CN208098070U - Reaction kettle is used in a kind of production of bodied ferric sulfate - Google Patents
Reaction kettle is used in a kind of production of bodied ferric sulfate Download PDFInfo
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- CN208098070U CN208098070U CN201820239619.1U CN201820239619U CN208098070U CN 208098070 U CN208098070 U CN 208098070U CN 201820239619 U CN201820239619 U CN 201820239619U CN 208098070 U CN208098070 U CN 208098070U
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- Prior art keywords
- reaction kettle
- oxidant
- ferric sulfate
- bodied ferric
- fixedly connected
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Abstract
The utility model discloses a kind of bodied ferric sulfate production reaction kettles, including reaction kettle, one surface of reaction kettle is provided with oxidant inlet, one surface of reaction kettle is provided with discharge port, the inner surface of reaction kettle is provided with detection device, one surface of reaction kettle is fixedly connected with upper cover, one surface of oxidant inlet is fixedly connected with oxidant adding set, one surface of upper cover is provided with feed inlet, one surface of upper cover, which is run through, driving device, one end of driving device output shaft is fixedly connected with agitating shaft, one surface of agitating shaft is fixedly connected with stirring rod, the utility model relates to chemical industry equipment manufacturing technology fields.Bodied ferric sulfate production reaction kettle, oxidant plenum sprinkling is realized by oxidant adding set, is merged so that oxidant rotates in a kettle with raw material, is accelerated the rate of bodied ferric sulfate production, temperature control device can regulate and control oxidant and reach suitable temperature, further catalytic.
Description
Technical field
The utility model relates to chemical industry equipment manufacturing technology field, reaction kettle is used in specially a kind of bodied ferric sulfate production.
Background technique
The broad understanding of reaction kettle has the container physically or chemically reacted, is designed by the structure to container and is matched with parameter
It sets, realizes the mixed function for heating, evaporation, cooling and the low high speed that technique requires.
Reaction kettle is widely used in petroleum, chemical industry, rubber, pesticide, dyestuff, medicine, food, for complete vulcanization, nitrification,
Pressure vessel of the technical process such as hydrogenation, hydrocarbonylation, polymerization, condensation, such as reactor, reaction pot, decomposition pot, polymeric kettle etc., material
Matter generally has carbon manganese steel, stainless steel, zirconium, Ni-based, alloy and other composite materials.
Bodied ferric sulfate reaction kettle at this stage promotes the quickening of reaction by stirring rod structure, and catalytic efficiency is low, and
Simple being stirred is easy to contact reactant unevenly, and reaction is caused to be not thorough.
Utility model content
In view of the deficiencies of the prior art, the utility model provides a kind of bodied ferric sulfate production reaction kettle, solves
The low problem of bodied ferric sulfate reaction kettle mixing efficiency.
In order to achieve the above object, the utility model is achieved by the following technical programs：A kind of bodied ferric sulfate production
With reaction kettle, including reaction kettle, a surface of the reaction kettle is provided with oxidant inlet, the surface setting of the reaction kettle
There is discharge port, the inner surface of the reaction kettle is provided with detection device, and a surface of the reaction kettle is fixedly connected with upper cover, institute
The surface for stating oxidant inlet is fixedly connected with oxidant adding set；
One surface of the upper cover is provided with feed inlet, and a surface of the upper cover, which is run through, driving device, the driving
One end of device output shaft is fixedly connected with agitating shaft, and a surface of the agitating shaft is fixedly connected with stirring rod, the stirring
The bottom end of axis is fixedly connected with the inner surface of reaction kettle；
The oxidant adding set includes pressurized nozzle, and a surface of the pressurized nozzle and oxidant inlet cooperation are solid
Fixed, a surface of the pressurized nozzle is communicated with temperature control device, and a surface of the temperature control device is communicated with oxidant pipe.
Preferably, a surface of the stirring rod offers several apertures, to be respectively far from stirring axis direction aperture
43.2mm, 47.8mm, 51.1mm, 57.8mm, 71.5mm and 86.2mm.
Preferably, the two sides of the detection device are respectively arranged with temperature sensor and pressure sensor.
Preferably, the upper surface of the reaction kettle is fixedly connected by bolt with upper cover.
Preferably, the driving device is speed reducer, reduction ratio 60:1.
Preferably, heater strip and condenser pipe, a surface of the temperature control device are respectively arranged with inside the temperature control device
It is electrically connected by electric wire with detection device.
Preferably, the shape of the pressurized nozzle is prismatoid structure, and the inclined-plane of the pressurized nozzle offers rectangle
Spray orifice.
Preferably, a surface of the oxidant inlet and the junction of pressurized nozzle are wound with glue cloth.
Beneficial effect
The utility model provides a kind of bodied ferric sulfate production reaction kettle.Has following beneficial effect：
（1）, the bodied ferric sulfate production use reaction kettle, by oxidant adding set realize oxidant plenum sprinkling, make
Oxidant is rotated in a kettle with raw material and is merged, accelerate the rate that bodied ferric sulfate produces, temperature control device can regulate and control
Oxidant reaches suitable temperature, further catalytic.
（2）, the bodied ferric sulfate production use reaction kettle, reaction kettle internal solution can be made by the aperture in stirring rod
Flow velocity it is more uniform, close to reaction kettle edge aperture it is bigger, be conducive to the faster solution of edge liquid flow velocity and pass through, stir
The porous structure for mixing bar has further refined mixed effect in reaction kettle, improves reaction speed.
Detailed description of the invention
Fig. 1 is the schematic perspective view that reaction kettle is used in a kind of bodied ferric sulfate production of the utility model；
Fig. 2 is the explosive view that reaction kettle is used in a kind of bodied ferric sulfate production of the utility model；
Fig. 3 is the schematic perspective view of the utility model reaction kettle；
Fig. 4 is the structural schematic diagram of the utility model upper cover；
Fig. 5 is the cross-sectional view that reaction kettle is used in a kind of bodied ferric sulfate production of the utility model；
Fig. 6 is the schematic perspective view of the utility model oxidant adding set.
In figure：1 reaction kettle, 101 oxidant inlets, 102 discharge ports, 103 detection devices, 2 upper covers, 201 feed inlets, 202
Driving device, 203 agitating shafts, 204 stirring rods, 3 oxidant adding sets, 301 pressurized nozzles, 302 temperature control devices, 303 oxidations
Agent pipe.
Specific embodiment
The following will be combined with the drawings in the embodiments of the present invention, carries out the technical scheme in the embodiment of the utility model
Clearly and completely describe, it is clear that the described embodiments are only a part of the embodiments of the utility model, rather than whole
Embodiment.Based on the embodiments of the present invention, those of ordinary skill in the art are without making creative work
Every other embodiment obtained, fall within the protection scope of the utility model.
Fig. 1-6 is please referred to, the utility model provides a kind of technical solution：A kind of bodied ferric sulfate production reaction kettle, packet
Include reaction kettle 1；
Wherein as shown in Figs. 1-5, a surface of reaction kettle 1 is provided with oxidant inlet 101, and a surface of reaction kettle 1 is set
It is equipped with discharge port 102, the inner surface of reaction kettle 1 is provided with detection device 103, and a surface of reaction kettle 1 is fixedly connected with upper cover
2, a surface of oxidant inlet 101 is fixedly connected with oxidant adding set 3；
Wherein, the two sides of detection device 103 are respectively arranged with temperature sensor and pressure sensor；
Wherein, the upper surface of reaction kettle 1 is fixedly connected by bolt with upper cover 2；
One surface of upper cover 2 is provided with feed inlet 201, and a surface of upper cover 2, which is run through, driving device 202, driving device
One end of 202 output shafts is fixedly connected with agitating shaft 203, and a surface of agitating shaft 203 is fixedly connected with stirring rod 204, stirring
The bottom end of axis 203 is fixedly connected with the inner surface of reaction kettle 1；
Wherein, driving device 202 is speed reducer, reduction ratio 60:1；
Wherein as shown in figure 4, a surface of stirring rod 204 offers 6 apertures, far from 203 direction aperture of agitating shaft
Respectively 43.2mm, 47.8mm, 51.1mm, 57.8mm, 71.5mm and 86.2mm；
Wherein as shown in fig. 6, oxidant adding set 3 includes pressurized nozzle 301, a surface of pressurized nozzle 301 and oxygen
The cooperation of agent entrance 101 is fixed, and a surface of pressurized nozzle 301 is communicated with temperature control device 302, a surface of temperature control device 302
It is communicated with oxidant pipe 303；
Wherein, heater strip and condenser pipe are respectively arranged with inside temperature control device 302, a surface of temperature control device 302 passes through
Electric wire is electrically connected with detection device 103；
Wherein, the shape of pressurized nozzle 301 is prismatoid structure, and the inclined-plane of pressurized nozzle 301 offers rectangle spray orifice；
Wherein, a surface of oxidant inlet 101 and the junction of pressurized nozzle 301 are wound with glue cloth.
When work, raw materials for production are poured into 1 by 201, the Stirring counterclockwise of driving device 202, the biography inside 103
Sensor detects 1 internal temperature with pressure, and oxidant enters 302 by 303, if 1 internal temperature is excessively high, 302 pairs of oxidations
Agent is freezed, if 1 internal temperature is too low, 302 pairs of oxidants are heated, and the oxidant after temperature adjustment sprays into 1 by 301 pressurizations
Inside achievees the purpose that the flow rate of liquid for improving reaction solution so that raw material and oxidant accelerate rotation inside 1.
It should be noted that, in this document, relational terms such as first and second and the like are used merely to a reality
Body or operation are distinguished with another entity or operation, are deposited without necessarily requiring or implying between these entities or operation
In any actual relationship or order or sequence.Moreover, the terms "include", "comprise" or its any other variant are intended to
Non-exclusive inclusion, so that the process, method, article or equipment including a series of elements is not only wanted including those
Element, but also including other elements that are not explicitly listed, or further include for this process, method, article or equipment
Intrinsic element.
While there has been shown and described that the embodiments of the present invention, for the ordinary skill in the art,
It is understood that these embodiments can be carried out with a variety of variations in the case where not departing from the principles of the present invention and spirit, repaired
Change, replacement and variant, the scope of the utility model is defined by the appended claims and the equivalents thereof.
Claims (8)
1. a kind of bodied ferric sulfate production reaction kettle, including reaction kettle（1）, it is characterised in that：The reaction kettle（1）A table
Face is provided with oxidant inlet（101）, the reaction kettle（1）A surface be provided with discharge port（102）, the reaction kettle（1）
Inner surface be provided with detection device（103）, the reaction kettle（1）A surface be fixedly connected with upper cover（2）, the oxidant
Entrance（101）A surface be fixedly connected with oxidant adding set（3）；
The upper cover（2）A surface be provided with feed inlet（201）, the upper cover（2）A surface through there is driving device
（202）, the driving device（202）One end of output shaft is fixedly connected with agitating shaft（203）, the agitating shaft（203）One
Surface is fixedly connected with stirring rod（204）, the agitating shaft（203）Bottom end and reaction kettle（1）Inner surface be fixedly connected；
The oxidant adding set（3）Including pressurized nozzle（301）, the pressurized nozzle（301）A surface and oxidant
Entrance（101）Cooperation is fixed, the pressurized nozzle（301）A surface be communicated with temperature control device（302）, the temperature control device
（302）A surface be communicated with oxidant pipe（303）.
2. a kind of bodied ferric sulfate production reaction kettle according to claim 1, it is characterised in that：The stirring rod
（204）A surface offer several apertures, with far from agitating shaft（203）Direction aperture be respectively 43.2mm, 47.8mm,
51.1mm, 57.8mm, 71.5mm and 86.2mm.
3. a kind of bodied ferric sulfate production reaction kettle according to claim 1, it is characterised in that：The detection device
（103）Two sides be respectively arranged with temperature sensor and pressure sensor.
4. a kind of bodied ferric sulfate production reaction kettle according to claim 1, it is characterised in that：The reaction kettle（1）
Upper surface pass through bolt and upper cover（2）It is fixedly connected.
5. a kind of bodied ferric sulfate production reaction kettle according to claim 1, it is characterised in that：The driving device
（202）For speed reducer, reduction ratio 60:1.
6. a kind of bodied ferric sulfate production reaction kettle according to claim 1, it is characterised in that：The temperature control device
（302）Inside is respectively arranged with heater strip and condenser pipe, the temperature control device（302）A surface pass through electric wire and detection device
（103）Electrical connection.
7. a kind of bodied ferric sulfate production reaction kettle according to claim 1, it is characterised in that：The pressurized nozzle
（301）Shape be prismatoid structure, the pressurized nozzle（301）Inclined-plane offer rectangle spray orifice.
8. a kind of bodied ferric sulfate production reaction kettle according to claim 1, it is characterised in that：The oxidant inlet
（101）A surface and pressurized nozzle（301）Junction be wound with glue cloth.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820239619.1U CN208098070U (en) | 2018-02-11 | 2018-02-11 | Reaction kettle is used in a kind of production of bodied ferric sulfate |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820239619.1U CN208098070U (en) | 2018-02-11 | 2018-02-11 | Reaction kettle is used in a kind of production of bodied ferric sulfate |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN208098070U true CN208098070U (en) | 2018-11-16 |
Family
ID=64124847
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201820239619.1U Expired - Fee Related CN208098070U (en) | 2018-02-11 | 2018-02-11 | Reaction kettle is used in a kind of production of bodied ferric sulfate |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN208098070U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112221442A (en) * | 2020-10-10 | 2021-01-15 | 马鞍山健鼎化工有限公司 | Novel polymeric ferric sulfate production anti-oxidation preparation tank and working method |
-
2018
- 2018-02-11 CN CN201820239619.1U patent/CN208098070U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112221442A (en) * | 2020-10-10 | 2021-01-15 | 马鞍山健鼎化工有限公司 | Novel polymeric ferric sulfate production anti-oxidation preparation tank and working method |
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| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| 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: 20181116 Termination date: 20200211 |