank 23
Tank in for columnar coating disperse chamber 16, further include coating delivery line 22, the liquid feeding end of the coating delivery line 22 is connected to institute
Coating dispersion 16 bottom of chamber is stated, solenoid valve and drawing liquid pump are installed on the coating delivery line 22；The coating dispersion chamber 16
Centre is provided with recycle liquid pump 13；It further include lateral liquid pump support 37, one end of the liquid pump support 37 is fixedly connected
23 inner wall of coating dispersion tank, the recycle liquid pump 13 are fixedly mounted on the other end of the liquid pump support 37.
The upper end liquid feeding end of the recycle liquid pump 13 is liquid inlet joint 18, and the lower end outlet end of the recycle liquid pump 13 is
Liquid connector 19；Concentric be provided in the top of the recycle liquid pump 13 is rotated into fluid cylinder 14, the lower end for being rotated into fluid cylinder 14
Outlet end is socketed by first bearing 17 and the liquid inlet joint 18 rotation；The upper end for being rotated into fluid cylinder 14 blocks setting,
And the concentric integration in upper end for being rotated into fluid cylinder 14 is connected with shaft 29, the shaft 29 and the coating dispersion tank 23
Bearing socket 32 on the wall body of top is rotatablely connected by second bearing 15；The top of the shaft 29 is provided with belt synchronizing wheel
47；The top of the coating dispersion tank 23 is equipped with synchronous translator 30, and the synchronous translator 30 passes through synchronous belt 31 and institute
State the drive connection of belt synchronizing wheel 47；Circumferentially array is fixedly connected with several lateral stir to the surrounding for being rotated into fluid cylinder 14
Cantilever 25 is mixed, the end of each stirring cantilever 25 is bent downward vertically, and the end of each stirring cantilever 25 is hung admittedly
Surely it is connected with stirring blade 24；The inside of each stirring cantilever 25 is provided with liquid-conveying ducts 27, each liquid-conveying ducts
27 one end is rotated into the tube inner chamber of fluid cylinder 14 described in being connected to；The end of each stirring cantilever 25 is respectively provided with liquid sucting port 28,
Each liquid sucting port 28 is respectively communicated with the other end of the liquid-conveying ducts 27；Each liquid sucting port 28 is respectively positioned on the coating dispersion
In chamber 16；The inner wall of the coating dispersion chamber 16, which also spirals, is provided with resistance heating wire 38.
The lower section of the recycle liquid pump 13 is concentric to be provided with spin rotor 42, and the upper end of the spin rotor 42 is concentric
Integration is connected with feed liquor column casing 20, and the feed liquor column casing 20 is socketed the liquid outlet connector 19 by the rotation of 3rd bearing 10；Institute
Stating spin rotor 42 is the open cylindricality cover structure in lower end, cover top 0 and cricoid cover of the spin rotor 42 including plate-like
The bottom of chamber spacing of body sidewall 9, the bottom end of the faceshield side wall 9 and coating dispersion chamber 16 is arranged；The spin rotor 42
Internal also concentric integrated setting has separator disc 46, and the diffluence room of plate-like is formed between the separator disc 46 and the cover top 0
11, the concentric connection diffluence room 11 in the lower end of the feed liquor column casing 20；The downside of the separator disc 46 forms columnar point
Jet chamber 35 is dissipated, circumferentially array hollow out is provided with several liquid pass holes 8 in the lower section portion of the faceshield side wall 9；The separator disc 46
Downside be fixedly connected with the injection pipes 39 of several lateral attitudes, each injection pipe 39 is along the separator disc 46 circumferentially array
Distribution, and the root of each injection pipe 39 is connected to the diffluence room 11, it is in incline that each 39 lower end of injection pipe, which is provided with,
The spout 40 of oblique injection direction 41, the recoil strength of the sprayed liquid of each spout 40 can drive the spin rotor 42 along up time
Needle rotation；Circumferentially array stationary distribution has several vertical blade supports 12 at the top on the cover top 0 of the spin rotor 42, respectively
The top of the blade support 12 is fixedly connected to middle stirring blade 45, uniformly distributed hollow out setting on each middle stirring blade 45
Have several first drag reductions hole 44, the outside of the faceshield side wall 9 of the spin rotor 42 circumferentially array distribution have it is several vertical
Lower stirring blade 33, uniformly distributed hollow out is provided with several second drag reductions hole 43 on each lower stirring blade 33.
The downside integrated coaxial heart of the separator disc 46 is provided with lower column casing 7, the bottom of chamber of the coating dispersion chamber 16
It is also vertically fixedly installed with air column 36, the upper end with air column 36 is turned by the inner wall of fourth bearing 4 and the lower column casing 7
Dynamic socket, forms plate-like cavity 5 between the fourth bearing 4 and the separator disc 46, in the upper end sidewall bodies of the lower column casing 7
Circumferentially array distribution has several exhaust passages 1, described in top connection of each exhaust passage 1 by the dispersive jet chamber 35
Plate-like cavity 5；The lower end with air column 36 is connected with air supply pipe 6 and exhaust pipe 3；Pacify on the air supply pipe 6 and exhaust pipe 3
Equipped with solenoid valve；If the outlet side connection dry air leadout hole 2 with the distribution of 36 bottom sidewall of air column of the air supply pipe 6；
The inlet end of the exhaust pipe 3 is connected to the plate-like cavity 5 on the top with air column 36；It is equipped on the air supply pipe 6
Supercharging air pump is equipped with negative pressure air pump on the exhaust pipe 3.
The coating dispersing technology, step and technological progress of this programme arrange as follows:
Step 1 simultaneously closes off the solenoid valve on exhaust pipe 3 and air supply pipe 6, then will configure according to a certain ratio and preliminary
Mixing is persistently directed into coating dispersion chamber 16 to dispersion paints lotion by feed inlet 26, until in coating dispersion chamber 16
Liquid level to dispersion paints lotion is totally submerged each stirring cantilever 25；Resistance heating wire 38 is powered at this time, maintains coating dispersion
38 DEG C to 45 DEG C of temperature constant state in chamber 16 makes to remain optimal dispersion temperature in coating dispersion chamber 16；It beats at the same time
The solenoid valve on air supply pipe 6 is opened, supercharging air pump continues to be pumped into air into air supply pipe 6, and the pressurized air in air supply pipe 6 persistently leads to
If the bottom of chamber medium position that dry air leadout hole 2 spills into coating dispersion chamber 16 in the form of bubble is crossed, if immediately from dry air
Leadout hole 2 persistently exports in bubble floating to dispersive jet chamber 35, and then is full of being partially formed in dispersive jet chamber 35
The cavity of air, and the liquid level 21 in dispersive jet chamber 35 is made highly to be consistently lower than height where the spout 40 of each injection pipe 39
Degree, the jet stream for making the spout 40 of each injection pipe 39 be gushed out have to first pass through the chamber portion in dispersive jet chamber 35, so
It is injected again in the liquid level 21 in dispersive jet chamber 35 afterwards；
Step 2 opens recycle liquid pump 13, and circulating pump is made to be in continuously running duty, in the chamber 16 of coating dispersion at this time
Upper partial emulsion by several liquid sucting ports 28 suck liquid-conveying ducts 27 in, then the lotion in liquid-conveying ducts 27 is inhaled into rotation
In feed liquor cylinder 14, it is rotated into the lotion in fluid cylinder 14 and is sucked in recycle liquid pump 13 by liquid inlet joint 18, in recycle liquid pump 13
Lotion is extruded in feed liquor column casing 20 by liquid outlet connector 19, and the lotion in feed liquor column casing 20 is pressed into diffluence room 11, Jin Erfen
Lotion is branched under the action of pump pressure in each injection pipe 39 in flow chamber 11, and then the spout 40 of each injection pipe 39 is gushed out
Jet stream first passes through the chamber portion in dispersive jet chamber 35, is then injected in the liquid level 21 in dispersive jet chamber 35 again, makes to disperse
The jet stream of lasting splashing impact type is formed at liquid level 21 in jet chamber 35, which can also collide repeatedly dispersion and penetrate
The lotion at the liquid level 21 in chamber 35 is flowed, and then is realized to the fining dispersion of the lotion in dispersive jet chamber 35, emulsifying effectiveness
It is finer and smoother；And then the lotion for the liquid level 21 injected in dispersive jet chamber 35 is spilled over to downwards the bottom of chamber position of coating dispersion chamber 16
It sets, and then the lotion of coating dispersion 16 bottom of chamber of chamber gradually travels up to the upper part in coating dispersion chamber 16, coating disperses chamber
The lotion of upper part in 16 continues to be sucked in liquid-conveying ducts 27 again by several liquid sucting ports 28, and then makes entire coating dispersion chamber
The interior circulation of constant flow is formed in 16；In above-mentioned inner cyclic process, all lotions in coating dispersion chamber 16 can pass through
The spray dispersion process of splashing impact type in dispersive jet chamber 35, and then realize that refinement dispersion process is uniform；It is each at the same time
The recoil strength of the sprayed liquid of spout 40 of injection pipe 39 drives the spin rotor 42 to rotate clockwise；And then spin rotor
42 rotate clockwise drives several middle stirring blades 45 and lower 33 synchronous rotary of stirring blade, and then makes coating dispersion chamber 16
Middle-lower part forms lasting eddy flow clockwise, and then plays stirring action；Start synchronous translator 30, synchronous belt at the same time
Motor 30 drives belt synchronizing wheel 47 to rotate counterclockwise by synchronous belt 31, and then rotates shaft 29 counterclockwise, and then shaft
29 rotation counterclockwise drives each upper stirring blade 24 to stir the lotion of part on coating dispersion chamber 16 counterclockwise, and then makes coating
The lotion of part forms eddy flow counterclockwise on dispersion chamber 16；And the middle-lower part of the chamber 16 of coating dispersion at this time formed it is lasting suitable
Hour hands eddy flow, the coating disperse the boundary position of middle-lower part eddy flow clockwise and upper part eddy flow counterclockwise in chamber 16 to lotion
The shearing thinning effect arranged by force is formed, and then promotes the further refinement dispersion of lotion；
Step 3, after the completion of the lotion in coating dispersion chamber 16 is completely dispersed, since the coating in step 2 disperses chamber
Refinement dispersion is being carried out to lotion during spray dispersion of the lotion by the splashing impact type in dispersive jet chamber 35 in 16
Process can also be to the bubble for bringing part additional in lotion；These bubbles need to eliminate；The electromagnetism on air supply pipe 6 is closed at this time
Valve opens the solenoid valve on exhaust pipe 3 at the same time, and starts the negative pressure pump on exhaust pipe 3, and then exhaust pipe 3 makes plate-like
The air for 21 top of liquid level for forming negative pressure in cavity 5, and then siphoning away several exhaust passages 1 rapidly in dispersive jet chamber 35,
Until dispersive jet chamber 35 is filled up completely by lotion, and then it is in each injection pipe 39 and spout 40 by lotion submergence
State closes the solenoid valve on exhaust pipe 3 after the air of 21 top of liquid level in dispersive jet chamber 35 is sucked away, each spray at this time
Chamber portion in dispersive jet chamber 35 will not be first passed through by penetrating the jet stream that the spout 40 of pipe 39 is gushed out, but is emitted directly toward point
It dissipates in jet chamber 35 in lotion, and then the jet stream that the spout 40 of injection pipe 39 is gushed out at this time will not bring air into and enter lotion
In；Then suitable defoaming agent is persistently directed into coating by feed inlet 26 to disperse in chamber 16, and maintained in step 2
Inner cyclic process, coating disperses in chamber 16 to be still within stirring at this time, and at this time under the action of defoaming agent, coating disperses chamber
Bubble in 16 can gradually eliminate during stirring；
Step 4 opens the solenoid valve on coating delivery line 22, and starts the drawing liquid pump on coating delivery line 22, by coating
Disperse the good coating export of dispersing and disintegrating in chamber 16.
Formula to the dispersion paints lotion score by weight of this programme: 35~40 parts of styrene-acrylic emulsion, tourmaline powder 1~
3 parts, 2~5 parts of cerium compound, 3~5 parts of titanate coupling agent, 1~2 part of nanogold, 0.1~1 part of germanium powder, seven aluminic acids 12
0.5~1 part of calcium, 1~5 part of ethyl alcohol, 0.1~0.3 part of Ricinate, 50~60 parts of water.
The defoaming agent of subsequent process is 1 part.
The above is only a preferred embodiment of the present invention, it should be pointed out that: for the ordinary skill people of the art
For member, various improvements and modifications may be made without departing from the principle of the present invention, these improvements and modifications are also answered
It is considered as protection scope of the present invention.
Claims (5)
1. aqueous negative oxygen ion interior wall paint production-process systems, it is characterised in that: including vertical columnar coating dispersion tank
(23), the top side of the coating dispersion tank (23) is provided with feed inlet (26), is in the tank of the coating dispersion tank (23)
Columnar coating disperses chamber (16), further includes coating delivery line (22), described in the liquid feeding end connection of the coating delivery line (22)
Coating disperses chamber (16) bottom, to be equipped with solenoid valve and drawing liquid pump on the coating delivery line (22)；The coating disperses chamber
(16) centre is provided with recycle liquid pump (13)；It further include lateral liquid pump support (37), the liquid pump support (37)
One end is fixedly connected with coating dispersion tank (23) inner wall, and the recycle liquid pump (13) is fixedly mounted on the liquid pump support (37)
The other end.
2. aqueous negative oxygen ion interior wall paint production-process systems according to claim 1, it is characterised in that: the circulation fluid
The upper end liquid feeding end for pumping (13) is liquid inlet joint (18), and the lower end outlet end of the recycle liquid pump (13) is liquid outlet connector (19)；
Concentric be provided in the top of the recycle liquid pump (13) is rotated into fluid cylinder (14), and described be rotated under fluid cylinder (14) brings out liquid
End is socketed by first bearing (17) and the liquid inlet joint (18) rotation；The upper end for being rotated into fluid cylinder (14), which blocks, to be set
It sets, and the concentric integration in upper end for being rotated into fluid cylinder (14) is connected with shaft (29), the shaft (29) and the painting
Expect that the bearing socket (32) at the top of dispersion tank (23) on wall body is rotatablely connected by second bearing (15)；The top of the shaft (29)
End is provided with belt synchronizing wheel (47)；Synchronous translator (30), the synchronization are installed at the top of the coating dispersion tank (23)
Translator (30) is drivingly connected by synchronous belt (31) and the belt synchronizing wheel (47)；The surrounding for being rotated into fluid cylinder (14)
Circumferentially array is fixedly connected with several lateral stirring cantilevers (25), and the end of each stirring cantilever (25) is curved downward vertically
Song, and the end of each stirring cantilever (25) hangs and is fixedly connected with stirring blade (24)；Each stirring cantilever
(25) inside is provided with liquid-conveying ducts (27), one end of each liquid-conveying ducts (27) be connected to described in be rotated into fluid cylinder
(14) tube inner chamber；The end of each stirring cantilever (25) is respectively provided with liquid sucting port (28), and each liquid sucting port (28) connects respectively
Lead to the other end of the liquid-conveying ducts (27)；Each liquid sucting port (28) is respectively positioned in coating dispersion chamber (16)；The painting
The inner wall of material dispersion chamber (16), which also spirals, is provided with resistance heating wire (38).
3. aqueous negative oxygen ion interior wall paint production-process systems according to claim 2, it is characterised in that: the circulation fluid
The lower section of pump (13) is concentric to be provided with spin rotor (42), and the concentric integration in upper end of the spin rotor (42) is connected with
Feed liquor column casing (20), the feed liquor column casing (20) are socketed the liquid outlet connector (19) by 3rd bearing (10) rotation；It is described from
Gyrator (42) is the open cylindricality cover structure in lower end, and the spin rotor (42) includes the cover top (0) of plate-like and cricoid
The bottom of chamber spacing of faceshield side wall (9), the bottom end of the faceshield side wall (9) and coating dispersion chamber (16) is arranged；The spin
The also concentric integrated setting in the inside of rotor (42) has separator disc (46), between the separator disc (46) and cover top (0)
Form the diffluence room (11) of plate-like, the concentric connection diffluence room (11) in the lower end of the feed liquor column casing (20)；The separation
The downside of disk (46) forms columnar dispersive jet chamber (35), and circumferentially array hollow out is set in the lower section portion of the faceshield side wall (9)
It is equipped with several liquid pass holes (8)；The injection pipe (39) of several lateral attitudes, each institute are fixedly connected on the downside of the separator disc (46)
Injection pipe (39) is stated along the separator disc (46) circumferentially array distribution, and described in the root of each injection pipe (39) is connected to
Diffluence room (11), each injection pipe (39) lower end are provided with the spout (40) of inclined injection direction (41), each spray
The recoil strength of the sprayed liquid of mouth (40) can drive the spin rotor (42) to rotate clockwise；The spin rotor (42)
Circumferentially array stationary distribution has several vertical blade supports (12) at the top on cover top (0), each blade support (12)
Top is fixedly connected to middle stirring blade (45), and uniformly distributed hollow out is provided with several first and subtracts on each middle stirring blade (45)
It hinders hole (44), circumferentially array distribution has several vertical lower stirrings in the outside of the faceshield side wall (9) of the spin rotor (42)
Blade (33), uniformly distributed hollow out is provided with several second drag reductions hole (43) on each lower stirring blade (33).
4. aqueous negative oxygen ion interior wall paint production-process systems according to claim 3, it is characterised in that: the separator disc
(46) the downside integrated coaxial heart is provided with lower column casing (7), and also vertically fixation is set for the bottom of chamber of coating dispersion chamber (16)
It is equipped with air column (36), the upper end with air column (36) passes through the inner wall turning set of fourth bearing (4) and the lower column casing (7)
It connects, forms plate-like cavity (5) between the fourth bearing (4) and the separator disc (46), the upper end side wall of the lower column casing (7)
Circumferentially array distribution has several exhaust passages (1) on body, and each exhaust passage (1) is by the top of the dispersive jet chamber (35)
Portion is connected to the plate-like cavity (5)；The lower end with air column (36) is connected with air supply pipe (6) and exhaust pipe (3)；The gas supply
Solenoid valve is mounted on pipe (6) and exhaust pipe (3)；The outlet side connection of the air supply pipe (6) is described to match air column (36) bottom
If the dry air leadout hole (2) of side wall distribution；The inlet end of the exhaust pipe (3) is connected to institute on the top with air column (36)
State plate-like cavity (5)；Supercharging air pump is installed on the air supply pipe (6), negative pressure air pump is installed on the exhaust pipe (3).
5. the dispersing technology of the process system of aqueous, environmental protective reflecting coating according to claim 4, it is characterised in that:
Step 1 simultaneously closes off the solenoid valve on exhaust pipe (3) and air supply pipe (6), then will configure according to a certain ratio and preliminary
Mixing is persistently directed into coating dispersion chamber (16) to dispersion paints lotion by feed inlet (26), until coating disperses chamber
(16) liquid level to dispersion paints lotion in is totally submerged each stirring cantilever (25)；Resistance heating wire (38) are powered at this time,
The temperature constant state for maintaining 38 DEG C to 45 DEG C in coating dispersion chamber (16) makes to remain optimal dispersion in coating dispersion chamber (16)
Temperature；The solenoid valve on air supply pipe (6) is opened at the same time, and supercharging air pump continues to be pumped into air, air supply pipe into air supply pipe (6)
(6) if in pressurized air continue through dry air leadout hole (2) spilt into the form of bubble coating dispersion chamber (16) chamber
Bottom medium position if persistently exporting bubble floating from dry air leadout hole (2) immediately in dispersive jet chamber (35), and then makes point
It dissipates in jet chamber (35) and is partially formed the cavity full of air, and make liquid level (21) height in dispersive jet chamber (35)
Height, the jet stream for making the spout (40) of each injection pipe (39) be gushed out where the spout (40) of consistently lower than each injection pipe (39)
It has to first pass through the chamber portion in dispersive jet chamber (35), then injects the liquid level (21) in dispersive jet chamber (35) again
In；
Step 2 opens recycle liquid pump (13), and circulating pump is made to be in continuously running duty, at this time in coating dispersion chamber (16)
Upper partial emulsion by several liquid sucting ports (28) sucking liquid-conveying ducts (27) in, then the lotion in liquid-conveying ducts (27) is inhaled
Enter to be rotated into fluid cylinder (14), be rotated into the lotion in fluid cylinder (14) and sucked in recycle liquid pump (13) by liquid inlet joint (18),
Lotion in recycle liquid pump (13) is extruded in feed liquor column casing (20) by liquid outlet connector (19), the lotion quilt in feed liquor column casing (20)
It is pressed into diffluence room (11), and then lotion is branched under the action of pump pressure in each injection pipe (39) in diffluence room (11), in turn
The jet stream that the spout (40) of each injection pipe (39) is gushed out first passes through the chamber portion in dispersive jet chamber (35), then penetrates again
Enter in the liquid level (21) in dispersive jet chamber (35), makes to form lasting splashing punching at the liquid level (21) in dispersive jet chamber (35)
The jet stream of push-style, the splash jet stream can also collide the lotion at the liquid level (21) in dispersive jet chamber (35), Jin Ershi repeatedly
It is now finer and smoother to the fining dispersion of the lotion in dispersive jet chamber (35), emulsifying effectiveness；And then inject dispersive jet chamber
(35) lotion of the liquid level (21) in is spilled over to downwards the bottom of chamber position of coating dispersion chamber (16), and then coating disperses chamber (16) chamber
The lotion at bottom gradually travels up to the upper part in coating dispersion chamber (16), and coating disperses the lotion of the upper part in chamber (16)
Continue to be sucked in liquid-conveying ducts (27) again by several liquid sucting ports (28), and then makes to be formed in entire coating dispersion chamber (16) and continue
The interior circulation of flowing；In above-mentioned inner cyclic process, all lotions in coating dispersion chamber (16) can pass through dispersive jet chamber
(35) the spray dispersion process of the splashing impact type in, and then realize that refinement dispersion process is uniform；Each injection pipe at the same time
(39) recoil strength of the sprayed liquid of spout (40) drives the spin rotor (42) to rotate clockwise；And then spin rotor
(42) rotate clockwise drives several middle stirring blades (45) and lower stirring blade (33) synchronous rotary, and then disperses coating
The middle-lower part of chamber (16) forms lasting eddy flow clockwise, and then plays stirring action；Start synchronous translator at the same time
(30), synchronous translator (30) drive belt synchronizing wheel (47) to rotate counterclockwise by synchronous belt (31), and then make shaft (29)
Rotation counterclockwise, and then the rotation counterclockwise of shaft (29) drives each upper stirring blade (24) stirring coating counterclockwise to disperse chamber
(16) lotion of part on, and then the lotion of part in coating dispersion chamber (16) is made to form eddy flow counterclockwise；And coating at this time
The middle-lower part of dispersion chamber (16) forms lasting eddy flow clockwise, which disperses middle-lower part eddy flow clockwise in chamber (16)
The shearing thinning effect arranged by force is formed to lotion with the boundary position of upper part eddy flow counterclockwise, and then promotes the further of lotion
Refinement dispersion；
Step 3, after the completion of the lotion in coating dispersion chamber (16) is completely dispersed, since the coating in step 2 disperses chamber
(16) it is refined during spray dispersion of the lotion by the splashing impact type in dispersive jet chamber (35) in lotion
The process of dispersion can also be to the bubble for bringing part additional in lotion；These bubbles need to eliminate；It closes on air supply pipe (6) at this time
Solenoid valve, open the solenoid valve on exhaust pipe (3) at the same time, and start the negative pressure pump on exhaust pipe (3), and then be vented
Pipe (3) makes to form negative pressure in plate-like cavity (5), and then siphons away several exhaust passages (1) in dispersive jet chamber (35) rapidly
Air above liquid level (21), until dispersive jet chamber (35) be filled up completely by lotion, and then make each injection pipe (39) and
Spout (40) is in the state submerged by lotion, after the air above the liquid level (21) in dispersive jet chamber (35) is sucked away
The solenoid valve on exhaust pipe (3) is closed, the jet stream that the spout (40) of each injection pipe (39) is gushed out at this time will not first pass through point
The chamber portion in jet chamber (35) is dissipated, but is emitted directly toward in dispersive jet chamber (35) interior lotion, and then injection pipe at this time
(39) jet stream that spout (40) is gushed out will not bring air into and enter in lotion；Then suitable defoaming agent is passed through into charging
Mouth (26) is persistently directed into coating dispersion chamber (16), and maintains the inner cyclic process in step 2, and coating disperses chamber at this time
(16) it is still within stirring in, at this time under the action of defoaming agent, the bubble that coating disperses in chamber (16) can be in stirring
It gradually eliminates in the process；
Step 4 opens the solenoid valve on coating delivery line (22), and starts the drawing liquid pump on coating delivery line (22), by coating
Disperse the good coating export of dispersing and disintegrating in chamber (16).
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| CN110433708A (en) * | 2019-08-19 | 2019-11-12 | 程莹 | Aqueous negative oxygen ion Paint Preparation System, preparation process and the coating composition |
| CN110841536A (en) * | 2019-11-26 | 2020-02-28 | 杭小洁 | Dispersion preparation equipment, preparation process and proportion of interior wall water-based paint |
| CN110862750A (en) * | 2019-11-14 | 2020-03-06 | 湖北巴司特科技股份有限公司 | Water-based alternative hot-spraying zinc coating and preparation method thereof |
| CN113491977A (en) * | 2020-03-19 | 2021-10-12 | 李茂正 | Improved structure of stirring tank equipment |
| CN116474620A (en) * | 2023-05-16 | 2023-07-25 | 江苏智泰新能源科技有限公司 | Coated diaphragm preparation device for sodium ion battery and preparation method thereof |
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Denomination of invention: Production process system and formula of water-based negative oxygen ion interior wall paint Granted publication date: 20200403 Pledgee: Wuxi rural commercial bank Limited by Share Ltd. Pledgor: WUXI YINGBO CHEMICAL CO.,LTD. Registration number: Y2024980023821 |