CN201603544U - Triglycidyl isocyanurate fusion and granulation device - Google Patents
Triglycidyl isocyanurate fusion and granulation device Download PDFInfo
- Publication number
- CN201603544U CN201603544U CN2010201113926U CN201020111392U CN201603544U CN 201603544 U CN201603544 U CN 201603544U CN 2010201113926 U CN2010201113926 U CN 2010201113926U CN 201020111392 U CN201020111392 U CN 201020111392U CN 201603544 U CN201603544 U CN 201603544U
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- CN
- China
- Prior art keywords
- organic solvent
- pulverizer
- therewith
- belt
- triglycidyl isocyanurate
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- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
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Abstract
The utility model relates to the technical field of riglycidyl isocyanurate granulation, in particular to a triglycidyl isocyanurate fusion and granulation device. The device consists of a distillation kettle, an organic solvent condenser, an organic solvent recycling can, a vacuum pump, a belt-type cooling conveyor, a pulverizer, a sieving machine, a packing machine, a steam pipeline and a cooling water pipeline, wherein the distillation kettle is provided with a stirring machine, the organic solvent condenser is connected with the distillation kettle through a gaseous organic solvent conveying pipeline, the organic solvent recycling can is connected with the organic solvent condenser, the vacuum pump is connected with the organic solvent recycling can, the belt-type cooling conveyor is arranged below the distillation kettle, the pulverizer is connected with the belt-type cooling conveyor, the sieving machine and the packing machine are connected with the pulverizer, and the steam pipeline and the cooling water pipeline are connected with an interlayer of the distillation kettle. The device has the advantages of recycling all organic solvents, improving operation environment, reducing production cost, having stable and safe technology and high product yield, shrinking the storage and transportation spaces due to high product density and lowering storage and transportation cost.
Description
Technical field
The utility model belongs to triglycidyl isocyanurate granulating technique field, particularly a kind of triglycidyl isocyanurate melting prilling granulator.
Background technology
Triglycidyl isocyanurate (TGIC) particle of producing all is the prilling granulator that adopts extruding granulator at present, and its technical process is: the triglycidyl isocyanurate that will contain organic solvent is through comminutor extruding pelletization, oven dry, packing.The material that contains the triglycidyl isocyanurate of organic solvent has a large amount of organic solvents (account for weight of material 30%) to evaporate in the air in drying course, not only contaminated environment, harm operating personnel physical and mental health, waste a large amount of organic solvents simultaneously, increased production cost.Because the product of extruding pelletization device is dried behind granulating and forming, 30% the organic solvent that accounts for weight of material in drying course volatilize away, but particle volume remains unchanged, so also has aspects such as packing, storage, the transportation big shortcoming that takes up room.
Summary of the invention
The purpose of this utility model is the deficiency that exists at above-mentioned extruding pelletization device, and a kind of production efficiency height is provided, reliable product quality, environmental protection, the triglycidyl isocyanurate melting prilling granulator that energy consumption is low.What the utility model was different with extruding pelletization is with all organic solvents of triglycidyl isocyanurate, all to reclaim.
The purpose of this utility model part by the following technical programs realizes.
Triglycidyl isocyanurate melting prilling granulator of the present utility model, it is characterized in that by the distillation still that has mixer, by the gaseous state organic solvent conveyance conduit organic solvent condenser that is connected of the distillation outlet of distillation still therewith, by the liquid organic solvent conveyance conduit organic solvent recycling can that is connected of organic solvent condenser therewith, by the vacuum lead vavuum pump that is connected of organic solvent recycling can therewith, be arranged on the belt coolconveyer of this distillation still below, the consecutive pulverizer of belt coolconveyer therewith, consecutive screening machine of pulverizer and packing machine therewith, the jet chimney that is connected by the interlayer of distillation still therewith, cooling water pipeline is formed.
Described belt coolconveyer is by the conveying band of circular flow, the conveyer belt driving wheel mechanism that carries band to be connected therewith, and the equipment water jetting cooler that is located in the conveying band of this circular flow is formed.
Be provided with control valve in described jet chimney, the cooling water pipeline.
Described pulverizer is for regulating the pulverizer of rotating speed, and the range of speeds of this pulverizer is 30～100 rev/mins.
The mesh size of described screening machine is 3～6mm.
The utility model was compared with former extruding pelletization device, had the following advantages:
1, reclaims whole organic solvents, improved the production process operating environment, and solved environmental issue.
2, the organic solvent of Hui Shouing can utilize again, has reduced production cost.
3, stable processing technique, safety, product yield height, the every index excellent performance of product.
5, because of its product density is big, dwindle storage and transportation space, reduced storage and cost of transportation.
Description of drawings
Fig. 1 is a structured flowchart of the present utility model.
The specific embodiment
Below in conjunction with the description of drawings specific embodiment of the present utility model.
As shown in Figure 1, triglycidyl isocyanurate melting prilling granulator of the present utility model, it is characterized in that by the distillation still 4 that has mixer, by the gaseous state organic solvent conveyance conduit organic solvent condenser 3 that is connected of the distillation outlet of distillation still 4 therewith, by the pipeline organic solvent recycling can 2 that is connected of organic solvent condenser 3 therewith, by the vacuum lead vavuum pump 1 that is connected of organic solvent recycling can 2 therewith, be arranged on the belt coolconveyer 5 of these distillation still 4 belows, belt coolconveyer 5 consecutive pulverizers 6 therewith, consecutive screening machine of pulverizer and packing machine 7 therewith, the jet chimney that is connected by the interlayer of distillation still therewith, cooling water pipeline is formed.
Described belt coolconveyer 5 is by the conveying band 5-1 of circular flow, and the conveyer belt driving wheel 5-2 of mechanism that carries band 5-1 to be connected therewith is located at this and carries the equipment water jetting cooler 5-3 in the band to form.
Be provided with control valve in described jet chimney, the cooling water pipeline.
Described pulverizer is for regulating the pulverizer of rotating speed, and the range of speeds of this pulverizer is 30～100 rev/mins.
The mesh size of described screening machine is 3～6mm.
The utlity model has following advantage: reclaimed whole organic solvents, improved the production process operating environment, and solved environmental issue. The organic solvent that reclaims can recycle, and has reduced production cost. Stable processing technique, safety, product yield height, product indices excellent performance. Because its product density is big, dwindled the space that stores and transport, reduced storage and cost of transportation.
Claims (5)
1. triglycidyl isocyanurate melting prilling granulator, it is characterized in that by the distillation still that has mixer, by the gaseous state organic solvent conveyance conduit organic solvent condenser that is connected of the distillation outlet of distillation still therewith, by the liquid organic solvent conveyance conduit organic solvent recycling can that is connected of organic solvent condenser therewith, by the vacuum lead vavuum pump that is connected of organic solvent recycling can therewith, be arranged on the belt coolconveyer of this distillation still below, the consecutive pulverizer of belt coolconveyer therewith, consecutive screening machine of pulverizer and packing machine therewith, the jet chimney that is connected by the interlayer of distillation still therewith, cooling water pipeline is formed.
2. triglycidyl isocyanurate melting prilling granulator according to claim 1, it is characterized in that the conveying band of described belt coolconveyer by circular flow, the conveyer belt driving wheel mechanism that carries band to be connected therewith, the interior equipment water jetting cooler of conveying band that is located at this circular flow is formed.
3. triglycidyl isocyanurate melting prilling granulator according to claim 1 is characterized in that being provided with control valve in described jet chimney, the cooling water pipeline.
4. production line according to claim 1 is characterized in that described pulverizer for regulating the pulverizer of rotating speed, and the range of speeds of this pulverizer is 30～100 rev/mins.
5. triglycidyl isocyanurate melting prilling granulator according to claim 1, the mesh size that it is characterized in that described screening machine is 3～6mm.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010201113926U CN201603544U (en) | 2010-02-04 | 2010-02-04 | Triglycidyl isocyanurate fusion and granulation device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010201113926U CN201603544U (en) | 2010-02-04 | 2010-02-04 | Triglycidyl isocyanurate fusion and granulation device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201603544U true CN201603544U (en) | 2010-10-13 |
Family
ID=42948254
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2010201113926U Expired - Lifetime CN201603544U (en) | 2010-02-04 | 2010-02-04 | Triglycidyl isocyanurate fusion and granulation device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201603544U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101773806B (en) * | 2010-02-04 | 2012-01-18 | 鞍山润德精细化工有限公司 | Triglycidyl isocyanurate melting granulating technology and production line thereof |
| CN106632473A (en) * | 2016-10-27 | 2017-05-10 | 湖北沙隆达股份有限公司 | Continuous crystallization device of trichlorphon raw medicine and method thereof |
-
2010
- 2010-02-04 CN CN2010201113926U patent/CN201603544U/en not_active Expired - Lifetime
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101773806B (en) * | 2010-02-04 | 2012-01-18 | 鞍山润德精细化工有限公司 | Triglycidyl isocyanurate melting granulating technology and production line thereof |
| CN106632473A (en) * | 2016-10-27 | 2017-05-10 | 湖北沙隆达股份有限公司 | Continuous crystallization device of trichlorphon raw medicine and method thereof |
| CN106632473B (en) * | 2016-10-27 | 2019-04-19 | 湖北沙隆达股份有限公司 | The continuous crystallisation devices and methods therefor of trichlorfon technical |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| AV01 | Patent right actively abandoned |
Granted publication date: 20101013 Effective date of abandoning: 20120118 |