CN202129072U - Reactor for producing resin products - Google Patents
Reactor for producing resin products Download PDFInfo
- Publication number
- CN202129072U CN202129072U CN201120195229U CN201120195229U CN202129072U CN 202129072 U CN202129072 U CN 202129072U CN 201120195229 U CN201120195229 U CN 201120195229U CN 201120195229 U CN201120195229 U CN 201120195229U CN 202129072 U CN202129072 U CN 202129072U
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- Prior art keywords
- kettle
- flabellum
- anchor agitator
- materials
- jack
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- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
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Abstract
A reactor for producing resin products comprises a vertical stirring shaft and a vertical reactor body. The upper end and the lower end of the vertical reactor body are closed, the lower end of the stirring shaft penetrates into the reactor body and is connected with a U-shaped anchor type stirrer, the upper end of the stirring shaft is exposed out of the upper end of the reactor body, a gap is reserved between the anchor type stirrer and each of side walls and the bottom wall of the reactor body, a plurality of pushing type upper stirring blades are peripherally uniformly distributed in the middle of the stirring shaft, the upper end of the anchor type stirrer is positioned within the height range of each upper stirring blade, and a gap is reserved between an extending end of each stirring blade and the inner wall of each side of the anchor type stirrer. When materials are stirred, the upper stirring blades push the materials floating in the reactor body downwards, so that the materials around the stirring shaft rotate at higher speed (particularly, rotation speed of the materials within the radius range of 20cm of the stirring shaft is increased remarkably), and the materials in different axial areas rotate at similar speed. In addition, by the aid of coordination of the anchor type stirrer, the materials are mixed better and solid and liquid cannot be separated easily. Accordingly, by the aid of the reactor for producing resin products, material scattering effect is better, sizes of grains of the resin products are uniform, and yield of the resin products is high.
Description
Technical field
The utility model relates to a kind of naval stores production and uses agitated reactor.
Background technology
Existing naval stores production for the material in the kettle is stirred, is adopted anchor agitator or gate stirrer with in the agitated reactor usually.All there is following defective in these two kinds of stirring structure forms: when stirring material, and the material of zones of different radially, its rotating speed difference is bigger; The material in the 20cm radius around the shaft particularly, its rotating speed is very slow, this make the material dispersed poor effect, Separation of Solid and Liquid appears easily; And solid phase can break away from water; Float on the liquid level or be sunken under the liquid level, finally form caking, so that the particle diameter of naval stores is inhomogeneous, yield is low.
The utility model content
The utility model technical problem to be solved provides a kind of naval stores production and uses agitated reactor, adopts this agitated reactor, and the material dispersed effect is preferable, so that the particle diameter of naval stores is even, yield is high.
For solving the problems of the technologies described above; The utility model provides a kind of naval stores production to use agitated reactor; It comprises the vertical shaft and the vertical kettle of closed at both ends up and down, and the lower end of shaft penetrates in the kettle from the upper end of kettle and is connected to the anchor agitator of U-shaped, and the upper end of shaft is exposed at outside the upper end of kettle; Anchor agitator leaves the gap respectively and between the sidewall of kettle and the diapire; The middle part of shaft circumferentially is uniformly distributed with the flabellum that go up to stir of some press-down types, and the upper end of anchor agitator is positioned at said going up within the altitude range that stirs flabellum, on stir between the sidepiece inwall of overhanging end and anchor agitator of flabellum and leave the gap.
For can concise description for the purpose of the problem, below said naval stores production all abbreviates this agitated reactor as with agitated reactor to the utility model.
When stirring material; Last stirring flabellum is pushed the material that floats in the kettle downwards; Let and stir axial material, its rotating speed obviously increases (particularly the material in the 20cm radius around the shaft, its rotating speed accelerates particularly evident); The feasible radially material of zones of different, its rotating speed difference is little; In addition, through the coordinated of anchor agitator, let material stirred, not be prone to Separation of Solid and Liquid preferably.
Therefore, adopt this agitated reactor, the material dispersed effect is preferable, so that the particle diameter of naval stores is even, yield is high.
As the optimization of the utility model, the bottom of said shaft circumferentially is uniformly distributed with the following stirring flabellum of some upper-turn-types, and the lower end of anchor agitator is lower than stirs flabellum down, leaves the gap between the overhanging end of following stirring flabellum and the sidepiece inwall of anchor agitator.
When stirring material, following stirring flabellum pushes the material that sinks in the kettle to the top, and in addition, the coordinated through last stirring flabellum and anchor agitator lets material stirred further, further improves the material dispersed effect.
As the further optimization of the utility model, the upper end of said kettle has a jack, and the downward view field of jack is between the sidewall of anchor agitator and kettle;
The upper end of kettle corresponding to the jack place be provided with one with jack coaxial communicate vertically articulate pipe, the upper end that articulates pipe have two specifications identical and be cross-shaped cross and arrange recessed;
Vertically carry the lower end of carrying bar through articulating pipe and jack and put in the kettle and being connected to vertical power-assisted baffle plate; The specification of power-assisted baffle plate makes it insert between the sidewall of anchor agitator and kettle, vertically carries the top of carrying bar and is uniformly distributed with the identical horizontal pin-and-hole of some specifications along its short transverse;
One of plug-in mounting and arbitrary recessed suitable horizontal bearing pin in arbitrary pin-and-hole, bearing pin places arbitrary recessed.
When stirring material; The power-assisted baffle plate makes the change of the material between anchor agitator and the kettle sidewall direction of motion in the kettle; Let said material flow, further increase the shaft rotating speed of material on every side, let material further stirred towards the direction of shaft; Further improve the material dispersed effect, the uniformity of material is better; In addition, when stirring material, can by means of bearing pin and some pin-and-holes, regulate the height of power-assisted baffle plate in kettle easily according to actual needs.
As the further optimization of the utility model, the said angle that presses down that goes up the stirring flabellum is 45o, and turning over angle on the following stirring flabellum is 45o.Like this, when stirring material, can guarantee the material dispersed best results.
Description of drawings
Fig. 1 is the structural representation of this agitated reactor.
Fig. 2 is the stereogram (leaving out the part-structure of front side) of this agitated reactor.
Fig. 3 is the partial enlarged drawing of A portion among Fig. 2.
The specific embodiment
Specifically describe below in conjunction with the embodiment of accompanying drawing the utility model.
Referring to Fig. 1-Fig. 3, this agitated reactor comprises the vertical shaft 2 and the vertical kettle 1 of closed at both ends up and down.
The lower end of shaft 2 penetrates in the kettle 1 from the center, upper end of kettle 1 and is connected to the anchor agitator 3 of U-shaped, and the upper end of shaft 2 is exposed at outside the upper end of kettle 1, and anchor agitator 3 leaves the gap respectively and between the sidewall of kettle 1 and the diapire.
The middle part of shaft 2 circumferentially is uniformly distributed with going up of two press-down types and stirs flabellum 4; The angle that presses down of last stirring flabellum 4 is 45o; The upper end of anchor agitator 3 is positioned within the said altitude range that go up to stir flabellum 4, on stir between the sidepiece inwall of overhanging end and anchor agitator 3 of flabellum 4 and leave the gap.
The bottom of shaft 2 circumferentially is uniformly distributed with the following stirring flabellum 5 of two upper-turn-types; Stir down flabellum 5 on to turn over angle be 45o; The lower end of anchor agitator 3 is lower than stirs flabellum 5 down, leaves the gap between the overhanging end of following stirring flabellum 5 and the sidepiece inwall of anchor agitator 3.
Two go up to be stirred flabellum 4, two to stir flabellum 5 down affixed with two decks 61, and each deck 61 is the semicircular plate that open side respectively has an overhanging wing plate, and two decks 61 are fixed on the shaft 2 by six groups of securing members 62.
The upper end of kettle 1 has a jack 11, and the downward view field of jack 11 is between the sidewall of anchor agitator 3 and kettle 1;
The upper end of kettle 1 corresponding to jack 11 places be provided with one with jack 11 coaxial communicate vertically articulate pipe 7, the upper end that articulates pipe 7 have two specifications identical and be cross-shaped cross arrange recessed 71;
Vertically carry the lower end of carrying bar 8 through articulating pipe 7 and put in the kettle 1 and being connected to vertical power-assisted baffle plate 82 with jack 11; The specification of power-assisted baffle plate 82 makes it insert between the sidewall of anchor agitator 3 and kettle 1; Vertically carry the top of carrying bar 8 and be uniformly distributed with seven horizontal pin-and-holes 81 that specification is identical along its short transverse, the distance between per two horizontal pin-and-holes 81 is 50mm;
One of plug-in mounting and arbitrary recessed 71 suitable horizontal bearing pins 9 in the 3rd pin-and-hole 81 of number from top to bottom, bearing pin 9 places one recessed 71.
When stirring material, through last stirring flabellum 4, stir the coordinated effect of flabellum 5, anchor agitator 3, power-assisted baffle plate 82 down, guarantee that the material dispersed effect is quite good, the uniformity of material is fairly good, so that the particle diameter of naval stores is even, yield is high.
Above-described only is a kind of embodiment of the utility model.Should be pointed out that for the person of ordinary skill of the art under the prerequisite that does not break away from the utility model principle, can also make some modification and improvement, these also should be regarded as belonging to the protection domain of the utility model.
Claims (5)
1. agitated reactor is used in naval stores production; Comprise the vertical shaft and the vertical kettle of closed at both ends up and down; The lower end of shaft penetrates in the kettle from the upper end of kettle and is connected to the anchor agitator of U-shaped; The upper end of shaft is exposed at outside the upper end of kettle, and anchor agitator leaves the gap respectively and between the sidewall of kettle and the diapire, it is characterized in that: the middle part of shaft circumferentially is uniformly distributed with going up of some press-down types and stirs flabellum; The upper end of anchor agitator is positioned within the said altitude range that go up to stir flabellum, on stir between the sidepiece inwall of overhanging end and anchor agitator of flabellum and leave the gap.
2. agitated reactor is used in naval stores production according to claim 1; It is characterized in that: the bottom of shaft circumferentially is uniformly distributed with the following stirring flabellum of some upper-turn-types; The lower end of anchor agitator is lower than stirs flabellum down, leaves the gap between the overhanging end of following stirring flabellum and the sidepiece inwall of anchor agitator.
3. agitated reactor is used in naval stores production according to claim 1 and 2, it is characterized in that:
The upper end of kettle has a jack, and the downward view field of jack is between the sidewall of anchor agitator and kettle;
The upper end of kettle corresponding to the jack place be provided with one with jack coaxial communicate vertically articulate pipe, the upper end that articulates pipe have two specifications identical and be cross-shaped cross and arrange recessed;
Vertically carry the lower end of carrying bar through articulating pipe and jack and put in the kettle and being connected to vertical power-assisted baffle plate; The specification of power-assisted baffle plate makes it insert between the sidewall of anchor agitator and kettle, vertically carries the top of carrying bar and is uniformly distributed with the identical horizontal pin-and-hole of some specifications along its short transverse;
One of plug-in mounting and arbitrary recessed suitable horizontal bearing pin in arbitrary pin-and-hole, bearing pin places arbitrary recessed.
4. agitated reactor is used in naval stores production according to claim 1 and 2, it is characterized in that: on stir flabellum the angle that presses down be 45o, turning over angle on the following stirring flabellum is 45o.
5. agitated reactor is used in naval stores production according to claim 3, it is characterized in that: on stir flabellum the angle that presses down be 45o, turning over angle on the following stirring flabellum is 45o.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201120195229U CN202129072U (en) | 2011-06-12 | 2011-06-12 | Reactor for producing resin products |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201120195229U CN202129072U (en) | 2011-06-12 | 2011-06-12 | Reactor for producing resin products |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN202129072U true CN202129072U (en) | 2012-02-01 |
Family
ID=45517858
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201120195229U Expired - Fee Related CN202129072U (en) | 2011-06-12 | 2011-06-12 | Reactor for producing resin products |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN202129072U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102274712A (en) * | 2011-06-12 | 2011-12-14 | 崔建 | Reaction kettle used for producing resin products |
| CN105505748A (en) * | 2014-11-14 | 2016-04-20 | 程叶红 | Biosurfactant microemulsion production system for chemical engineering |
-
2011
- 2011-06-12 CN CN201120195229U patent/CN202129072U/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102274712A (en) * | 2011-06-12 | 2011-12-14 | 崔建 | Reaction kettle used for producing resin products |
| CN105505748A (en) * | 2014-11-14 | 2016-04-20 | 程叶红 | Biosurfactant microemulsion production system for chemical engineering |
| CN105505748B (en) * | 2014-11-14 | 2018-08-31 | 三门华迈化工产品有限公司 | A kind of biological surfactant microemulsion production system for chemical industry |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| EE01 | Entry into force of recordation of patent licensing contract |
Assignee: Bengbu Liaoyuan New Material Co., Ltd. Assignor: Cui Jian Contract record no.: 2014340000053 Denomination of utility model: Reaction kettle used for producing resin products Granted publication date: 20120201 License type: Exclusive License Record date: 20140327 |
|
| LICC | Enforcement, change and cancellation of record of contracts on the licence for exploitation of a patent or utility model | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20120201 Termination date: 20150612 |
|
| EXPY | Termination of patent right or utility model |