CN202376987U - High efficiency reactor - Google Patents
High efficiency reactor Download PDFInfo
- Publication number
- CN202376987U CN202376987U CN2011205495375U CN201120549537U CN202376987U CN 202376987 U CN202376987 U CN 202376987U CN 2011205495375 U CN2011205495375 U CN 2011205495375U CN 201120549537 U CN201120549537 U CN 201120549537U CN 202376987 U CN202376987 U CN 202376987U
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- static mixer
- reactor
- high efficiency
- efficiency reactor
- kettle type
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Abstract
The utility model discloses a reactor, in particular to a high efficiency reactor used for chemical engineering production. The high efficiency reactor comprises a kettle type reactor and a static mixer, wherein the kettle type reactor and the static mixer are connected through a branch pipe at the lower portion, a circulating pump is arranged on the branch pipe at the position of an inlet of the static mixer, the branch pipe is connected with the kettle type reactor and the static mixer respectively at the lower portions of the kettle type reactor and the static mixer. A temperature control meter and a temperature displayer are connected onto the static mixer, a even distributor is installed at the bottom of the static mixer, and the static mixer is provided with a condensing system which is arranged in a countercurrent mode. The high efficiency reactor has the advantages of enabling media to be sufficiently dispersed and mixed, quickening reaction speed, shortening reaction time, improving yield and saving energy. The high efficiency reactor can be widely applied to chemical engineering enterprises and the like.
Description
Technical field
This practicality relates to a kind of reactor, specifically is meant a kind of high efficiency reactor that is used for Chemical Manufacture.
Technical background
Along with global environmental consciousness strengthens; Production to chemical enterprise has proposed higher hygienic requirements; Countries in the world numerous and confused developmental research environment-friendly type production equipment; The tank reactor of using in the Chemical Manufacture has multiple whipped form such as paddle agitator, anchor agitator, gate stirrer, spiral chip agitator etc., and stirring technique can provide higher shearing and tensile stress, makes the reaction medium distribution uniform; Reaction speed is very fast, and the tank reactor that therefore has agitating device is used very extensive in Chemical Manufacture.But because its field of flow of setting up nearly all is a laminar-type, the medium specific gravity difference of participating in reaction is bigger, makes can not fully contact between the reactant; It is even inadequately to distribute mutually, causes reaction thorough inadequately, and the reaction time is longer; Consume more manpower and materials, waste energy.
Because plastic processing both domestic and external industry is high speed development all, thereby chemical industry has good market prospects, and this makes in recent years becomes focus to the new application of chemical products and the research of new oxidation technology.Improve the service efficiency of chemical industry equipment, all cost enterprise, research unit are given priority to direction with utilization rate that energy consumption is provided etc.
The utility model content
The utility model proposes a kind of reactor more efficiently to deficiency of the prior art, is used for the production of chemical enterprise.
The utility model is achieved through following technical proposals:
A kind of high efficiency reactor; It is characterized in that comprising tank reactor and static mixer; Wherein, Tank reactor is connected with the arm of static mixer through the below, and a circulating pump is arranged on the arm of static mixer import department, arm and tank reactor, static mixer be connected respectively bottom at tank reactor, static mixer; Be connected with temperature controller and temperature indicator on the static mixer.
As preferably, an even distributor is installed in the static mixer bottom in above-mentioned a kind of high efficiency reactor.Described even distributor is that footpath with holes is the distributor of 0.5mm-2.5mm aperture, sieve aperture, sintering hole or pore.
As preferably, the static mixer inside in above-mentioned a kind of high efficiency reactor is some tubulations, is filled by filler in the tubulation.
As preferably, the static mixer in above-mentioned a kind of high efficiency reactor is furnished with condenser system, and condenser system becomes the adverse current setting with static mixer.
In above-mentioned reactor, mixture tentatively is dispersed into the reaction stream with certain decentralization after through even distributor, enters into the static mixer that is connected even distributor top afterwards.Arrange tubulation in the middle of the blender; Fill the rotary unit that gets up by the mutual cross lamination of flight in the tubulation; In order to change the main flow direction of fluid; Fluid flows into and wherein to obtain guiding, when the fluid of high flow velocities flows simultaneously from the wall region direction to the equiulbrium flow in cross-section center zone, realize that thus mixture fluid fully mixes.Because acutely friction between the fluid, molecular motion is fierce, thereby produces higher heat; Heat is absorbed by reactant mixture; The heat that offers reaction system when having saved reaction is supplied with, and carries out for the heat that prevents to produce influences successful reaction too greatly, above static Hi-mixer, thermometer is housed; At any time understand the variations in temperature in the blender, temperature is by the automatic temperature control instrument control on next door.Static Hi-mixer is furnished with condenser system simultaneously, can prevent that too high temperature appears in locking system.
Because the hole diameter on the even distributor in this kind static mixer is very little, the material requirement that therefore gets into static mixer does not have solid particle, and perhaps solid particle will fully be dissolved in the liquid, in order to avoid stop up the aperture.
Beneficial effect: the utility model provides a kind of high efficiency reactor, in reactor, can make the abundant dispersing and mixing of medium, and fast reaction speed has shortened the reaction time, has improved output, saves the energy.
Description of drawings
The structural representation of Fig. 1 the utility model
1, even distributor 2, condensed water import 3, control valve 4, static mixer 5, temperature controller
6, temperature indicator 7, condensation-water drain 8, tank reactor 9, circulating pump
The specific embodiment
Below in conjunction with accompanying drawing, the enforcement of the utility model is specified:
According to structure shown in Figure 1; Prepare a high efficiency reactor; Comprising comprising tank reactor 8 and static mixer 4; Tank reactor 8 is connected with the arm of static mixer 4 through the below, and a circulating pump 9 is arranged on the arm of static mixer 4 import departments, arm and tank reactor 8, static mixer 4 be connected respectively bottom at tank reactor 8, static mixer 4; Be connected with temperature controller 5 and temperature indicator 6 on the static mixer 4; An even distributor 1 is installed in static mixer 4 bottoms; Evenly distributor 1 is the distributor of 0.5mm-2.5mm aperture, sieve aperture, sintering hole or pore for footpath with holes, and present embodiment adopts the distributor of 2.0mm sieve aperture; Static mixer 4 inside are some tubulations, are filled by filler in the tubulation; In addition, static mixer 4 is furnished with condenser system, 4 one-tenth adverse current settings of condenser system and static mixer.
In the utility model, after fluid gets into tank reactor 8, flow into static mixer 4 through following arm again; Behind even distributor 1, fluid can more evenly enter into static mixer 4, and because the motive force of circulating pump 9; Fluid-flow rate is fast, and the mutual collision between the reactant molecule has been accelerated in the mixing on the microsize between whereby can the realization response thing; Collision between while reaction medium and the container, friction aggravation make the temperature of reaction medium change, if reaction is the heat release type; Then reaction can offer the reaction system heat automatically, and does not need extraly to reaction system heating, and temperature is elevated to when surpassing the suitable temperature of reaction; To suitable scope, the temperature indicator 6 through peripheral hardware can reflect through automatic temperature-adjusting controller 5 adjustment temperature.For effective control of realizing temperature and effective control of reaction, can open control valve 3, start the condensed water import 2 input condensed waters of condenser system, through having carried out after the heat exchange, flow out by condensation-water drain 7 again with static mixer 4.
Through the use of the utility model in actual enterprise, the reaction time that can make reaction medium pass through this high efficiency reactor shortens greatly, shortens to about 3 hours by original 9-10 hour, has realized high production, and huge economic benefit is arranged.
Claims (5)
1. high efficiency reactor; It is characterized in that comprising tank reactor (8) and static mixer (4); Wherein, Tank reactor (8) is connected with the arm of blender (4) through the below, and a circulating pump (9) is arranged on the arm of blender (4) import department, arm and tank reactor (8), static mixer (5) be connected respectively bottom at tank reactor (8), static mixer (4); Be connected with temperature controller (5) and temperature indicator (6) on the static mixer (4).
2. a kind of high efficiency reactor according to claim 1 is characterized in that described static mixer (a 4) bottom installation even distributor (1).
3. a kind of high efficiency reactor according to claim 2 is characterized in that described even distributor (1) is the distributor of 0.5mm-2.5mm aperture, sieve aperture, sintering hole or pore for footpath with holes.
4. a kind of high efficiency reactor according to claim 1 is characterized in that described static mixer (4) inside is some tubulations, is filled by filler in the tubulation.
5. a kind of high efficiency reactor according to claim 1 is characterized in that described static mixer (4) is furnished with condenser system, and condenser system becomes the adverse current setting with static mixer (4).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011205495375U CN202376987U (en) | 2011-12-25 | 2011-12-25 | High efficiency reactor |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011205495375U CN202376987U (en) | 2011-12-25 | 2011-12-25 | High efficiency reactor |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN202376987U true CN202376987U (en) | 2012-08-15 |
Family
ID=46625509
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2011205495375U Expired - Fee Related CN202376987U (en) | 2011-12-25 | 2011-12-25 | High efficiency reactor |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN202376987U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112452282A (en) * | 2020-12-22 | 2021-03-09 | 武汉伯业科技发展有限公司 | Synthesis device of 2-amino-5-mercapto-1, 3, 4-thiadiazole and use method thereof |
-
2011
- 2011-12-25 CN CN2011205495375U patent/CN202376987U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112452282A (en) * | 2020-12-22 | 2021-03-09 | 武汉伯业科技发展有限公司 | Synthesis device of 2-amino-5-mercapto-1, 3, 4-thiadiazole and use method thereof |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C17 | Cessation of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20120815 Termination date: 20121225 |