CN205517780U - Spiral reaction unit - Google Patents
Spiral reaction unit Download PDFInfo
- Publication number
- CN205517780U CN205517780U CN201520913021.2U CN201520913021U CN205517780U CN 205517780 U CN205517780 U CN 205517780U CN 201520913021 U CN201520913021 U CN 201520913021U CN 205517780 U CN205517780 U CN 205517780U
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- China
- Prior art keywords
- oxygen
- reaction unit
- liquid
- reactor body
- spiral reaction
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Abstract
The utility model discloses a spiral reaction unit, including the reation kettle body, this internal spiral pipe of installing of reation kettle, the cross section of spiral pipe is divided into the triplex by the baffle, is condenser pipe, oxygen hose and liquid feeding pipe respectively, is provided with out the oxygen hole on the lateral wall of oxygen hose, is provided with out the liquid hole on the lateral wall of liquid feeding pipe, all is provided with two -layer baffle between condenser pipe, oxygen hose and the liquid feeding pipe, and all is provided with the vacuum space between the two -layer baffle, the utility model discloses in putting into the reation kettle body with the spiral pipe to divide into 3 parts with the spiral pipe, reation kettle is put into from the introduction port to the raw materials, inserts oxygen hose and liquid feeding pipe respectively with oxygen and solvent as required, and oxygen and solvent get into reation kettle from going out the oxygen hole and going out the liquid hole, the spiral pipe has increased the contact surface of oxygen and solvent and raw materials effectively, all be provided with the vacuum space between the two -layer baffle between condenser pipe, oxygen hose and the liquid feeding pipe, avoided influencing mutually the problem of temperature effectively between oxygen, solvent and the comdenstion water.
Description
Technical field
This utility model belongs to chemical reaction equipment technical field, particularly to the spiral reaction unit of one.
Background technology
The broad understanding of reactor i.e. has the container physically or chemically reacted, by the structure of container is designed and parameter configuration, realize the heating of technological requirement, evaporate, cool down and the mixture function of low high speed, be provided with in it and react the stirring paddle carried out for stirring, accelerate.Reaction solution and solid reactant, under the effect of stirring slurry, mix in reactor, react.During reaction, if adding oxygen or air, then can strengthen the carrying out of reaction, thus shorten the time of reaction, improve production efficiency.At present, the method increasing air has varied, but mostly there is various problem, if any reactor teeter column changed into ajutage to carry air for reactor, during reaction, reactant corrosive power is the strongest, the teeter column being provided with multiple spray-hole is easily corroded and bad replacing, adds cost, brings problem.
Industrial chemicals during processing, need first by granular solid material after crusher for crushing, be then transferred in blender, add solvent and carry out hybrid reaction, complex procedures, and process equipment is many, and cost is high.It addition, existing during stirring, lid is provided in the top of housing, not only makes heat distribute soon, and liquid can move up along with stirring, cause stirring efficiency low.
Utility model content
Utility model purpose: this utility model provides a kind of spiral reaction unit, to solve the problems of the prior art.
Technical scheme: to achieve these goals, this utility model by the following technical solutions:
A kind of spiral reaction unit, including reactor body, described reactor is the most internal is provided with serpentine pipe, the cross section of described serpentine pipe is divided into three parts by dividing plate, it is respectively condensing tube, oxygen hose and liquid-feeding tube, the lateral wall of described oxygen hose is provided with several oxygen outlet, the lateral wall of described liquid-feeding tube is provided with several liquid outlets, dividing plate between described condensing tube, oxygen hose and liquid-feeding tube is between two-layer, and two-layer dividing plate and is provided with vacuum voids.
Further, condensing tube, oxygen hose and the liquid-feeding tube at described serpentine pipe top all stretches out reactor body, and oxygen hose top is provided with oxygen feeder, and liquid-feeding tube top is provided with filling opening.
Further, the bottom of described serpentine pipe only condensing tube stretches out reactor body, forms loop by condensation cycle pump, and described condensation cycle pump connects motor.
Further, described oxygen feeder is also circumscribed with blower fan.
Further, described reactor is the most internal is also equipped with thermometer.
Further, described thermometer externally connected with display screen, described display screen is installed on the lateral wall of outer barrel.
Further, described reactor bodies top is provided with air vent；Cover plate is installed on described air vent, between described air vent and cover plate, is provided with rubber blanket.
Further, described reactor bodies top is additionally provided with injection port, injection port is provided with sample introduction cover plate, is provided with rubber blanket between described injection port and sample introduction cover plate.
Further, described reactor body is made up of inner barrel and outer barrel, is provided with vacuum voids between inner barrel and outer barrel.
Further, the medial wall of described interior bucket is additionally provided with anticorrosive coat.
Beneficial effect: serpentine pipe is inserted in reactor body by this utility model, and serpentine pipe is divided into 3 parts, raw material puts into reactor from injection port, further according to needs, oxygen and solvent are respectively connected to oxygen hose and liquid-feeding tube, oxygen and solvent enter reactor from oxygen outlet and liquid outlet, it is also possible to regulation oxygen and the consumption of solvent as required；Serpentine pipe is effectively increased the contact area of oxygen and solvent and raw material；Reactor interior reaction temperature is monitored according to the display screen on outer barrel outer wall, according to reaction temperature, the flow velocity of condensed water in regulation condensing tube.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model；
Fig. 2 is the structural representation of serpentine pipe in this utility model；
Fig. 3 is the structural representation of this utility model cover plate and rubber blanket；
Fig. 4 is sample introduction cover plate and the structural representation of rubber blanket in this utility model；
Wherein: 1-condensation cycle pump, 2-serpentine pipe, 3-condensing tube, 4-oxygen hose, 5-liquid-feeding tube, 6-outer barrel, bucket in 7-, 8-thermometer, 9-filling opening, 10-blower fan, 11-liquid outlet, 12-oxygen outlet, 13-motor, 14-display, 15-anticorrosive coat, 16-air vent, 17-cover plate, 18-reactor body, 19-rubber blanket, 20-oxygen feeder, 21-injection port, 22-sample introduction cover plate, 23-dividing plate.
Detailed description of the invention
Below in conjunction with embodiment, this utility model is further described.
As shown in the figure, a kind of spiral reaction unit, including reactor body 18, in described reactor body 18, serpentine pipe 2 is installed, the cross section of described serpentine pipe 2 is divided into three parts by dividing plate 23, it is respectively condensing tube 3, oxygen hose 4 and liquid-feeding tube 5, several oxygen outlet 12 it are provided with on the lateral wall of described oxygen hose 4, several liquid outlets 11 it are provided with on the lateral wall of described liquid-feeding tube 5, dividing plate 23 between described condensing tube 3, oxygen hose 4 and liquid-feeding tube 5 is between two-layer, and two-layer dividing plate 23 and is provided with vacuum voids.Serpentine pipe 2 is inserted in reactor body 18 by this utility model, and serpentine pipe 2 is divided into 3 parts, raw material puts into reactor from injection port 21, further according to needs, oxygen and solvent is respectively connected to oxygen hose 4 and liquid-feeding tube 5, oxygen and solvent enter reactor from oxygen outlet 12 and liquid outlet 11, it is also possible to regulation oxygen and the consumption of solvent as required；Serpentine pipe 2 is effectively increased the contact area of oxygen and solvent and raw material；Reactor interior reaction temperature is monitored according to the display screen 14 on outer barrel 6 outer wall, according to reaction temperature, the flow velocity of condensed water in regulation condensing tube 3.It is provided with two-layer dividing plate 23 between described condensing tube 3, oxygen hose 4 and liquid-feeding tube 5, and it is provided with vacuum voids between two-layer dividing plate 23, the problem that efficiently avoid the temperature that interacts between oxygen, solvent and condensed water, especially condensate temperature is relatively low, dividing plate 23 is used it to be separated with oxygen hose 4 and liquid-feeding tube 4, in order to avoid condensed water reduces oxygen or the temperature of solvent.
Condensing tube 3, oxygen hose 4 and the liquid-feeding tube 5 at described serpentine pipe 2 top all stretches out reactor body 18, and oxygen hose 4 top is provided with oxygen feeder 20, and liquid-feeding tube 5 top is provided with filling opening 9.
The bottom of described serpentine pipe 2 only condensing tube 3 stretches out reactor body 18, forms loop by condensation cycle pump 1, and described condensation cycle pump 1 connects motor 13.
Described oxygen feeder 20 is also circumscribed with blower fan 10, increases the inflow of oxygen.
Thermometer 8, the at any time temperature in monitoring reactor it is also equipped with in described reactor body 18.
Described thermometer 8 externally connected with display screen 14, described display screen 14 is installed on the lateral wall of outer barrel 6, according to the condensed water flow velocity in displays temperature regulation condensing tube 3.
Described reactor body 18 top is provided with air vent 16；Cover plate 17 is installed on described air vent 16, is provided with rubber blanket 19 between described air vent 16 and cover plate 17, works as generated reactive gas, cover plate 17 can be opened, allow gas discharge；When reaction is the reaction that need not oxygen, then close cover plate 17, oxygen hose 4 does not access oxygen.
Described reactor body 18 top is additionally provided with injection port 21, injection port 21 is provided with sample introduction cover plate 22, is provided with rubber blanket 19 between described injection port 21 and sample introduction cover plate 22, and raw material is directly placed into reactor from injection port 21.
Described reactor body 18 is made up of interior bucket 7 and outer barrel 6, is provided with vacuum voids between interior bucket 7 and outer barrel 6, and some reaction needs to react at a constant temperature, therefore vacuum voids is so that interior bucket 7 is incubated.
It is additionally provided with anticorrosive coat 15 on the medial wall of described interior bucket 6.
Below it is only preferred implementation of the present utility model; it is noted that, for those skilled in the art; on the premise of without departing from this utility model principle, it is also possible to make some improvements and modifications, these improvements and modifications also should be regarded as protection domain of the present utility model.
Claims (10)
1. a spiral reaction unit, including reactor body, it is characterized in that: in described reactor body (18), serpentine pipe (2) is installed, the cross section of described serpentine pipe (2) is divided into three parts by dividing plate (23), it is respectively condensing tube (3), oxygen hose (4) and liquid-feeding tube (5), several oxygen outlet (12) it are provided with on the lateral wall of described oxygen hose (4), several liquid outlets (11) it are provided with on the lateral wall of described liquid-feeding tube (5), described condensing tube (3), dividing plate (23) between oxygen hose (4) and liquid-feeding tube (5) is two-layer, and it is provided with vacuum voids between two-layer dividing plate (23).
Spiral reaction unit the most according to claim 1, it is characterized in that: the condensing tube (3) at described serpentine pipe (2) top, oxygen hose (4) and liquid-feeding tube (5) all stretch out reactor body (18), oxygen hose (4) top is provided with oxygen feeder (20), and liquid-feeding tube (5) top is provided with filling opening (9).
Spiral reaction unit the most according to claim 1, it is characterized in that: the bottom of described serpentine pipe (2) only has condensing tube (3) and stretches out reactor body (18), forming loop by condensation cycle pump (1), described condensation cycle pump (1) connects motor (13).
Spiral reaction unit the most according to claim 2, it is characterised in that: described oxygen feeder (20) is also circumscribed with blower fan (10).
Spiral reaction unit the most according to claim 1, it is characterised in that: it is also equipped with thermometer (8) in described reactor body (18).
Spiral reaction unit the most according to claim 5, it is characterised in that: described thermometer (8) externally connected with display screen (14), described display screen (14) is installed on the lateral wall of outer barrel (6).
Spiral reaction unit the most according to claim 1, it is characterised in that: described reactor body (18) top is provided with air vent (16)；Cover plate (17) is installed on described air vent (16), between described air vent (16) and cover plate (17), is provided with rubber blanket (19).
Spiral reaction unit the most according to claim 1, it is characterized in that: described reactor body (18) top is additionally provided with injection port (21), sample introduction cover plate (22) is installed on injection port (21), between described injection port (21) and sample introduction cover plate (22), is provided with rubber blanket (19).
Spiral reaction unit the most according to claim 1, it is characterised in that: described reactor body (18) is made up of interior bucket (7) and outer barrel (6), is provided with vacuum voids between interior bucket (7) and outer barrel (6).
Spiral reaction unit the most according to claim 9, it is characterised in that: it is additionally provided with anticorrosive coat (15) on the medial wall of described interior bucket (6).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520913021.2U CN205517780U (en) | 2016-05-23 | 2016-05-23 | Spiral reaction unit |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520913021.2U CN205517780U (en) | 2016-05-23 | 2016-05-23 | Spiral reaction unit |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205517780U true CN205517780U (en) | 2016-08-31 |
Family
ID=56761572
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520913021.2U Expired - Fee Related CN205517780U (en) | 2016-05-23 | 2016-05-23 | Spiral reaction unit |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205517780U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105251431A (en) * | 2015-11-17 | 2016-01-20 | 苏州市金翔钛设备有限公司 | Spiral type reaction device |
-
2016
- 2016-05-23 CN CN201520913021.2U patent/CN205517780U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105251431A (en) * | 2015-11-17 | 2016-01-20 | 苏州市金翔钛设备有限公司 | Spiral type reaction device |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20160831 Termination date: 20170523 |