CN204051602U - A kind of hollow cone type spray cooling granulation equipment - Google Patents
A kind of hollow cone type spray cooling granulation equipment Download PDFInfo
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- CN204051602U CN204051602U CN201420500090.6U CN201420500090U CN204051602U CN 204051602 U CN204051602 U CN 204051602U CN 201420500090 U CN201420500090 U CN 201420500090U CN 204051602 U CN204051602 U CN 204051602U
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- cooling tower
- hollow cone
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- sprayer
- deduster
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Abstract
The utility model discloses a kind of hollow cone type spray cooling granulating device, feature is: be made up of feed pump, cooling tower, sprayer, air-cooler, Blowing stopper, deduster, air-introduced machine, fused materials input pipe is connected with the top sprayer be arranged in cooling tower by feed pump, the heat outlet at cooling tower top is connected with the import of deduster, and the outlet of deduster is connected with the import of air-introduced machine; Material outlet bottom cooling tower is connected with the import of Blowing stopper, and the outlet of air-cooler extend into cooling tower bottom and opening up from the lower sides of cooling tower, cold wind being entered in the middle of cooling tower bottom by rising gas cap, allowing solid particle cool in time.Sprayer is made up of the hollow cone nozzles of a hollow cone nozzles or two or more parallel connection.The utility model have kind simple and practical, with strong points, production process without dust, good product mobility, uniform particles, be convenient to mutual blending, add the advantages such as easy to use.
Description
Technical field
The utility model relates to spray-cooling granulating field, especially relates to a kind of hollow cone type spray cooling granulation equipment.
Background technology
The amide-type products such as oleamide, erucyl amide and stearic amide are the very important interpolation auxiliary agents of rubber and plastic industry.Along with the fast development of China's rubber and plastic industry, demand significantly increases, and also constantly upgrades to the requirement of product quality, especially requires the good fluidity of product, uniform particles, is convenient to the even blending with materials such as resins, without dust harzard.The traditional forming method of this series products adopts cooling water indirectly to cool, cut into slices again after solidification, the semi-finished product of sheet are ground into powdery product by airslide disintegrating mill, product is irregular powder, and the apparent density of product and domain size distribution are difficult to control, in the package handling and interpolation use procedure of product, easily produce dust, labour intensity is large, energy consumption is high, and powder is easily reunited caking, add use very inconvenient.
Patent CN201454488U, the structure of sprayer and air sparger is more complicated, and directly contacts with air at high temperature section material, easily affects the color and luster of product, especially inapplicable to the thermal sensitivity such as oleamide and erucyl amide product.
Patent CN201300047Y, equipment is more complicated, and rotating sprinkler is for fatty acid acyl amine products such as the low oleamide of viscosity and erucyl amides, and easily sticky wall, process units is difficult to normal operation, lacks specific aim and practicality.
Summary of the invention
The purpose of this utility model there are provided a kind of simple and practical, with strong points, small investment, operating cost are low, production process non-dusting hollow cone type spray cooling granulation equipment, by good product mobility, uniform particles that this equipment is obtained, be convenient to mutual blending, add easy to use.
The purpose of this utility model is achieved in that
A kind of hollow cone type spray cooling granulating device, feature is: by feed pump, cooling tower, sprayer, air-cooler, Blowing stopper, deduster, air-introduced machine forms, the discharging opening of fused materials input pipe with fused materials transfer valve is connected with the charging aperture of feed pump, sprayer is arranged on the top in cooling tower, the discharging opening of feed pump to be extend in cooling tower from the top of cooling tower by conveying pipeline and is connected with the charging aperture of sprayer, the heat outlet at cooling tower top is connected with the import of deduster, the outlet of deduster is connected with the import of air-introduced machine, the heat that deduster and the air-introduced machine material of drawing in time in cooling tower produces when solidifying, material outlet bottom cooling tower is connected with the import of Blowing stopper, the outlet of air-cooler to extend in the middle of cooling tower bottom and opening up from the lower sides of cooling tower, cold wind being entered in the middle of cooling tower bottom from by rising gas cap, allowing the solid particle solidifying from top and settle down contact with cold wind reverse flow uniform and cooling in time.
Sprayer is made up of the hollow cone nozzles of a hollow cone nozzles or two or more parallel connection, wherein: hollow cone nozzles is made up of nozzle body, corner eddy flow chamber, taper spray orifice, material inlet.
The cold wind temperature of air-cooler controls at 6-8 DEG C, guarantees that middle and lower part temperature in cooling tower is lower than 35 DEG C.
The utility model is made up of feed pump, cooling tower, sprayer, air-cooler, Blowing stopper, deduster, air-introduced machine, fused materials is sent in the sprayer in cooling tower by feed pump, sprayed from the top down by the hollow cone nozzles in sprayer, now cold wind blows out by air-cooler from bottom to top, allow the timely cooled and solidified of atomization shape material of melting, form solid particle, be deposited in the material outlet bottom cooling tower, and flow out cooling tower by self gravitation; And the heat that the atomization shape material of melting produces when cooled and solidified is drawn in time by deduster and air-introduced machine, make the middle and lower part temperature of cooling tower lower than 35 DEG C.
The utility model have kind simple and practical, with strong points, small investment, production process without dust, good product mobility, uniform particles, be convenient to mutual blending, add advantage that is easy to use, economical and practical, low cost of manufacture.
The utility model can substitute traditional cooling section and Jet Mill, for the primary fatty acids such as oleamide and erucyl amide amide products, the bisamide products such as the two-12-hydroxy stearic acid acid amides of ethylene and the two oleamides of ethylene, and the cooling forming of the secondary amide product such as stearyl erucamide and octadecyl stearmide.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model;
Fig. 2 is the structural representation of hollow cone nozzles.
Detailed description of the invention
Contrast accompanying drawing below in conjunction with embodiment the utility model is described in further detail.
A kind of hollow cone type spray cooling granulating device, by feed pump 1, cooling tower 4, sprayer 3, air-cooler 2, Blowing stopper 5, deduster 6, air-introduced machine 7 forms, discharging opening with the fused materials input pipe 9 of fused materials transfer valve 8 is connected with the charging aperture of feed pump 1, sprayer 3 is arranged on the top in cooling tower 4, the discharging opening of feed pump 1 to be extend in cooling tower from the top of cooling tower 4 by conveying pipeline 10 and is connected with the charging aperture of sprayer 3, the heat outlet at cooling tower 4 top is connected with the import of deduster 6, the outlet of deduster 6 is connected with the import of air-introduced machine 7, the heat that deduster 6 and air-introduced machine 7 produce when the material of drawing in cooling chamber 11 solidifies in time, material outlet bottom cooling tower 4 is connected with the import of Blowing stopper 5, the outlet of air-cooler 2 to extend into cooling tower and opening up from the lower sides of cooling tower 4, make cold wind pass through to rise gas cap 11 to enter in the middle of cooling tower 4 bottom, allow the solid particle solidifying from top and settle down contact with cold wind reverse flow uniform and cool in time.
Sprayer 3 is made up of the hollow cone nozzles 12 of a hollow cone nozzles 12 or two or more parallel connection, wherein: hollow cone nozzles 12 is made up of nozzle body 12-1, corner eddy flow chamber 12-2, taper spray orifice 12-3, material inlet 12-4.
The cold wind temperature of air-cooler 2 controls at 6-8 DEG C, guarantees that middle and lower part temperature in cooling tower is lower than 35 DEG C.
Claims (3)
1. a hollow cone type spray cooling granulating device, it is characterized in that: be made up of feed pump, cooling tower, sprayer, air-cooler, Blowing stopper, deduster, air-introduced machine, the discharging opening of fused materials input pipe with fused materials transfer valve is connected with the charging aperture of feed pump, sprayer is arranged on the top in cooling tower, the discharging opening of feed pump to be extend in cooling tower from the top of cooling tower by conveying pipeline and is connected with the charging aperture of sprayer, the heat outlet at cooling tower top is connected with the import of deduster, and the outlet of deduster is connected with the import of air-introduced machine; Material outlet bottom cooling tower is connected with the import of Blowing stopper, and the outlet of air-cooler to extend in the middle of cooling tower bottom and opening up from the lower sides of cooling tower.
2. hollow cone type spray cooling granulating device according to claim 1, it is characterized in that: sprayer is made up of the hollow cone nozzles of a hollow cone nozzles or two or more parallel connection, wherein: hollow cone nozzles is made up of nozzle body, corner eddy flow chamber, taper spray orifice, material inlet.
3. hollow cone type spray cooling granulating device according to claim 1, is characterized in that: the cold wind temperature of air-cooler controls at 6-8 DEG C, guarantees that middle and lower part temperature in cooling tower is lower than 35 DEG C.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420500090.6U CN204051602U (en) | 2014-09-02 | 2014-09-02 | A kind of hollow cone type spray cooling granulation equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420500090.6U CN204051602U (en) | 2014-09-02 | 2014-09-02 | A kind of hollow cone type spray cooling granulation equipment |
Publications (1)
| Publication Number | Publication Date |
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| CN204051602U true CN204051602U (en) | 2014-12-31 |
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| CN201420500090.6U Active CN204051602U (en) | 2014-09-02 | 2014-09-02 | A kind of hollow cone type spray cooling granulation equipment |
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| CN (1) | CN204051602U (en) |
Cited By (10)
| Publication number | Priority date | Publication date | Assignee | Title |
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| CN105482156A (en) * | 2016-01-18 | 2016-04-13 | 佟立新 | Bead-shaped granular composite plastic additive, preparation method and application thereof |
| CN105504348A (en) * | 2016-01-18 | 2016-04-20 | 佟立新 | Bead-shaped granular antioxidant 1010 as well as preparation method and application thereof |
| CN105542224A (en) * | 2016-01-18 | 2016-05-04 | 佟立新 | Bead-shaped granular antioxidant 1076 as well as preparation method and application thereof |
| CN105601999A (en) * | 2016-01-18 | 2016-05-25 | 佟立新 | Antioxidant 168 in shape of bead-shaped particles and preparation method and application thereof |
| CN105601998A (en) * | 2016-01-18 | 2016-05-25 | 佟立新 | Antioxidant in shape of bead-shaped particles and preparation method and application thereof |
| CN105601997A (en) * | 2016-01-18 | 2016-05-25 | 佟立新 | Antioxidant 626 in shape of bead-shaped particles and preparation method and application thereof |
| CN106422967A (en) * | 2016-11-16 | 2017-02-22 | 陈业忠 | Manufacturing equipment of dispersible beaded cosmetic raw material |
| CN109225061A (en) * | 2018-11-08 | 2019-01-18 | 常州市星云润滑材料有限公司 | Powdered lubricant ultimogeniture producing line and lubrication powder preparation method |
| CN109475832A (en) * | 2016-06-15 | 2019-03-15 | 科莱恩国际有限公司 | Method for producing granular material |
| CN113694546A (en) * | 2021-08-30 | 2021-11-26 | 东方红集团(湖北)粮食机械股份有限公司 | Palm stearin powder spraying system and technological method thereof |
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2014
- 2014-09-02 CN CN201420500090.6U patent/CN204051602U/en active Active
Cited By (18)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105601999B (en) * | 2016-01-18 | 2018-11-06 | 佟立新 | There are bead shaped particle shape antioxidant 168 and its preparation method and the application of environmental benefit |
| CN105542224A (en) * | 2016-01-18 | 2016-05-04 | 佟立新 | Bead-shaped granular antioxidant 1076 as well as preparation method and application thereof |
| CN105601997B (en) * | 2016-01-18 | 2018-11-06 | 佟立新 | There are bead shaped particle shape antioxidant 626 and its preparation method and the application of environmental benefit |
| CN105504348B (en) * | 2016-01-18 | 2018-11-06 | 佟立新 | There are environmental benefit bead shaped particle shape antioxidant 1010 and its preparation method and application |
| CN105601998A (en) * | 2016-01-18 | 2016-05-25 | 佟立新 | Antioxidant in shape of bead-shaped particles and preparation method and application thereof |
| CN105601997A (en) * | 2016-01-18 | 2016-05-25 | 佟立新 | Antioxidant 626 in shape of bead-shaped particles and preparation method and application thereof |
| CN105482156A (en) * | 2016-01-18 | 2016-04-13 | 佟立新 | Bead-shaped granular composite plastic additive, preparation method and application thereof |
| CN105601998B (en) * | 2016-01-18 | 2018-11-06 | 佟立新 | There are antioxidant and its preparation method and the application of the bead shaped particle shape of environmental benefit |
| CN105542224B (en) * | 2016-01-18 | 2018-11-06 | 佟立新 | There are environmental benefit bead shaped particle shape antioxidant 1076 and its preparation method and application |
| CN105504348A (en) * | 2016-01-18 | 2016-04-20 | 佟立新 | Bead-shaped granular antioxidant 1010 as well as preparation method and application thereof |
| CN105601999A (en) * | 2016-01-18 | 2016-05-25 | 佟立新 | Antioxidant 168 in shape of bead-shaped particles and preparation method and application thereof |
| CN105482156B (en) * | 2016-01-18 | 2018-11-06 | 佟立新 | There are bead shaped particle shape composite plastic additive and its preparation method and the application of environmental benefit |
| CN109475832A (en) * | 2016-06-15 | 2019-03-15 | 科莱恩国际有限公司 | Method for producing granular material |
| CN109475832B (en) * | 2016-06-15 | 2022-07-22 | 科莱恩国际有限公司 | Method for producing granular material |
| CN106422967B (en) * | 2016-11-16 | 2024-04-16 | 陈业忠 | Easily-dispersed beaded cosmetic raw material manufacturing equipment |
| CN106422967A (en) * | 2016-11-16 | 2017-02-22 | 陈业忠 | Manufacturing equipment of dispersible beaded cosmetic raw material |
| CN109225061A (en) * | 2018-11-08 | 2019-01-18 | 常州市星云润滑材料有限公司 | Powdered lubricant ultimogeniture producing line and lubrication powder preparation method |
| CN113694546A (en) * | 2021-08-30 | 2021-11-26 | 东方红集团(湖北)粮食机械股份有限公司 | Palm stearin powder spraying system and technological method thereof |
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