CN103240047A - Fluorescent material polymerization reaction electromagnetism heating system - Google Patents
Fluorescent material polymerization reaction electromagnetism heating system Download PDFInfo
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- CN103240047A CN103240047A CN2013101650089A CN201310165008A CN103240047A CN 103240047 A CN103240047 A CN 103240047A CN 2013101650089 A CN2013101650089 A CN 2013101650089A CN 201310165008 A CN201310165008 A CN 201310165008A CN 103240047 A CN103240047 A CN 103240047A
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- reactor
- fluorescent material
- heating system
- hydraulic lifting
- reaction kettle
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Abstract
The invention provides a fluorescent material polymerization reaction electromagnetism heating system. The system comprises a stirrer, a reaction kettle, an electromagnetism heating device, a pressure-reducing station and a hydraulic lifting system, wherein the stirrer is arranged above the reaction kettle, an exhaust pipe is arranged on the stirrer, the downward side of the exhaust pipe is in butt joint with the reaction kettle, the hydraulic lifting system is connected with the reaction kettle by a bearing, the pressure-reducing station is connected with the hydraulic lifting system by a shaft, and the electromagnetism heating device is placed on the outer surface of at the two-thirds part of the reaction kettle from bottom to top. The system provided by the invention has the advantages that the electromagnetism is adopted for heating, the heating speed is fast, after heating stops, the temperature can not rush upwards, the thermal insulation effect is good, the safety performance is high, and the system has few influences on the environment.
Description
Technical field
The novel polymerizing reactor field that relates to the chemical industry reactor of the present invention, especially a kind of fluorescent material polymerisation electromagnetic heating system.
Background technology
At present, use organic heat carrier furnace to be heating agent with conduction oil, enter reacting kettle jacketing by circulating pump, the material in the reactor is heated polymerization reaction take place.Reaction moves to mixing position with reactor and fixes before beginning, and connects conduction oil and connects flexible pipe and locking soon, and the heating of opening conduits valve will be stirred the beginning stirring reaction that descends behind the input raw material; After reaction finishes, lifting is stirred, close the conduction oil valve, open snap joint the conduction oil flexible pipe is broken away from from reactor, untie the reactor fixture, reactor is moved between batch turning, sling with an electric block, another electric block hooks reactor bottom suspension ring to be sling, and with the reactor tip tilt, material in reactor is poured out.The shortcoming of present technology: because material properties relation (the material viscosity is very high) can't can only be led to the mode discharging of toppling over from reactor bottom blowing, often occur aspects influences such as safety, environment in process of production; Because removing reactor will disconnect thermal conductive oil pipeline, the usually oil temperature has the part conduction oil and overflows at 250 ℃ when throwing off connection, and the personnel that cause easily scald; Valve is more on the pipeline, causes maloperation easily, produces accident potential; Shifting out reactor between batch turning the time, have large quantity of exhaust gas in the unlimited reactor and distribute in inside, workshop, cause environmental pollution; Use the electric block batch turning, reactor rocks when batch turning, and the influence operation has a small amount of conduction oil and is dropped in easily in the material after the upset, influence materials quality; When the mobile response still, because reactor adds that the weight of material is very heavy, the mobile response still is gruelling, damages ground again easily, causes the ground uneven; Owing to when the turnover reactor, want the lifting mixer, make that the discharge duct on stirring can not be fixed, cause exhaust problem, the waste gas that produces in the course of reaction remains in the material, influences materials quality.
Summary of the invention
The objective of the invention is to overcome the defective of prior art, a kind of fluorescent material polymerisation electromagnetic heating system is provided.
The present invention is achieved by the following technical solutions: a kind of fluorescent material polymerisation electromagnetic heating system, comprise, operating platform, mixer, reactor, electromagnetic heater, pressure-reducing station and hydraulic lifting system, mixer is arranged on the top of reactor, blast pipe is arranged on the mixer, blast pipe below butt joint reactor, hydraulic lifting system is connected with bearing with reactor, and pressure-reducing station is connected with the hydraulic lifting system axle.
Further, opening one at operating platform can be for reactor hole up and down.
Further, mixer is connected with snap close with the joint portion of reactor.
Further, electromagnetic heater places the reactor outer surface at 2/3rds places from the bottom up.
Described electromagnetic heater is electromagnetic heater.
The present invention has following good effect: adopt the electromagnetism heating, heating is that speed is fast, and stopping temperature after heating can be toward upper punch, high insulating effect, the security performance height is little to ambient influnence; Mixer is without lifting, and exhaust outlet can fixedly mount, and exhaust performance is good to have very big lifting to product quality and ambient influnence; The reactor back batch turning automatically that descends realizes the batch turning automation, avoids dismantling the potential safety hazard that oil pipe brings originally, the ambient influnence of avoiding reactor to move causing and ground damaged.Raise labour efficiency greatly and processing safety; Improve 8 of special equipments such as the inactive boiler in back and electric block, reduction equipment, operation and special equipment inspection cost have improved the production safety coefficient.
Description of drawings
Fig. 1 is structural representation of the present invention.
Fig. 2 is process flow diagram of the present invention.
In the drawings, 1-mixer, 2-reactor, 3-Hydraulic Station, 4-hydraulic lifting system, 5-electromagnetic heater.
The specific embodiment
The invention will be further described below in conjunction with embodiment.
Embodiment
Referring to Fig. 1, a kind of fluorescent material polymerisation of the present invention electromagnetic heating system, comprise: mixer 1, reactor 2, Hydraulic Station 3, hydraulic lifting system 4 and electromagnetic heater 5, to stir, 1 is installed on 2.5 meters operating platforms, and flat reaction still 2 positions are opened one can be for reactor hole up and down.Reactor 2 adopts the electromagnetism mode of heating, and electromagnetic heater 5 places the reactor outer surface at 2/3rds places from the bottom up, installs on the liftable hydraulic platform, docks back locking with mixer by the hydraulic pressure rising during use and is used for reaction mass.After reaction finishes, open fixedly snap close, reactor dropped under the platform, start the batch turning hydraulic means, with the reactor top to mouthful downward-sloping, with material to going out.
Referring to Fig. 2, technological process of the present invention is: before the reaction beginning, the cleaning reactor rotates reactor to plumbness, and the primer fluid pressing system rises to reactor and is fit to the position that feeds intake on the platform.Drop into raw material, the reactor rising is being combined with mixer and locking.Start electromagnetic heating system, start to be stirred to react and finish.Stop the electromagnetism heating, stop to stir.Start the reactor hydraulic system reactor is dropped to minimum state under the platform.Starting the reactor rotation reverses reactor to material and can flow out the position automatically.After the material evacuation, the cleaning reactor rotates reactor to plumbness, the next circulation of beginning.
Claims (5)
1. fluorescent material polymerisation electromagnetic heating system, comprise, operating platform, mixer, reactor, electromagnetic heater, pressure-reducing station and hydraulic lifting system, it is characterized in that: mixer is arranged on the top of reactor, blast pipe is arranged on the mixer, blast pipe below butt joint reactor, hydraulic lifting system is connected with bearing with reactor, and pressure-reducing station is connected with the hydraulic lifting system axle.
2. fluorescent material polymerisation electromagnetic heating system as claimed in claim 1 is characterized in that: open one at operating platform and can supply reactor hole up and down.
3. fluorescent material polymerisation electromagnetic heating system as claimed in claim 1, it is characterized in that: mixer is connected with snap close with the joint portion of reactor.
4. fluorescent material polymerisation electromagnetic heating system as claimed in claim 1, it is characterized in that: electromagnetic heater places the reactor outer surface at 2/3rds places from the bottom up.
5. fluorescent material polymerisation electromagnetic heating system as claimed in claim 4, it is characterized in that: described electromagnetic heater is electromagnetic heater.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2013101650089A CN103240047A (en) | 2013-05-08 | 2013-05-08 | Fluorescent material polymerization reaction electromagnetism heating system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2013101650089A CN103240047A (en) | 2013-05-08 | 2013-05-08 | Fluorescent material polymerization reaction electromagnetism heating system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN103240047A true CN103240047A (en) | 2013-08-14 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2013101650089A Pending CN103240047A (en) | 2013-05-08 | 2013-05-08 | Fluorescent material polymerization reaction electromagnetism heating system |
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Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US6048459A (en) * | 1999-04-09 | 2000-04-11 | Mockba Corporation | Method and apparatus for fluidization of particulate bed materials |
| CN101041488A (en) * | 2006-03-20 | 2007-09-26 | 北京国力源高分子科技研发中心 | Method for producing green fuel by free radical treatment paper liquor waste slag and electrical catalytic reaction device |
| CN102527446A (en) * | 2012-02-14 | 2012-07-04 | 迈瑞尔实验设备（上海）有限公司 | Hydrothermal ageing device for multi-sample parallel catalyst |
| CN102553510A (en) * | 2010-12-23 | 2012-07-11 | 四川国和新材料有限公司 | Glass reactor device |
-
2013
- 2013-05-08 CN CN2013101650089A patent/CN103240047A/en active Pending
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US6048459A (en) * | 1999-04-09 | 2000-04-11 | Mockba Corporation | Method and apparatus for fluidization of particulate bed materials |
| CN101041488A (en) * | 2006-03-20 | 2007-09-26 | 北京国力源高分子科技研发中心 | Method for producing green fuel by free radical treatment paper liquor waste slag and electrical catalytic reaction device |
| CN102553510A (en) * | 2010-12-23 | 2012-07-11 | 四川国和新材料有限公司 | Glass reactor device |
| CN102527446A (en) * | 2012-02-14 | 2012-07-04 | 迈瑞尔实验设备（上海）有限公司 | Hydrothermal ageing device for multi-sample parallel catalyst |
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Application publication date: 20130814 |