CN205398127U - Production facility of likepowder sodium silicate - Google Patents
Production facility of likepowder sodium silicate Download PDFInfo
- Publication number
- CN205398127U CN205398127U CN201620142971.4U CN201620142971U CN205398127U CN 205398127 U CN205398127 U CN 205398127U CN 201620142971 U CN201620142971 U CN 201620142971U CN 205398127 U CN205398127 U CN 205398127U
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- sodium silicate
- production equipment
- powdery sodium
- tank
- likepowder
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Abstract
The utility model discloses a production facility of likepowder sodium silicate aims at solving the problem that drying effect is poor, and its technical scheme main points are production facility of likepowder sodium silicate, packetize material jar and with change the bin stock pond that the material jar is connected, it is equipped with the dust remover to change material jar top, bin stock pond one end is connected with the deckle board pressure filter through the charging pump, deckle board pressure filter one end is connected with the mixture jar, mixture jar lower extreme is connected with the reaction through the charging pump, the reaction lower extreme is connected with spray drier, the last cloth screen that is connected with of spray drier, the spray drier lower extreme is connected with the screw feeding ware, screw feeding ware one end is connected with rotatory dry bed, rotatory dry bed is connected with the cooler. The utility model discloses a likepowder sodium silicate drying effect is good, avoids extravagant in the production process.
Description
Technical field
This utility model relates to a kind of waterglass processing production equipment field, more specifically, it relates to the production equipment of a kind of powdery sodium silicate.
Background technology
Sodium silicate is commonly called as sodium silicate, is a kind of water-soluble silicate, and its aqueous solution is commonly called as waterglass, is a kind of ore deposit adhesive.Its chemical formula is R2O nSiO2, and in formula, R2O is alkali metal oxide, and n is the ratio of silicon dioxide and alkali metal oxide molal quantity, is called the number that rubs of waterglass.It is used to manufacture the various silicates products such as silica gel, white carbon, zeolite molecular sieve, metasilicate pentahydrate sodium, Ludox, layer silicon and instant powdery sodium silicate, sodium potassium silicate at chemical system, is the base stock of silicon compound.In developed country, having evolved to more than 50 kinds with the deep processing series of products that sodium silicate is raw material, some has been applied to high, precision and frontier sciemtifec and technical sphere;Light industry is indispensable raw material in the detergent such as detergent, soap, is also water softener, settling agent;Textile industry is used for help dye, bleaching and sizing;Machinery industry is widely used in casting, emery wheel manufacture and anticolodal etc.;Building trade is used for manufacture quick hardening cement, acid-resistant cement dubbin, soil-solidified-agent, refractory material etc.;Agriculturally can manufacture silicon element fertilizer material;Additionally may act as exotic material, anticolodal, water softener, detergent builders, refractory material and Ceramic Material, the drift of textile, dye and slurry, mine ore dressing, waterproof, leak stopping, fire retarding wood protection, food antiseptic and the preparing adhesives etc. such as the silica-alumina catalyst of petroleum catalytic cracking, the filler of soap, the adhesive of corrugated paper, laboratory crucibles and enumerate problem, but sodium silicate there will be wall sticking phenomenon in process of production, thus causing that material moisture exceeds standard, have a strong impact on the quality of sodium silicate product.
For the problems referred to above, application number is the disclosed a kind of production powdery sodium silicate production equipment of Chinese patent of 201420791116.7, what change scheme has technical point that a kind of production powdery sodium silicate production equipment, including material tank, and material-stored pool tank connected with material;Described material-stored pool one end is connected to filter by feeding engine;Described filter one end is connected to joins mould tank;Described mould tank lower end of joining is connected to blender by feeding engine;Described blender lower end is connected to spray dryer;Described spray dryer lower end is connected to conveying worm;Described conveying worm one end is connected to cooling vibrated bed;This utility model realizes the spray drying to mixing liquid, and drying efficiency is high, and energy consumption is low, and the sodium silicate quality of production is good, solves sodium silicate and wall sticking phenomenon occurs when using drying equipment to be dried, improves the product quality of sodium silicate.But sodium silicate contains substantial amounts of moisture before entering drying equipment in this production equipment, cause that drying equipment processing speed is slower, and drying time is shorter, sodium silicate is not dried fully, and the problem easily producing dust waste aborning, it is therefore desirable to a kind of new scheme is proposed to solve this problem.
Utility model content
For the deficiency that prior art exists, the purpose of this utility model is in that to provide a kind of drying effect good, and efficiency is high, it is to avoid the production equipment of a kind of powdery sodium silicate of waste.
Above-mentioned technical purpose of the present utility model has the technical scheme that the production equipment of a kind of powdery sodium silicate, including material tank and material-stored pool tank connected with material, described material tank is arranged over cleaner unit, described material-stored pool one end is connected to deckle board pressure filter by feeding engine, described deckle board pressure filter one end is connected to mixing batch can, described mixing batch can lower end is connected to reactive tank by feeding engine, described reactive tank lower end is connected to spray dryer, described spray dryer is connected to bagroom, described spray dryer lower end is connected to feeding screw, described feeding screw one end is connected to Rotary drying bed, described Rotary drying bed is connected to cooler.
nullBy adopting technique scheme,Material tank adds the raw material producing sodium silicate,A large amount of dust is easily produced in reinforced,It is arranged over cleaner unit at material tank,Cleaner unit can absorb certain dust,It has been connected below material-stored pool at material tank,Mixed material is temporarily stored in material-stored pool,Material is temporary fusion in material-stored pool,Delivered in deckle board pressure filter by feeding engine,Carry out contaminant filter,Then pass through pipeline and be transported to mixing batch can,Mixing batch can adds adjuvant,Then static state deposition is carried out,It is transported to reactive tank by feeding engine,Reactive tank stirring material,Material is fully merged,Can accelerate to merge speed,Spray dryer is passed into by pipeline by the material after merging,Material is dried and with by material production powdering,Spraying needs material atomisation in process of production,Itself and hot air is made to be dried,Major part be dried after sodium silicate fall in spray dryer,Some can waft aloft,It is connected to cloth dust-precipitator by spraying feeder,The aerial powdery sodium silicate that will waft is collected in cloth bag,Cloth bag can prevent powdery sodium silicate from touching water,The quality of powdery sodium silicate will not be destroyed,Feeding screw is connected in spray dryer lower end,The powdery sodium silicate produced is sent to Rotary drying bed,Carry out second time dry,Improve product quality,Finally the powdery sodium silicate on Rotary drying bed is sent into cooler to cool down,Complete to produce.
This utility model is further arranged to: described cleaner unit is fixedly connected with the hood for protecting rider above the charge door for covering on material tank.
By adopting technique scheme, in reinforced process, in order to make cleaner unit reach best dust removing effects, above material tank, blackout hood for protecting rider, increases the absorption region of cleaner unit.
This utility model is further arranged to: described hood for protecting rider is fixedly connected with water jet.
By adopting technique scheme, further enhance dust removing effects, hood for protecting rider is provided with water jet, instead of, in reinforced, the process added water, moreover it is possible to reach the effect of dedusting.
This utility model is further arranged to: be provided with effusion meter between described mixing batch can and reactive tank.
By adopting technique scheme, the quality of the mixing effect of reactive tank directly influences the quality of product, adds effusion meter between mixing batch can and reactive tank, and operator by the numerical monitor of effusion meter, can control the amount of reactive tank stirring.
This utility model is further arranged to: described reactive tank is provided with observation panel.
By adopting technique scheme, for the stirring state in real time reaction reactive tank, reactive tank is provided with observation panel, it is provided that the stirring state in operator's observing response groove at any time.
This utility model is further arranged to: be provided with drying tube between described feeding screw and Rotary drying bed and Rotary drying bed and cooler.
By adopting technique scheme, liquid sodium silicate is made for powdery by spray dryer, remove the moisture of 95% ~ 98%, in order to further enhance drying effect, it is equipped with drying tube so that powdery sodium silicate is further dried between feeding screw and Rotary drying bed and Rotary drying bed and cooler.
This utility model is further arranged to: described bagroom is connected with blower fan respectively, and the discharging opening of described bagroom and feeding screw connect.
By adopting technique scheme, bagroom is collected in cloth bag by the wind-force of the blower fan aerial powdery sodium silicate that will waft, and is then delivered in feeding screw, it is to avoid waste.
In sum, this utility model has the advantages that by repeatedly drying powdery, improves drying effect, thus improving the quality of product;It is arranged above cleaner unit at charging aperture and bagroom is installed by spray dryer, the utilization rate of material can be improved, it is to avoid waste, reducing production cost.
Accompanying drawing explanation
Fig. 1 is the structural representation of the present embodiment;
In figure: 1, material tank;2, material-stored pool;3, cleaner unit;4, deckle board pressure filter;5, mixing batch can;6, reactive tank;7, spray dryer;8, bagroom;9, feeding screw;10, Rotary drying bed;11, cooler;12, effusion meter;13, blower fan.
Detailed description of the invention
Below in conjunction with drawings and Examples, this utility model is described in detail.
nullAs shown in Figure 1,Material tank 1 adds the raw material producing sodium silicate,A large amount of dust is easily produced in reinforced,It is arranged over cleaner unit 3 at material tank 1,Cleaner unit 3 can absorb certain dust,Cleaner unit 3 is also fixedly connected with the hood for protecting rider above the charge door for covering on material tank 1,Increase the absorption region of cleaner unit 3,It is fixedly connected with water jet at hood for protecting rider,Instead of the process additionally added water in reinforced process and can also play the effect of dedusting,It has been connected below material-stored pool 2 at material tank 1,Mixed material is temporarily stored in material-stored pool 2,Material is temporary fusion in material-stored pool 2,Delivered in deckle board pressure filter 4 by feeding engine,Carry out contaminant filter,Then pass through pipeline and be transported to mixing batch can 5,Mixing batch can 5 adds adjuvant,Then static state deposition is carried out,It is transported to reactive tank 6 by feeding engine,It is provided with effusion meter 12 between mixing batch can 5 and reactive tank 6,Operator can pass through the numerical monitor of effusion meter 12,Control the amount of reactive tank 6 stirring,Reactive tank 6 stirs material,Material is fully merged,Can accelerate to merge speed,Reactive tank 6 is provided with observation panel,Operator can pass through the stirring state in observation panel Real Time Observation reactive tank 6,Spray dryer 7 is passed into by pipeline by the material after merging,Material is dried and with by material production powdering,Spraying needs material atomisation in process of production,Itself and hot air is made to be dried,Major part be dried after sodium silicate fall in spray dryer 7,Some can waft aloft,It is connected to cloth dust-precipitator by spraying feeder,The aerial powdery sodium silicate that will waft is collected in cloth bag,Cloth bag can prevent powdery sodium silicate from touching water,The quality of powdery sodium silicate will not be destroyed,Feeding screw 9 is connected in spray dryer 7 lower end,The powdery sodium silicate produced is sent to Rotary drying bed 10 by drying tube,Carry out second time dry,Improve product quality,Finally by drying tube, the powdery sodium silicate on Rotary drying bed 10 is sent into cooler 11 to cool down,Complete to produce.By such scheme, the good powdery sodium silicate of drying effect can be produced, also be avoided that waste in process of production simultaneously.
The above is only preferred implementation of the present utility model, and protection domain of the present utility model is not limited merely to above-described embodiment, and all technical schemes belonged under this utility model thinking belong to protection domain of the present utility model.It should be pointed out that, for those skilled in the art, without departing from the some improvements and modifications under this utility model principle premise, these improvements and modifications also should be regarded as protection domain of the present utility model.
Claims (7)
- null1. the production equipment of a powdery sodium silicate,It is characterized in that: include material tank (1) and the material-stored pool (2) being connected with material tank (1),Described material tank (1) is arranged over cleaner unit (3),Described material-stored pool (2) one end is connected to deckle board pressure filter (4) by feeding engine,Described deckle board pressure filter (4) one end is connected to mixing batch can (5),Described mixing batch can (5) lower end is connected to reactive tank (6) by feeding engine,Described reactive tank (6) lower end is connected to spray dryer (7),Described spray dryer (7) is connected to bagroom (8),Described spray dryer (7) lower end is connected to feeding screw (9),Described feeding screw (9) one end is connected to Rotary drying bed (10),Described Rotary drying bed (10) is connected to cooler (11).
- 2. the production equipment of a kind of powdery sodium silicate according to claim 1, it is characterised in that: described cleaner unit (3) is fixedly connected with the hood for protecting rider above the charge door for covering on material tank (1).
- 3. the production equipment of a kind of powdery sodium silicate according to claim 2, it is characterised in that: described hood for protecting rider is fixedly connected with water jet.
- 4. the production equipment of a kind of powdery sodium silicate according to claim 1, it is characterised in that: it is provided with effusion meter (12) between described mixing batch can (5) and reactive tank (6).
- 5. the production equipment of a kind of powdery sodium silicate according to claim 4, it is characterised in that: described reactive tank (6) is provided with observation panel.
- 6. the production equipment of a kind of powdery sodium silicate according to claim 1, it is characterised in that: it is provided with drying tube between described feeding screw (9) and Rotary drying bed (10) and Rotary drying bed (10) and cooler (11).
- 7. the production equipment of a kind of powdery sodium silicate according to claim 1, it is characterized in that: described bagroom (8) is connected with blower fan (13) respectively, the discharging opening of described bagroom (8) and feeding screw (9) connect.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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CN201620142971.4U CN205398127U (en) | 2016-02-25 | 2016-02-25 | Production facility of likepowder sodium silicate |
Applications Claiming Priority (1)
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CN201620142971.4U CN205398127U (en) | 2016-02-25 | 2016-02-25 | Production facility of likepowder sodium silicate |
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CN205398127U true CN205398127U (en) | 2016-07-27 |
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CN201620142971.4U Expired - Fee Related CN205398127U (en) | 2016-02-25 | 2016-02-25 | Production facility of likepowder sodium silicate |
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Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN109036830A (en) * | 2018-09-18 | 2018-12-18 | 钱光宝 | Magnetic coarse powder system of processing |
-
2016
- 2016-02-25 CN CN201620142971.4U patent/CN205398127U/en not_active Expired - Fee Related
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN109036830A (en) * | 2018-09-18 | 2018-12-18 | 钱光宝 | Magnetic coarse powder system of processing |
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C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20160727 Termination date: 20210225 |
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CF01 | Termination of patent right due to non-payment of annual fee |