CN104650677A - Distributive green environmentally-friendly paint manufacturing system - Google Patents
Distributive green environmentally-friendly paint manufacturing system Download PDFInfo
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- CN104650677A CN104650677A CN201310598090.4A CN201310598090A CN104650677A CN 104650677 A CN104650677 A CN 104650677A CN 201310598090 A CN201310598090 A CN 201310598090A CN 104650677 A CN104650677 A CN 104650677A
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- 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
- C09D133/00—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 only one carboxyl radical, or of salts, anhydrides, esters, amides, imides, or nitriles thereof; Coating compositions based on derivatives of such polymers
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- 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
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- 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
- C09D127/00—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 a halogen; Coating compositions based on derivatives of such polymers
- C09D127/02—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 a halogen; Coating compositions based on derivatives of such polymers not modified by chemical after-treatment
- C09D127/12—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 a halogen; Coating compositions based on derivatives of such polymers not modified by chemical after-treatment containing fluorine atoms
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- 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
- C09D131/00—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 acyloxy radical of a saturated carboxylic acid, of carbonic acid, or of a haloformic acid; Coating compositions based on derivatives of such polymers
- C09D131/02—Homopolymers or copolymers of esters of monocarboxylic acids
- C09D131/04—Homopolymers or copolymers of vinyl acetate
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- 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
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- 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
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- 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
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Abstract
The embodiment of the invention provides a distributive green environmentally-friendly paint manufacturing system which comprises a powder storage subsystem, a solution aid storage subsystem, a dispersion subsystem, a sanding subsystem, a intermediate slurry storage subsystem, an emulsion storage subsystem, a paint mixing subsystem, a finished product storage subsystem, a filling subsystem and a product control subsystem. By automatic production control, several intermediate slurry components with different functions are manufactured, paint products with different properties, qualities and types are obtained by mixing according to different ratio, and colored paints are prepared by the utilization of the produced paint products. According to the invention, problems such as many pollutants, high cost and low production efficiency that are generated during the large-scale paint manufacturing process in the prior art are solved; production efficiency of paints is enhanced; and production costs of paints are reduced.
Description
Technical field
The present invention relates to a kind of coating manufacturing system of distribute type environmental protection.
Background technology
Coating refers to that being applied to body surface can form a class I liquid I of solid-state film or the general name of solid material with protection decoration or property (as insulation, anticorrosion, mark etc.).
The wherein one of coating is aqueous architectural coating.Aqueous architectural coating is commonly called as emulsion paint, and current manufacture is substantially in Manual material feeding and produces, by manually the auxiliary agents such as water, dispersion agent, defoamer, sterilant being dropped in Scattered Kettle, and low speed 3-5 minute; Manually the powders such as titanium dioxide, coarse whiting, kaolin are dropped in still, high speed dispersion about 20 minutes; Again mould inhibitor, defoamer, thickening material etc. are slowly dropped into modulation finished product by artificial; Finally filter and package warehouse-in, reuse after cleaning Scattered Kettle.Its production process produces the pollutents such as a large amount of dust, waste water, waste residue, the productive efficiency of serious restriction coating manufacturing concern and development prospect.
Emulsion paint range of product is various, Various Functions, and category can be divided into: interiro wall latex paint and exterior wall latex paint; Can be divided into by gloss: without photosensitiveness, silkiness, half photosensitiveness and high photosensitiveness; Can be divided into by quality: salable product, acceptable end product and premium grads; Can be divided into by toning classification: white paint, light base paint, middle look base paint and dark base paint, in conjunction with two above-mentioned kinds, four kinds of gloss, three kinds of qualities, four kinds of toning classifications, Paint manufacturers needs to produce to be not less than 96 kinds of products.This needs huge factory, warehouse and equipment investment, can realize the coating products producing so many kind, meet market sale demand.Add that the turnout of colored paint product is difficult to control, and some unconventional product, order volume is little, produces difficulty, large-tonnage product must be caused dull, and even scrap, have a strong impact on the development of enterprise.Huge investment, must limit Paint manufacturers and carry out scale operation.Extensive coating manufacture is produced, is necessary that reducing factory building drops into, and reaches the object realizing flexible operation on the basis of existing factory building.Therefore, the manufacture method improving coating is the key of problem.
Summary of the invention
The embodiment of the present invention provides a kind of coating manufacturing system of distribute type environmental protection, manufacture production process produce a large amount of pollutent, cost is high and production efficiency is low problem to solve extensive coating in prior art, improve the production efficiency of coating, reduce the production cost of coating.
The embodiment of the present invention provides a kind of coating manufacturing system of distribute type environmental protection, comprise powder storage subsystem, soluble additive storage subsystem, dispersion subsystem, sand milling subsystem, intermediate pulp storage subsystem, emulsion storage subsystem, paint subsystem, finished product storage subsystem, filling subsystem and production control subsystem
Described powder storage subsystem is made up of multiple powder storage tank and multiple powder conveying components and parts, for storing powder and being carried out the conveying of powder by production control subsystem;
Described soluble additive storage subsystem carries components and parts to form, for providing starting material for described dispersion subsystem and described paint subsystem by multiple soluble additive storage tank and multiple soluble additive;
Described dispersion subsystem forms, for the production of intermediate pulp by by multiple Scattered Kettle and multiple dispersion components and parts;
Described frosted subsystem comprises multiple stage skin grinder, for controlling the fineness of intermediate pulp product;
Described intermediate pulp storage subsystem is made up of, for storing the intermediate pulp needed for paint workshop section multiple intermediate pulp storage tank and multiple storage components and parts;
Described emulsion storage subsystem is made up of multiple emulsion storage tank and emulsion components and parts, and for paint, workshop section provides material;
Described paint subsystem is made up of multiple paint mixing kettle, short run distribution plant and paint components and parts, for the materials such as intermediate pulp, soluble additive, emulsion being produced required finished product by the proportioning of different ratios according to formula and order demand;
Described finished product storage subsystem is made up of, for storing finished product multiple finished product storage tank and finished product components and parts;
Described filling subsystem is made up of multiple full-automatic Bottling Line and semi-automatic packer, for being undertaken filling by material;
Described production control subsystem comprises multiple treater and recipe database, for controlling the store content of material in above-mentioned each subsystem, and controls the flow of described material, beginning and end time of components and parts and rotating speed in above-mentioned each subsystem.
Accompanying drawing explanation
In order to be illustrated more clearly in the technical scheme of the embodiment of the present invention, below the accompanying drawing used required in describing embodiment is briefly described, apparently, accompanying drawing in the following describes is some embodiments of the present invention, for those of ordinary skill in the art, under the prerequisite not paying creative work, other accompanying drawing can also be obtained according to these accompanying drawings.
Fig. 1 is the schematic diagram of the coating manufacturing system of factory assigned formula of the present invention environmental protection.
Fig. 2 is the schematic diagram that Fig. 1 intermediate pulp of the present invention manufactures workshop section.
Fig. 3 manufactures the schematic diagram of the powder stocking system of workshop section for intermediate pulp shown in Fig. 2.
Fig. 4 manufactures the schematic diagram of the soluble additive stocking system of workshop section for intermediate pulp shown in Fig. 2.
Fig. 5 manufactures the schematic diagram of the dispersion system of workshop section for intermediate pulp shown in Fig. 2.
Fig. 6 manufactures the schematic diagram of the sanding system of workshop section for intermediate pulp shown in Fig. 2.
Fig. 7 manufactures the schematic diagram of the intermediate pulp stocking system of workshop section for intermediate pulp shown in Fig. 2.
Fig. 8 is that Fig. 1 finished product of the present invention manufactures workshop section's schematic diagram.
Fig. 9 manufactures the schematic diagram of the emulsion stocking system of workshop section for finished product shown in Fig. 8.
Figure 10 manufactures the schematic diagram of the paint mixing system of workshop section for finished product shown in Fig. 8.
Figure 11 manufactures the schematic diagram of the finished product stocking system of workshop section for finished product shown in Fig. 8.
Figure 12 manufactures the schematic diagram of the bulking system of workshop section for finished product shown in Fig. 8.
Embodiment
For making the object of the embodiment of the present invention, technical scheme and advantage clearly, below in conjunction with the accompanying drawing in the embodiment of the present invention, technical scheme in the embodiment of the present invention is clearly and completely described, obviously, described embodiment is the present invention's part embodiment, instead of whole embodiments.Based on the embodiment in the present invention, the every other embodiment that those of ordinary skill in the art obtain under the prerequisite not making creative work, all belongs to the scope of protection of the invention.
The invention provides the coating manufacturing system of a kind of factory assigned formula environmental protection, it both can be used for manufacturing all kinds of required types and colored coating, turn avoid the material loss in production process and pollutant emission simultaneously, realize large to 10t, the little optimization production pattern to 5L bucket, reaches the object of zero inventory.
This vanish system relies on automatic production to control, and produces the intermediate pulp component of some difference in functionalitys, goes out performance, quality, coating products that classification is different according to different formula rate Mixed Pinyins, and utilizes the coating products produced to be mixed with colo(u)r coating.Wherein, this system to adopt basic coating and mill base by the integrated mode of discharging control, reaches the object of empty bucket toning, thus realizes three-waste free discharge.In addition, this vanish system can according to colored paint order demand, realizes the toning of empty bucket and does not produce the production technique of the three wastes.
This vanish system comprises a set of powder storage subsystem (being made up of some powder storage tanks and balancing boom device), a set of coating soluble additive storage subsystem (being made up of some soluble additive storage tanks and balancing boom device), a set of dispersion subsystem (being made up of some Scattered Kettles and components and parts), a set of sand milling subsystem (being made up of some sand mills), a set of emulsion storage subsystem (being made up of some emulsion storage tanks and balancing boom device), a set of intermediate pulp storage subsystem (being made up of some intermediate pulp storage tanks and balancing boom device), a set of paint subsystem is (by some paint mixing kettles, short run distribution plant and balancing boom device composition), the computer controlled subsystem of two covers (is made up of two computers and some balancing boom devices, be respectively production control subsystem and toning control subsystem), a set of finished product storage subsystem (being made up of multiple finished product storage tank and controller), a set of filling subsystem (being made up of some full-automatic Bottling Lines and semi-automatic packer).The storage capacity of the above-mentioned storage tank material of computer control subsystem controls, accomplishes high-low-position and alarm, also controls the flow of material, the beginning and end time of dispersing apparatus and rotating speed simultaneously.
Computer controlled subsystem is divided into production control subsystem and toning control subsystem.Comprise multiple processing server and recipe database.Recipe database comprises formula for a product database and colour formula database, specifically comprises the corresponding material data of some different intermediate pulp, finished product and color coating and production technique.The instruction of computer controlled subsystem determination formula for a product ratio, comprise querying database with retrieval or the instruction revising this ratio, and according to the instruction of order coating type, to be dispensed in paint subsystem without the intermediate pulp of classification, emulsion by ratio requirement, then the rotating speed formulated by processing requirement opens paint mixing kettle, realizing dispersion limit, limit by computer control subsystem controls and slowly add the auxiliary agents such as defoamer, mould inhibitor, thickening material, can warehouse-in be packed through being up to the standards.
Production control subsystem real-time reception sensing data, and send instruction to corresponding equipment, according to formula and the flow of processing requirement dynamic conditioning material and the opened condition of equipment.Production control subsystem also comprises some electronic or start adjustable valve, can be used for adjusting entering the different flow producing the input aperture of subsystem, and sends signal to control subsystem, comprises each that send alone and control some valves.
Production control subsystem comprises alarm module, automatically according to the storage capacity automatic alarm of each material, accomplishes that timely feed supplement or stopping are fed in raw material to remind operator according to prompting.When intermediate pulp reserves are lower than set(ting)value, subsystem is by automatic alarm, and start slurry production sequence, utilize pipeline that production raw material (comprising the auxiliary agents such as water, dispersion agent, sterilant, defoamer, pH value conditioning agent) is sent into dispersion subsystem by control subsystem, open Scattered Kettle also by rotating speed and the time dispersion of processing requirement formulation, send in Scattered Kettle by control subsystem by the powder in powder storage subsystem, control subsystem constantly modulates powder conveying amount to guarantee to meet formulary requirements by the real time data feedback of Weighing module.Subsystem adjusts rotating speed at a high speed automatically according to technique, controls jitter time, through delivering to intermediate pulp storage tank after the assay was approved.It should be noted that, dynamic flow control by production control subsystem according to real-time weight data feed back start in time or valve-off to guarantee that required material meets the demand of formula.
When finished product storage tank low memory is in set(ting)value, production control subsystem is by automatic alarm, and start finished product production sequence, utilize pipeline that production raw material (is comprised water by control subsystem, intermediate pulp, emulsion, the auxiliary agents such as film coalescence aid) send into paint subsystem, open paint mixing kettle also by rotating speed and the time dispersion of processing requirement formulation, by control subsystem by defoamer, the auxiliary agents such as thickening material slowly add in paint mixing kettle, subsystem adjusts rotating speed automatically according to technique, control jitter time, through delivering in finished product storage tank after the assay was approved, above-mentioned finished product storage tank is that the Realization of Product that conventional sales volume is large has enough to meet the need fast, the utilization ratio improving paint mixing kettle is arranged especially.As run into unconventional product, and measure less, then can be produced by mixing machine in short run distribution plant.
When all soluble additive storage tanks, powder storage tank, emulsion storage tank storage lower than set(ting)value are, production control subsystem, by automatic alarm, is reminded the timely feed supplement of operator, is avoided production process to interrupt, realize High-efficient Production.
When client needs colored paint product, the mode reality utilizing empty bucket reinforced by toning subsystem is produced in time, accurately and efficiently, stopped the loss of error that general factory manually mixes colours and material, achieved three-waste free discharge simultaneously.
Below in conjunction with accompanying drawing, by the description to embodiment, understand above-mentioned and other feature, situation and advantage of the present invention better.
Fig. 1 represents the coating manufacturing system 100 of factory assigned formula environmental protection, and this system is made up of powder storage subsystem A, soluble additive storage subsystem B, dispersion subsystem C, sand milling subsystem D, intermediate pulp storage subsystem E, emulsion storage subsystem F, paint subsystem (containing short run distribution plant) G, finished product storage subsystem H, filling subsystem I, production control subsystem J, toning subsystem K, toning control subsystem L.
This system 100 not only can realize extensive coating manufacture but also be applicable to coating manufacture on a small scale, and the micro-coating manufacture of single barrel or several barrels.
Just the system 100 production process steering routine shown in Fig. 1 does a detailed description below, native system sets seven kinds of dissimilar intermediate pulp (can need according to different formulas to do suitable increase and decrease), and Mixed Pinyin becomes to be not less than the coating being not less than 96 types mentioned in background technology.Different basic coatings can be distinguished according to order and user's use properties.In basic coating, add mill base namely can be made into a series of color coating.
In order to realize the maximization of production capacity, lift technique utilization ratio, finished product storage subsystem H is provided with in system 100, its object is to for a certain or several sales volume relatively large, the increase amount of having that the product that turnover rate is higher is suitable, starts automatic production sequence by the hi-lo signal alarm of Liquid level subsystem.When there is low alarm in finished product storage, the production sequence that paint mixing system will start automatically for this alarming product, the materials such as required intermediate pulp, emulsion, soluble additive add in paint mixing kettle according to recipe requirements by production control system automatically, and according to preset program adjustment rotating speed, order of addition(of ingredients) and feed rate.Production completes, and through after the assay was approved, product is sent in appointed product storage tank by Controlling System automatically.As the unconventional product that product is beyond finished product stocking system, system will be arranged production automatically according to order and paint mixing kettle service condition, directly pack warehouse-in after the assay was approved by bulking system.If product is micro-product, then feed in raw material by short run distribution plant and mix and put in storage after the assay was approved.
When intermediate pulp storage is not enough, dispersion system will start, according to system preset program, the materials such as water, soluble additive, powder are added in Scattered Kettle, as defective in intermediate pulp fineness, then utilize sanding system to grind further until fineness is qualified, otherwise directly intermediate pulp is sent in appointment intermediate pulp storage tank.
Explanation is described in detail below with regard to each system involved in system 100.
A-powder storage subsystem (as shown in Figure 3).In the present invention, this subsystem is divided into seven kinds of powder body materials, it is respectively:
Titanium dioxide: the R-706 produced as du pont company;
700 order water-ground limestones: 700 order coarse whitings of Fujian material company limited as prosperous in Guangdong Jiao Ling;
1000 order water-ground limestones: 1000 order coarse whitings of Fujian material company limited as prosperous in Guangdong Jiao Ling;
Light calcium carbonate: as the fine particle calcium carbonate of Nanyang chemical industry;
Calcined kaolin: as the calcined kaolin of Inner Mongol Hua Sheng;
Water-washed kaoline: the water-washed kaoline in Dongcheng as new in Zhanjiang;
Process white: as the 5AA of Guizhou millimicro.
Powder conveying subsystem components and parts of being correlated with are as described below:
A-001 is powder storage subsystem signal transmitted data line.
A-002 is powder output channel.
A-003 is powder input station.
A-004 is powder input line.
A-005 is powder transport tank car.
A-100 ~ 106 are powder storehouse.
To put in storage valve for powder in A-200 ~ 206.
A-300 ~ 306 are pulsed jet cloth filter.
A-400 ~ 406 are level gage.
A-500 ~ 506 are powder metering storehouse.
A-600 ~ 606 are air compressor.
A-700 ~ 706 are the special intake line of tank car.
Required powder, by powder input station A-003, utilizes pressurized air to send into powder storehouse through powder input line A-004 or by tank car A-005, inputs powder storehouse through special intake line A-700 ~ 706 of tank car.Adjust powder by production control subsystem J to put in storage the on off state of valve A-200 ~ 206, to guarantee that powder accurately enters appointment feed bin.Powder carry adopts the mode of malleation dilute phase to carry out, and the pressurized air needed for its course of conveying is provided by air compressor A-600 ~ 606.After powder puts in storage, gas powder is separated with the process of pulsed jet cloth filter A-300 ~ 306, guarantees to pollute, without material loss without powder storehouse.When in feed bin A-500 ~ 506, material is lower than minimum set(ting)value, then data transfer rate line A-001 is fed back to production control subsystem J by level gage A-400 ~ 406, control subsystem is incited somebody to action and alarm, need to add in time by the way, normally carry out to guarantee to produce, simultaneously when material arrives high-order, timely alarm stops reinforced by subsystem, overflows to prevent material.
B-soluble additive storage subsystem (as shown in Figure 4).In the present invention, this subsystem is divided into ten kinds of soluble additives, it is respectively:
Freeze-thaw-agent: as propylene glycol;
Dispersion machine: as Dow Chemical fast easily;
Film coalescence aid: as the Texanol of Yi Shi Man of the U.S.;
Defoamer: as the 681F of French Rhodia;
PH value conditioning agent: as the AMP95 of Dow Chemical company;
Mould inhibitor: as 316 of Dow Chemical;
Alkali swollen thickener: as the TT935 of Dow Chemical;
Associative thickener: as 2020 of Dow Chemical company;
Tensio-active agent: as the NP-10 of Dow Chemical;
Sterilant: as the LXE of Dow Chemical.
Soluble additive storage subsystem conveying components and parts are as described below:
B-001 is soluble additive storage subsystem signal transmitted data line.
B-002 is soluble additive output channel.
B-003 is soluble additive Raw material pail.
B-004 is soluble additive tank car.
B-100 ~ 109 are soluble additive storage tank.
B-200 ~ 209 are liquidometer.
B-300 ~ 309 are vacuum pressure valves.
B-400 ~ 409 are pneumatic diaphragm pump.
B-500 ~ 509 are inlet control valve 1.
B-600 ~ 609 are discharging control valve 1.
B-700 ~ 709 are discharging control valve 2.
B-800 ~ 809 are inlet control valve 2.
B-900 ~ 909 are soluble additive feed-pipe.
Soluble additive storage subsystem is mainly dispersion subsystem and paint subsystem provides starting material, utilizes computer control subsystem controls order of addition(of ingredients), feed rate and addition.
When needing in production process to add relevant soluble additive, then control subsystem is by B-001 signal transmitted data line feedback data, utilizes the pneumatic diaphragm pump of B-400 ~ 409 to be delivered in designated equipment by B-002 soluble additive reservoir conduit by material.
In order to ensure feed promptly and accurately, spy is provided with two position alert sub-system B-200 ~ 209, and when liquid level is too high or too low, subsystem is all by automatic alarm, supplements material in time or stop feed supplement in order to alert.The mass transport mode that supplier provides, based on barreled (as B-003) and tank car (B-004), utilizes pneumatic diaphragm pump B-400 ~ 409, is added by material and specifies in storage tank.Pass in and out mode for storage tank B-100 with regard to material below, spy is explained as follows:
Subsystem report to the police low liquid level time, then need supplementary material.Now open B-500 inlet control valve 1 and B-800 inlet control valve 2, and opening for feed is connected with Raw material pail B-003 or tank car B-004, close B-600 discharging control valve 1 and B-700 discharging control valve 2 simultaneously, after complete above-mentioned steps, open pneumatic control valve and open pneumatic diaphragm pump B-400, until high liquid level warning, stop charging, complete feed supplement process.When need of production soluble additive exports, then close B-500 inlet control valve 1 and B-800 inlet control valve 2, and close all control valves of other storage tanks, open B-600 discharging control valve 1 and B-700 discharging control valve 2 simultaneously, after complete above-mentioned steps, open pneumatic diaphragm pump B-400 outputting material, after reinforced, all valves cut out by subsystem automatically.The turnover of other storage tank materials is consistent with said process.
C-disperses subsystem (as shown in Figure 5).
C-001 is dispersion subsystem signals transmission data line.
C-002 is slurry output channel.
C-003 is water supply pipe.
C-100 ~ 101 are Scattered Kettle.
C-200 ~ 201 are powder temporary storage tank.
C-300 ~ 301 are pulsed sack cleaner.
C-400 ~ 401 are soluble additive feed valve.
C-500 ~ 501 are powder feed valve.
C-600 ~ 601 are screw feeding device.
C-700 ~ 701 are bleeder valve 1.
C-800 ~ 801 are pneumatic diaphragm pump.
C-900 ~ 901 are bleeder valve 2.
Dispersion subsystem mainly production intermediate pulp, utilize computer control subsystem controls order of addition(of ingredients), feed rate and addition, according to the technique rotation speed requirements that subsystem presets, the working order of adjustment Scattered Kettle, reaches the object realizing maximum output by lowest energy consumption.
According to intermediate pulp need of production, subsystem starts production sequence automatically, first required powder is delivered in powder temporary storage tank C-200 ~ C201 through A-powder storage subsystem in advance, secondly by water, soluble additive adds in Scattered Kettle C-100 ~ 101, disperse several minutes, by screw feeding device C-600 ~ 601, powder is slowly delivered in Scattered Kettle by dispersion limit, limit, rate of feeding and jitter time is controlled well according to preset program, in order to effectively promote intermediate pulp dispersion effect, Scattered Kettle spy is equipped with scraping and elevating function, in order to further improving product quality, its scraping and elevating function are controlled by the preset program of control subsystem.After dispersion, through being up to the standards, then direct material is sent into intermediate pulp storage subsystem, otherwise have to pass through sand milling subsystem.The process of sending of material is with starting surge pump C-800 ~ 801 for propulsion source, utilizing pneumatic control subsystem to the control realization of valve.Just for the discharging program of Scattered Kettle C-100, first guarantee that the required bleeder valve except C-100 Scattered Kettle is closing condition, then open C-500 bleeder valve 1 and C-700 bleeder valve 2 successively, the Pneumatic valve that control subsystem opens pneumatic diaphragm pump C-600 can realize the turnover of material.
D-sand milling subsystem (as shown in Figure 6).
D-002 is slurry output channel.
D-100 ~ 101 are vertical grinding machine.
D-200 ~ 201 are feed valve.
D-300 ~ 301 are bleeder valve 1.
D-400 ~ 401 are pneumatic diaphragm pump.
D-500 ~ 501 are bleeder valve 2.
Sand milling subsystem is mainly used in the fineness controlling intermediate pulp product, reaches the abundant finely dispersed object of material by the continuous shock of granulated glass sphere.
This workshop section due to sand milling effect relevant with factors such as product viscosity, mass flow, granulated glass sphere loading levels, therefore Automated condtrol cannot be realized, based on manual operation.In addition, required liquid material utilizes pneumatic or motor-operated control valve control mass flow by pneumatic diaphragm pump.
First intermediate pulp enters sand mill D-100 ~ 101 through a upper workshop section slurry transport lines C-002 by feed valve D-200 ~ 201, after flow of controlling well guarantees that fineness is up to standard, with pneumatic diaphragm pump D-500 ~ 501, delivers to and specifies in intermediate pulp storage tank.
E-intermediate pulp storage subsystem (as shown in Figure 7).In the present invention, this subsystem is divided into seven kinds of intermediate pulp, it is respectively:
Freeze-thaw-agent: as propylene glycol;
Dispersion machine: as Dow Chemical fast easily;
Film coalescence aid: as the Texanol of Yi Shi Man of the U.S.;
Defoamer: as the 681F of French Rhodia;
PH value conditioning agent: as the AMP95 of Dow Chemical company;
Mould inhibitor: as 316 of Dow Chemical;
Alkali swollen thickener: as the TT935 of Dow Chemical;
Associative thickener: as 2020 of Dow Chemical company;
Tensio-active agent: as the NP-10 of Dow Chemical;
Sterilant: as the LXE of Dow Chemical.
Soluble additive storage subsystem components and parts of being correlated with are as described below:
E-001 is intermediate pulp storage subsystem signal transmitted data line.
E-002 is intermediate pulp output channel.
E-100 ~ 106 are intermediate pulp storage tank.
E-200 ~ 206 are liquidometer.
E-300 ~ 306 are vacuum pressure valves.
E-400 ~ 406 are feed valve.
E-500 ~ 506 are bleeder valve 1.
E-600 ~ 606 are pneumatic diaphragm pump.
E-700 ~ 706 are bleeder valve 2.
Intermediate pulp storage subsystem is mainly used in storing the intermediate pulp needed for paint workshop section, to realize high-effect production.
According to formula needs, utilize signal transmitted data line E-001 by information feed back to control subsystem, automatically required intermediate pulp is delivered to by predetermined quantity in the paint mixing kettle of specifying by control subsystem.
Liquidometer E-200 ~ 206 and alarm material high-low-position, during to material low alarm, then remind staff to supplement material in time; When liquid level full level alarm, then require that staff stops reinforced in case material overflows.
The turnover process of material is described with storage tank E-100.As shown in Figure 7, when intermediate pulp then opens C-002 pipeline valve and E-400 feed valve without the need to sand milling simultaneously, pneumatic diaphragm pump charging is utilized.When needs discharging, then open E-500 and E-700 two bleeder valves, other bleeder valves cut out simultaneously, utilize startup surge pump E-600 to be sent by material.Other storage tanks, as example, pass in and out material according to formulary requirements and material storage condition.
F-emulsion storage subsystem (as shown in Figure 9).In the present invention, this subsystem is divided into emulsion in six, it is respectively:
Pure-acrylic emulsion: as the PA237 of German Basf;
Benzene emulsion: as the 998A of Ahmedabad richness;
VAE: as 1608 of Celanese;
Acrylate and vinyl acetate emulsion: as 8353 of Guangdong silver dollar;
Vac-veova emulsion: as the TE-2 of Guangzhou sunrise;
Water-base fluorocarbon emulsion: 4312 of Changxing.
Emulsion storage subsystem components and parts of being correlated with are as described below:
F-001 is emulsion storage subsystem signal transmitted data line.
F-002 is emulsion output channel.
F-003 is emulsion transport tank car.
F-004 is emulsion input pneumatic diaphragm pump.
F-005 is emulsion input channel
F-100 ~ 105 are emulsion storage tank.
F-200 ~ 205 are liquidometer.
F-300 ~ 305 are vacuum pressure valves.
F-400 ~ 405 are feed valve.
F-500 ~ 505 are bleeder valve 1.
F-600 ~ 605 are pneumatic diaphragm pump.
F-700 ~ 705 are bleeder valve 2.
Emulsion storage subsystem is mainly paint workshop section and provides material.By the turnover of production control subsystem controls material.
According to formula needs, utilize signal transmitted data line E-001 by information feed back to control subsystem, automatically required intermediate pulp is delivered to by predetermined quantity in the paint mixing kettle of specifying by control subsystem.
Liquidometer E-200 ~ 206 and alarm material high-low-position, during to material low alarm, then remind staff to supplement material in time; When liquid level full level alarm, then require that staff stops reinforced in case material overflows.
The turnover process of material is described with storage tank E-100.As shown in Figure 7, when intermediate pulp then opens C-002 pipeline valve and E-400 feed valve without the need to sand milling simultaneously, pneumatic diaphragm pump charging is utilized.When needs discharging, then open E-500 and E-700 two bleeder valves, other bleeder valves cut out simultaneously, utilize startup surge pump E-600 to be sent by material.Other storage tanks, as example, pass in and out material according to formulary requirements and material storage condition.
G-paint subsystem.
G-001 is paint subsystem signals transmission data line.
G-002 is finished product output channel.
G-003 is soluble additive test tank.
G-004 is test tank delivery valve.
G-005 is soluble additive feed valve.
G-006 is small serial production emulsion feed valve.
G-007 is small serial production intermediate pulp feed valve.
G-008 is small serial production soluble additive feed valve.
G-009 is small serial production weigher.
G-100 ~ 101 are paint mixing kettle.
G-200 ~ 201 are emulsion feed valve.
G-300 ~ 301 are intermediate pulp feed valve.
G-400 ~ 401 are soluble additive feed valve.
G-500 ~ 501 are finished product bleeder valve.
The materials such as intermediate pulp, soluble additive, emulsion are mainly produced required finished product by the proportioning of different ratios according to formula and order demand by paint subsystem.
Design according to predetermined formulation, utilize signal transmitted data line G-001 by information feed back to control subsystem, automatically the materials such as required intermediate pulp, soluble additive, emulsion are successively added by proportioning and processing requirement by control subsystem, control rotating speed and jitter time well, after through carrying appointed product storage tank or directly filling after the assay was approved.
Large still paint is for paint mixing kettle G-100.As shown in figure 12, first control subsystem is utilized intermediate pulp to be added in paint mixing kettle G-100, the timely feedback data of weighing device is guaranteed accurately reinforced, secondly emulsion is added, finally according to process requirements, soluble additive slowly being dropped into by the mode added while stirring, disperseing can carry out subsequent processing through being up to the standards in several minutes.
Material requested is then pressed recipe requirements by small serial production emulsion feed valve G-006, small serial production intermediate pulp feed valve G-007, small serial production soluble additive feed valve G-008 etc. by small serial production, by small serial production weigher G-009, material is accurately added in tank, utilize mixing machine to carry out mixing.
H-finished product storage subsystem.
H-001 is finished product storage subsystem signal transmitted data line.
H-002 is finished product output channel.
H-100 ~ 107 are finished product storage tank.
H-200 ~ 207 are liquid level control gage.
H-300 ~ 307 are finished product feed valve.
H-400 ~ 407 are vacuum pressure valves.
H-500 ~ 507 are finished product bleeder valve.
Finished product storage subsystem is mainly the rate of utilization of raising paint subsystem and arranges, for storing the relatively high product of sales volume.
Utilize control subsystem to the police of material two position, then remind operator to operate accordingly.Then reminding when being in low liquid level warning operator to carry out in time producing supplementary feed supplement, when material is in high liquid level warning, then reminding operator to stop charging, in case material overflows.
The filling subsystem of I-.
I-100 ~ 101 are full-automatic Bottling Line.
I-200 ~ 201 are feed valve.
I-300 ~ 301 are self-cleaning strainer.
I-400 ~ 401 are for starting surge pump.
Filling subsystem is by starting surge pump I-400 ~ 401 feed, and self-cleaning strainer I-500 ~ 501 filter material, sends into filling subsystem by material by the gate control of pipeline transfer valve and carry out filling, packaging warehouse-in.
Toning subsystem K and toning control subsystem L realizes that factory produces fast, production model mixed colours by the empty bucket that arranges especially without tailing, three-waste free discharge.
Specific practice is integrated together required basic coating and mill base discharge port, utilizes the formula of computer controlled subsystem to produce as required, controls flow well, mix the method for the color coating obtained after filling through mixing machine according to the data feedback of electronic scales.
Manufacture and select the method for intermediate pulp and modulation finished product below by specifically describing.
Starting material of the present invention include but not limited to the above-mentioned material mentioned, wherein:
Powder, as color stuffing, is inorganic materials or Opacifying polymers, and they do not give primary colors or the opacifying power of coating.Dark-colored paint does not usually contain or contains minute quantity white opaque pigment.Comprise titanium dioxide, water-ground limestone, light calcium carbonate, process white, mica powder, kaolin etc.
The white opaque pigment be suitable for comprises titanium dioxide or opacity polymer etc., and wherein opacity polymer comprises space emulsion polymerization composition granule, zinc oxide, plumbous oxide, synthetic polymer pigment and their mixture.Rutile type Titanium Dioxide and anatase thpe white powder are all applicable to the present invention.Rutile type Titanium Dioxide is preferentially selected.Multiple organic surface treatment or inorganic surface treatment can be carried out, such as, with the oxidation of silicon oxide, aluminum oxide or zirconium white to the surface of these titanium dioxides.
Dispersion agent includes but not limited to nonionic, negatively charged ion and cation dispersing agent, amino 2-methyl 1-propyl alcohol (AMP) of such as 2-, dimethylaminoethanol (DMAE), Potassium tripolyphosphate (KTPP), Tripyrophosphoric acid trisodium (TSPP), citric acid and other hydroxy acids etc.Anionic polymer is also suitable for and makes dispersion agent, such as based on homopolymer and the multipolymer of many hydroxy acids, comprise those through hydrophobic or hydrophilic modifying, such as, with the polypropylene of various of monomer such as vinylbenzene, diisobutylene and other hydrophobic or hydrophilic co-monomer modifications or polymethyl acrylic acid or maleic anhydride.
Defoamer comprises defoamer based on silicone oil and mineral oil and resemblance.
Solvent comprises ethylene glycol, propylene glycol, hexylene glycol, 2,2,4-trimethylammonium-1,3-pentanediol mono isobutyrates (TEXANOL), glycol ether, solvent oil, methyl carbitol, butyl carbitol, phthalic ester, adipic acid ester etc.
Emulsion comprises and is singly not limited to ACRYLIC EMULSION, venamul, styrene-acrylic emulsion, styrene butadiene emulsion, vinyl acetate-acrylic emulsion, ethylene-vinyl acetate emulsion, the homopolymer of vinyl-acetic ester-branched paraffin hydroxy acid vinyl acetate emulsion, vinyl-acetic ester-maleat emulsion, acetate-vinyl chloride-ACRYLIC EMULSION, ethane-acetic acid ethyenyl ester-ACRYLIC EMULSION and their mixture, multipolymer or terpolymer.
Thickening material a kind ofly adds in coating any material changing rheological.Preferred thickening material is associative thickener.The thickening material that the present invention is suitable for comprises polyvinyl alcohol (PVA), hydrophobically modified caustic solubility milk sap (HASE), caustic solubility milk sap (ASE), hydrophobically modified propylene oxide-polyurethane emulsion (HEUR) and cellulose thickener, such as Walocel MT 20.000PV (HMC), Natvosol (HEC), Natrosol Plus (HMHEC), sodium cellulose glycolate (SCMC), methylol 2-sodium hydroxyethyl cellulose, 2-Vltra tears, 2-hydroxyethylmethyl-cellulose, 2-hydroxy butyl methyl cellulose, 2-hydroxyethyl ethylcellulose, 2-hydroxypropylcellulose etc.
The mould inhibitor be suitable for and sterilant comprise zinc oxide, isothiazolinone, triazole etc.
The tensio-active agent be suitable for comprises positively charged ion, negatively charged ion and nonionogenic tenside.
Intermediate pulp needs the scope of the key property considered required for production system, and sets a series of intermediate pulp, and these intermediate pulp can be obtained by mixing the required key property of coating production line with multiple combination.The amount of the intermediate pulp needed for formula will determine flexibly according to required final coating.Some property can be improved by adding the additive improving advantageous property.Need take into full account during design intermediate pulp and can realize its wide in range property of filling a prescription desired properties and reach optimization.
One of ordinary skill in the art will appreciate that: accompanying drawing is the schematic diagram of an embodiment, the unit in accompanying drawing or flow process might not be that enforcement the present invention is necessary.
In several embodiments that the application provides, should be understood that, disclosed system, equipment and method, can realize by another way.Such as, apparatus embodiments described above is only schematic, such as, the division of described unit, be only a kind of logic function to divide, actual can have other dividing mode when realizing, such as multiple unit or assembly can in conjunction with or another system can be integrated into, or some features can be ignored, or do not perform.Another point, shown or discussed coupling each other or direct-coupling or communication connection can be by some interfaces, and the indirect coupling of equipment or unit or communication connection can be electrical, machinery or other form.
The described unit illustrated as separating component or can may not be and physically separates, and the parts as unit display can be or may not be physical location, namely can be positioned at a place, or also can be distributed on multiple NE.Some or all of unit wherein can be selected according to the actual needs to realize the object of the present embodiment scheme.
In addition, each functional unit in each embodiment of the present invention can be integrated in a processing unit, also can be that the independent physics of unit exists, also can two or more unit in a unit integrated.Above-mentioned integrated unit both can adopt the form of hardware to realize, and the form that hardware also can be adopted to add SFU software functional unit realizes.
The above-mentioned integrated unit realized with the form of SFU software functional unit, can be stored in a computer read/write memory medium.Above-mentioned SFU software functional unit is stored in a storage media, comprising some instructions in order to make a computer equipment (can be Personal Computer, server, or the network equipment etc.) perform the part steps of method described in each embodiment of the present invention.And aforesaid storage media comprises: USB flash disk, portable hard drive, read-only storage (Read-Only Memory, be called for short ROM), random access memory (Random Access Memory, be called for short RAM), magnetic disc or CD etc. various can be program code stored medium.
Last it is noted that above embodiment is only in order to illustrate technical scheme of the present invention, be not intended to limit; Although with reference to previous embodiment to invention has been detailed description, those of ordinary skill in the art is to be understood that: it still can be modified to the technical scheme described in foregoing embodiments, or carries out equivalent replacement to wherein portion of techniques feature; And these amendments or replacement, do not make the essence of appropriate technical solution depart from the spirit and scope of various embodiments of the present invention technical scheme.
Claims (8)
1. the coating manufacturing system of a distribute type environmental protection, it is characterized in that, comprise powder storage subsystem, soluble additive storage subsystem, dispersion subsystem, sand milling subsystem, intermediate pulp storage subsystem, emulsion storage subsystem, paint subsystem, finished product storage subsystem, filling subsystem and production control subsystem
Described powder storage subsystem is made up of multiple powder storage tank and multiple powder conveying components and parts, for storing powder and being carried out the conveying of powder by production control subsystem;
Described soluble additive storage subsystem carries components and parts to form, for providing starting material for described dispersion subsystem and described paint subsystem by multiple soluble additive storage tank and multiple soluble additive;
Described dispersion subsystem forms, for the production of intermediate pulp by by multiple Scattered Kettle and multiple dispersion components and parts;
Described frosted subsystem comprises multiple stage skin grinder, for controlling the fineness of intermediate pulp product;
Described intermediate pulp storage subsystem is made up of, for storing the intermediate pulp needed for paint workshop section multiple intermediate pulp storage tank and multiple storage components and parts;
Described emulsion storage subsystem is made up of multiple emulsion storage tank and emulsion components and parts, and for paint, workshop section provides material;
Described paint subsystem is made up of multiple paint mixing kettle, short run distribution plant and paint components and parts, for the materials such as intermediate pulp, soluble additive, emulsion being produced required finished product by the proportioning of different ratios according to formula and order demand;
Described finished product storage subsystem is made up of, for storing finished product multiple finished product storage tank and finished product components and parts;
Described filling subsystem is made up of multiple full-automatic Bottling Line and semi-automatic packer, for being undertaken filling by material;
Described production control subsystem comprises multiple treater and recipe database, for controlling the store content of material in above-mentioned each subsystem, and controls the flow of described material, beginning and end time of components and parts and rotating speed in above-mentioned each subsystem.
2. system according to claim 1, it is characterized in that, described production control subsystem is also for determining the instruction of formula for a product ratio, and according to the indication information of order coating type of input, to be dispensed in described paint subsystem without the intermediate pulp of classification, emulsion, then open described paint mixing kettle by the rotating speed pre-seted, progressively also dispersion adds in paint mixing kettle described in defoamer, mould inhibitor, thickening material value.
3. system according to claim 1 and 2, it is characterized in that, described production control subsystem also comprises sensor, the data of described computer subsystem Real-time Obtaining sensor, according to formula and the flow of processing requirement dynamic conditioning material and the opened condition of equipment.
4. system according to claim 1, it is characterized in that, described production control subsystem also comprises some electronic or startup adjustable valves, enters the different flow producing the input aperture of subsystem for adjusting, and signal is sent to control subsystem, control some valves each.
5. system according to claim 1, it is characterized in that, described production control subsystem also comprises alarm module, when intermediate pulp reserves are lower than set(ting)value, described production control subsystem is by alarm module automatic alarm, and start slurry production sequence, utilize pipeline that production raw material is sent into described dispersion subsystem, open Scattered Kettle also by rotating speed and the time dispersion of processing requirement formulation, by control subsystem, the powder in powder storage subsystem is sent in Scattered Kettle, described production control subsystem also comprises Weighing module, powder conveying amount is constantly modulated to guarantee to meet formulary requirements by the real time data feedback of Weighing module, and automatically adjust rotating speed to high speed according to technique, control jitter time, through delivering to intermediate pulp storage tank after the assay was approved.
6. system according to claim 5, is characterized in that, constantly modulates powder conveying amount to guarantee to meet formulary requirements, comprising by the real time data feedback of Weighing module:
Described production control subsystem start in time according to real-time weight data feedback or valve-off to guarantee that required material meets the demand of formula.
7. the system according to claim 5 or 6, it is characterized in that, described production control subsystem also for: when finished product storage tank low memory is in set(ting)value, described production control subsystem is by alarm module automatic alarm, and start finished product production sequence, utilize pipeline that production raw material is sent into paint subsystem by control subsystem, open paint mixing kettle also by rotating speed and the time dispersion of processing requirement formulation, by control subsystem by defoamer, the auxiliary agents such as thickening material slowly add in paint mixing kettle, subsystem adjusts rotating speed automatically according to technique, control jitter time, through delivering in finished product storage tank after the assay was approved.
8. the system according to any one of claim 5-7, is characterized in that, when all soluble additive storage tanks, powder storage tank, emulsion storage tank storage are lower than set(ting)value, described production control subsystem, by automatic alarm, reminds the timely feed supplement of operator.
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Cited By (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105169981A (en) * | 2015-08-12 | 2015-12-23 | 东莞兆舜有机硅科技股份有限公司 | Production method of electronic-pouring sealant |
| CN105676813A (en) * | 2016-01-06 | 2016-06-15 | 惠州东方雨虹建筑材料有限责任公司 | Pipeline monitoring system for water-based pigment make-up system in pigment coating workshop |
| CN106338314A (en) * | 2016-09-21 | 2017-01-18 | 北京瑞思达化工设备有限公司 | Control method for powdery solid material metering |
| CN107159042A (en) * | 2017-05-10 | 2017-09-15 | 苏州弗克技术股份有限公司 | A kind of zero-discharge production process of architectural coating paste materials |
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Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1230731A (en) * | 1997-11-10 | 1999-10-06 | 巴斯福公司 | Computerized virtual paint manufacturing and application system |
| CN1317521A (en) * | 2000-02-18 | 2001-10-17 | 约翰·迈克尔·弗里尔 | Distributing paint mfg. system |
| WO2006040033A1 (en) * | 2004-10-14 | 2006-04-20 | Imperial Chemical Industries Plc | A tinting machine system |
| CN101040013A (en) * | 2004-11-18 | 2007-09-19 | 关西涂料株式会社 | Paint producing method and paint producing system |
| CN101352665A (en) * | 2007-06-01 | 2009-01-28 | 微混技术有限公司 | Method and apparatus for producing paint |
| CN101537322A (en) * | 2008-03-19 | 2009-09-23 | 刘俊才 | Process for producing fully-automatic integrative paint complete equipment |
-
2013
- 2013-11-22 CN CN201310598090.4A patent/CN104650677A/en active Pending
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1230731A (en) * | 1997-11-10 | 1999-10-06 | 巴斯福公司 | Computerized virtual paint manufacturing and application system |
| CN1317521A (en) * | 2000-02-18 | 2001-10-17 | 约翰·迈克尔·弗里尔 | Distributing paint mfg. system |
| WO2006040033A1 (en) * | 2004-10-14 | 2006-04-20 | Imperial Chemical Industries Plc | A tinting machine system |
| CN101040013A (en) * | 2004-11-18 | 2007-09-19 | 关西涂料株式会社 | Paint producing method and paint producing system |
| CN101352665A (en) * | 2007-06-01 | 2009-01-28 | 微混技术有限公司 | Method and apparatus for producing paint |
| CN101537322A (en) * | 2008-03-19 | 2009-09-23 | 刘俊才 | Process for producing fully-automatic integrative paint complete equipment |
Cited By (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105169981A (en) * | 2015-08-12 | 2015-12-23 | 东莞兆舜有机硅科技股份有限公司 | Production method of electronic-pouring sealant |
| CN105676813A (en) * | 2016-01-06 | 2016-06-15 | 惠州东方雨虹建筑材料有限责任公司 | Pipeline monitoring system for water-based pigment make-up system in pigment coating workshop |
| CN106338314A (en) * | 2016-09-21 | 2017-01-18 | 北京瑞思达化工设备有限公司 | Control method for powdery solid material metering |
| CN107159042A (en) * | 2017-05-10 | 2017-09-15 | 苏州弗克技术股份有限公司 | A kind of zero-discharge production process of architectural coating paste materials |
| CN108479628A (en) * | 2018-04-10 | 2018-09-04 | 广东金宝力化工科技装备股份有限公司 | A kind of high-effect automatic production line of building coating |
| CN111632510A (en) * | 2020-06-28 | 2020-09-08 | 三棵树涂料股份有限公司 | Closed coating manufacturing system and method |
| CN111849235A (en) * | 2020-08-21 | 2020-10-30 | 西卡(上海)管理有限公司 | Normal-pressure continuous production method and production system for interior wall putty paste |
| CN114851394A (en) * | 2022-05-23 | 2022-08-05 | 江苏方达正塬电子材料科技有限公司 | Ceramic slurry automatic production line |
| CN114851394B (en) * | 2022-05-23 | 2023-08-08 | 江苏方达正塬电子材料科技有限公司 | Ceramic slurry automatic production line |
| CN115889409A (en) * | 2022-11-11 | 2023-04-04 | 茌平信源环保建材有限公司 | System for realize online useless gypsum board recycle |
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Application publication date: 20150527 |