CN205925680U - Free reation kettle of production polycarboxylic acids - Google Patents
Free reation kettle of production polycarboxylic acids Download PDFInfo
- Publication number
- CN205925680U CN205925680U CN201620377921.4U CN201620377921U CN205925680U CN 205925680 U CN205925680 U CN 205925680U CN 201620377921 U CN201620377921 U CN 201620377921U CN 205925680 U CN205925680 U CN 205925680U
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- China
- Prior art keywords
- tank body
- rotary shaft
- blade
- pair
- polycarboxylic acids
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- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
The utility model relates to a free reation kettle of production polycarboxylic acids, including one jar of body, a jar body is made by stainless steel material, and the latter half cover of jar external side is equipped with the carbon steel material cover, establishes material inlet pipe on jar body, jar internal rotation axis that is equipped with, the lower extreme of rotation axis extends an arc puddler to both sides respectively, the lower part of rotation axis respectively the pin joint have first to paddle and second to the paddle, be provided with two slope stirring leaves on the rotation axis, the upper end that two arc puddlers are connected respectively to leaves is stirred in two slopes, material inlet pipe includes vertical pipe and inclined tube, and on jar body was fixed in in the installation of vertical pipe, inclined tube connected the lower extreme of vertical pipe, and inclined tube lies in a jar internal portion, and the rotatory axis inclination of orientation sets up, and inclined tube's end includes upper end and tip down, upper end and lower extreme position in same vertical on -line. It is even that free reation kettle of production polycarboxylic acids can make the material distribute, and chemical reaction is complete, improves production efficiency, reduction in production cost.
Description
Technical field
This utility model is related to a kind of reactor, more particularly, to a kind of reactor producing polycarboxylic acids monomer.
Background technology
Water reducer refers to, under concrete workability and cement consumption permanence condition, to reduce mixing water amount, improve and mix
Solidifying soil intensity;Or under workability and intensity permanence condition, save the additive of cement consumption.Polycarboxylic acid series high-performance diminishing
Agent is that at present forefront, scientific and technological content highest, a kind of application prospect is best, combination property is optimum concrete are super plasticized in the world
Agent.
Polycarboxylate high performance water-reducing agent is the compound product of carboxylic acidss graft polyol copolymer and other effectively auxiliary agents, system
Standby polycarboxylate high performance water-reducing agent need to first prepare polycarboxylic acids monomer.In the reactor using at present, material skewness, change
Learn reaction not exclusively, lead to yield relatively low, production cost is higher.
It is therefore desirable to designing a kind of reactor producing polycarboxylic acids monomer, to overcome the problems referred to above.
Utility model content
The purpose of this utility model is to overcome the defect of prior art, there is provided one kind makes material be evenly distributed, chemistry
Reaction completely, can improve production efficiency, reduce the reactor of the production polycarboxylic acids monomer of production cost.
This utility model is realized in:
This utility model provides a kind of reactor producing polycarboxylic acids monomer, and including a tank body, described tank body is by rustless steel
Material is made, and the latter half outside described tank body is arranged with carbon steel material set, and described tank body sets material inlet pipe, described tank
It is provided with rotary shaft in vivo, described rotary shaft is located on the axis of described tank interior, and the outside at described tank body top is provided with
Motor, the upper end of described rotary shaft connects described motor;The lower end of described rotary shaft extends an arc puddler to both sides respectively,
Two arc puddlers all upwardly extend, and the bottom of described rotary shaft is articulated with first pair of blade and second pair of blade, institute respectively
State first pair of blade and described second pair of blade is respectively positioned on inside two described arc puddlers, described rotary shaft is provided with two
Individual inclination paddle, two tilt the upper end that paddle connects two arc puddlers respectively;Described material inlet pipe includes erecting
Straight tube and tipping tube, described VERTICAL TUBE is mounted on described tank body, and described tipping tube connects the lower end of described VERTICAL TUBE, institute
State tipping tube and be located at described tank interior, and be obliquely installed towards described rotary shaft, the end of described tipping tube includes upper end
And bottom, described upper end and described lower end part are on same vertical curve.
Further, described first pair of blade is located at the top of described second pair of blade, and is in " ten " font.
Further, described VERTICAL TUBE and described tipping tube are integrally formed.
This utility model has the advantages that:
The material come in from described material inlet pipe, by the mesozone of described inclination pipe inspection to described tank interior
Domain, can effectively prevent material autohemagglutination caking in inner tank wall in Deca, material is directly by arc puddler, first pair of blade
And second pair of blade is stirred together for, distribution is more uniform, improves the contact area of material reaction so as to reaction completes, can
Improve yield, reduces cost;Meanwhile, described tank body is made up of stainless steel material, and the latter half outside described tank body is arranged with
Carbon steel material set, has saved material, reduces cost of manufacture.
Brief description
In order to be illustrated more clearly that this utility model embodiment or technical scheme of the prior art, below will be to embodiment
Or in description of the prior art the accompanying drawing of required use be briefly described it should be apparent that, drawings in the following description are only
It is some embodiments of the present utility model, for those of ordinary skill in the art, in the premise not paying creative work
Under, other accompanying drawings can also be obtained according to these accompanying drawings.
The structural representation of the reactor of the production polycarboxylic acids monomer that Fig. 1 provides for this utility model embodiment.
Specific embodiment
Below in conjunction with the accompanying drawing in this utility model embodiment, the technical scheme in this utility model embodiment is carried out
Clearly and completely description is it is clear that described embodiment is only a part of embodiment of this utility model rather than whole
Embodiment.Based on the embodiment in this utility model, those of ordinary skill in the art are not making the premise of creative work
Lower obtained all other embodiment, broadly falls into the scope of this utility model protection.
As Fig. 1, this utility model embodiment provides a kind of reactor producing polycarboxylic acids monomer, including a tank body 100, institute
State tank body 100 to be made up of stainless steel material, the latter half in described tank body 100 outside is arranged with carbon steel material set 9, has saved material
Material, reduces cost of manufacture.
As Fig. 1, described tank body 100 sets material inlet pipe, in described tank body 100, be provided with rotary shaft 1, described rotary shaft 1
On axis within positioned at described tank body 100, the outside at described tank body 100 top is provided with motor 2, described rotary shaft 1
Upper end connects described motor 2.Described motor 2 drives described rotary shaft 1 to be rotated, and can control the rotation of described rotary shaft 1
Speed.
As Fig. 1, described material inlet pipe includes VERTICAL TUBE 7 and tipping tube 8, and described VERTICAL TUBE 7 is mounted on described tank
On body 100, described tipping tube 8 connects the lower end of described VERTICAL TUBE 7, and described tipping tube 8 is located inside described tank body 100, and court
It is obliquely installed to described rotary shaft 1, the material come in from described material inlet pipe, sprayed to described tank by described tipping tube 8
Zone line within body 100, can effectively prevent material autohemagglutination caking on tank body 100 inwall in Deca, make material reaction
Completely.The end of described tipping tube 8 includes upper end 81 and bottom 82, and described upper end 81 and described bottom 82 are positioned at same
So that material is difficult to rest on the terminal part of described tipping tube 8 on one vertical curve, effectively solve the problems, such as feed blocking.
In this preferred embodiment, described VERTICAL TUBE 7 is integrally formed with described tipping tube 8 so that its making is more convenient.
As Fig. 1, respectively to both sides extension one arc puddler 3, two arc puddlers 3 are equal for the lower end of described rotary shaft 1
Upwardly extend, the bottom of described rotary shaft 1 is articulated with first pair of blade 4 and second pair of blade 5, described first pair of blade 4 respectively
It is respectively positioned on inside two described arc puddlers 3 with described second pair of blade 5, it is right that described first pair of blade 4 is located at described second
The top of blade 5, and be in " ten " font.Two inclination paddles 6, two 6 points of paddles of inclination are provided with described rotary shaft 1
Not Lian Jie two arc puddlers 3 upper end, two tilt paddles 6 be used for oblique cutting stirring, strengthen mixing effect.Pass through
Motor 2 is rotated axle 1 and rotates, and rotary shaft 1 drives arc puddler 3 to rotate in tank body 100, and the material in tank body 100 obtains
Stir to preliminary, add that 4, second pair of blade 5 of first pair of blade and inclination paddle 6 are stirred together for so that material is filled
The stirring dividing, reaction completely, can improve yield.
In sum, the material come in from described material inlet pipe, injects directly to described tank body by above-mentioned tipping tube 8
Zone line within 100, can effectively prevent material autohemagglutination caking on tank body 100 inwall in Deca, material is directly by arc
3, first pair of blade 4 of shape puddler and second pair of blade 5 are stirred together for, and distribution is more uniform, improves connecing of material reaction
Contacting surface is amassed so as to reaction completes, and can improve yield, reduces cost;Meanwhile, described tank body 100 is made up of stainless steel material, described
The latter half in tank body 100 outside is arranged with carbon steel material set, has saved material, has reduced cost of manufacture.
The foregoing is only preferred embodiment of the present utility model, not in order to limit this utility model, all this
Within the spirit of utility model and principle, any modification, equivalent substitution and improvement made etc., should be included in this utility model
Protection domain within.
Claims (3)
1. a kind of reactor producing polycarboxylic acids monomer is it is characterised in that include a tank body, described tank body is by stainless steel material system
Become, the latter half outside described tank body is arranged with carbon steel material set, described tank body sets material inlet pipe, sets in described tank body
There is rotary shaft, described rotary shaft is located on the axis of described tank interior, and the outside at described tank body top is provided with motor, institute
The upper end stating rotary shaft connects described motor;
The lower end of described rotary shaft extends an arc puddler to both sides respectively, and two arc puddlers all upwardly extend, described
The bottom of rotary shaft is articulated with first pair of blade and second pair of blade respectively, and described first pair of blade and described second pair of blade are equal
Inside two described arc puddlers, described rotary shaft is provided with two inclination paddles, two tilt paddle and divide
Not Lian Jie two arc puddlers upper end;
Described material inlet pipe includes VERTICAL TUBE and tipping tube, and described VERTICAL TUBE is mounted on described tank body, described inclination
Pipe connects the lower end of described VERTICAL TUBE, and described tipping tube is located at described tank interior, and is obliquely installed towards described rotary shaft, institute
The end stating tipping tube includes upper and lower end, and described upper end and described lower end part are on same vertical curve.
2. as claimed in claim 1 produce polycarboxylic acids monomer reactor it is characterised in that:Described first pair of blade is located at institute
State the top of second pair of blade, and be in " ten " font.
3. as claimed in claim 1 or 2 produce polycarboxylic acids monomer reactor it is characterised in that:Described VERTICAL TUBE with described
Tipping tube is integrally formed.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201620377921.4U CN205925680U (en) | 2016-04-29 | 2016-04-29 | Free reation kettle of production polycarboxylic acids |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201620377921.4U CN205925680U (en) | 2016-04-29 | 2016-04-29 | Free reation kettle of production polycarboxylic acids |
Publications (1)
Publication Number | Publication Date |
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CN205925680U true CN205925680U (en) | 2017-02-08 |
Family
ID=57934004
Family Applications (1)
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CN201620377921.4U Expired - Fee Related CN205925680U (en) | 2016-04-29 | 2016-04-29 | Free reation kettle of production polycarboxylic acids |
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Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN109603683A (en) * | 2019-01-17 | 2019-04-12 | 威士达半导体科技(张家港)有限公司 | Drop tube, adhesive preparation facilities and application |
-
2016
- 2016-04-29 CN CN201620377921.4U patent/CN205925680U/en not_active Expired - Fee Related
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN109603683A (en) * | 2019-01-17 | 2019-04-12 | 威士达半导体科技(张家港)有限公司 | Drop tube, adhesive preparation facilities and application |
CN109603683B (en) * | 2019-01-17 | 2024-04-12 | 威士达半导体科技(张家港)有限公司 | Drip tube, adhesive preparation device and application |
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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 |
Granted publication date: 20170208 Termination date: 20180429 |
|
CF01 | Termination of patent right due to non-payment of annual fee |