CN204503067U - Be applicable to the stirring apparatus for reaction kettle of high viscosity material - Google Patents

Be applicable to the stirring apparatus for reaction kettle of high viscosity material Download PDF

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Publication number
CN204503067U
CN204503067U CN201420869520.1U CN201420869520U CN204503067U CN 204503067 U CN204503067 U CN 204503067U CN 201420869520 U CN201420869520 U CN 201420869520U CN 204503067 U CN204503067 U CN 204503067U
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China
Prior art keywords
stirring vane
stirring
reactor
applicable
high viscosity
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CN201420869520.1U
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Chinese (zh)
Inventor
李申
李珊珊
唐晓先
赵泽华
常彩
郑倩
赵晓刚
黄远寿
李哲
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Anhui Jiuwu Tianhong Environmental Protection Technology Co., Ltd.
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ANHUI TIANHONG LVZHOU ENVIRONMENTAL PROTECTION TECHNOLOGY Co Ltd
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Abstract

The utility model relates to reactor stirring technique field, particularly relates to the stirring apparatus for reaction kettle being applicable to high viscosity material.Agitating device comprises the fan-shaped one-level stirring vane, paddle secondary stirring vane, frame three grades of stirring vanes and several lower skateboards that have and be bent downwardly radian, and lower skateboard is fixed on reactor madial wall, and is 60 ° of angles with madial wall.The utility model adopts multistage multiple stirring vane to contribute to improving mixing speed and uniformity coefficient, and one-level stirring vane and lower skateboard are combined with and help the material of input to be dispersed in reactor cavity, improves dispersion and the mixing evenness of material.

Description

Be applicable to the stirring apparatus for reaction kettle of high viscosity material
Technical field
The utility model belongs to reactor stirring technique field, particularly relates to the stirring apparatus for reaction kettle being applicable to high viscosity material.
Background technology
In the industrial production, stirring operation can make two or more different materials disperse mutually among each other, thus reaches Homogeneous phase mixing, also accelerates heat transfer and mass transport process simultaneously.
Present stage reactor industry, many use individual layer spiral agitators in high concentration material whipping process, but spiral agitator is applicable to stir the lower material such as liquid, suspension, emulsion of viscosity more, for the material that viscosity is higher, adopt individual layer spiral agitator that material cannot be made fully to be mixed and make material occur to react thoroughly, cause course of reaction overlong time, energy consumption is excessive, affects product income.
When generally feeding intake, material directly drops in reactor, mixes with material in still.Such as, but the material that some additions account for overall reaction material proportion less directly drops into, catalyst etc., easily cause this material local concentration in still too high, cause the side reactions such as organic matter implode, affect reaction result or product quality.
Utility model content
Technical problem to be solved in the utility model is to provide that a kind of stirring efficiency is high, material dispersion and the stirring apparatus for reaction kettle being applicable to high viscosity material that mixes.
For solving the problems of the technologies described above, the utility model provides following technical scheme: the stirring apparatus for reaction kettle being applicable to high viscosity material, comprise the transmission device being arranged at reactor outside, the shaft being arranged at reactor inside, be arranged on stirring vane on shaft and several lower skateboards, described stirring vane is divided into one-level stirring vane, secondary stirring vane and three grades of stirring vanes, one-level stirring vane is positioned at the top of shaft, secondary stirring vane is the middle part with shaft, and three grades of stirring vanes are positioned at the bottom of shaft; One-level stirring vane is that to have the sector, the secondary stirring vane that are bent downwardly radian be paddle blade, and three grades of stirring vanes are frame blade; Described lower skateboard is fixed on reactor madial wall, is 40 ° to 70 ° angles with madial wall.
Further, described lower skateboard is ring-type, and diameter and the reactor intracavity section diameter of a circle of ring match, and lower skateboard and madial wall are 60 ° of angles.
Further, described one-level stirring vane is at least evenly distributed with 3 sectors; Described secondary stirring vane equidistantly divides three layers, and every layer is at least evenly distributed with 3 paddle blades; Described three grades of stirring vanes are 1.
The beneficial effect that the utility model compared with prior art has is: agitating device adopts multiple stirring vanes of three ranks, can fully stir the material of high viscosity, is convenient to storeroom and merges; One-level stirring vane adopts reclinate sector, the material of input is convenient to disperse to surrounding, simultaneously, the lower skateboard that reactor madial wall is arranged contributes to the material dropped into disperse to reactor chamber central, avoid material concentration of local near cavity wall, improve the uniformity of material dispersion and mixing further.
Accompanying drawing explanation
Fig. 1 is the structural representation of the utility model agitating device.
Detailed description of the invention
In order to make the purpose of this utility model, technical scheme and advantage clearly understand, below in conjunction with drawings and Examples, the utility model is further elaborated.Should be appreciated that specific embodiment described herein only in order to explain the utility model, and be not used in restriction the utility model.
In description of the present utility model, it will be appreciated that, term " longitudinal direction ", " transverse direction ", " on ", D score, " front ", " afterwards ", " left side ", " right side ", " vertically ", " level ", " top ", " end ", " interior ", orientation or the position relationship of the instruction such as " outward " are based on orientation shown in the drawings or position relationship, it is only the utility model for convenience of description, instead of indicate or imply that the device of indication or element must have specific orientation, with specific azimuth configuration and operation, therefore can not be interpreted as restriction of the present utility model.
As shown in Figure 1, be applicable to the stirring apparatus for reaction kettle of high viscosity material, comprise the transmission device 1 being arranged at reactor outside, the shaft 2 being arranged at reactor inside, be arranged on stirring vane on shaft 2 and several lower skateboards 6, described stirring vane is divided into one-level stirring vane 3, secondary stirring vane 4 and three grades of stirring vanes 5, one-level stirring vane 3 is positioned at the top of shaft 2, secondary stirring vane 4 is the middle part with shaft 2, and three grades of stirring vanes 5 are positioned at the bottom of shaft 2; One-level stirring vane 3 is bent downwardly the sector of radian for having, secondary stirring vane 4 is paddle blade, and three grades of stirring vanes 5 are frame blade.
One-level stirring vane 3 is at least evenly distributed with 3 sectors; Described secondary stirring vane 4 equidistantly divides three layers, and every layer is at least evenly distributed with 3 paddle blades; Described three grades of stirring vanes 5 are 1.Agitating device adopts multiple stirring vanes of three ranks, can fully stir the material of high viscosity, is convenient to storeroom and merges, and improves efficiency and the mixing quality of material stirring.
One-level stirring vane 3 adopts reclinate sector, be convenient to by drop into material dispersed to surrounding, can also by the material of overflow deadweight and blade effect under deliver to equably in the working region of secondary stirring vane 4 and three grades of stirring vanes 5.Described lower skateboard 6 is fixed on reactor madial wall, is 40 ° to 70 ° angles with madial wall, preferably 60 ° herein.Lower skateboard 6 is ring-type, and diameter and the reactor intracavity section diameter of a circle of ring match.Reactor madial wall is arranged lower skateboard 6 to contribute to the material dropped into disperse to reactor chamber central, avoid material concentration of local near cavity wall, the uniformity improving material dispersion further and be uniformly mixed.
The foregoing is only preferred embodiment of the present utility model; not in order to limit the utility model; all do within spirit of the present utility model and principle any amendment, equivalent to replace and improvement etc., all should be included within protection domain of the present utility model.

Claims (3)

1. be applicable to the stirring apparatus for reaction kettle of high viscosity material, comprise the transmission device (1) being arranged at reactor outside, be arranged at the shaft (2) of reactor inside, and the stirring vane be arranged on shaft (2), it is characterized in that: also comprise several lower skateboards (6), described stirring vane is divided into one-level stirring vane (3), secondary stirring vane (4) and three grades of stirring vanes (5), one-level stirring vane (3) is positioned at the top of shaft (2), secondary stirring vane (4) is the middle part with shaft (5), three grades of stirring vanes (5) are positioned at the bottom of shaft (2), one-level stirring vane (3) is for having the sector being bent downwardly radian, and secondary stirring vane (4) is paddle blade, and three grades of stirring vanes (5) are frame blade, described lower skateboard (6) is fixed on reactor madial wall, is 40 ° to 70 ° angles with madial wall.
2. the stirring apparatus for reaction kettle being applicable to high viscosity material according to claim 1, it is characterized in that: described lower skateboard (6) is ring-type, diameter and the reactor intracavity section diameter of a circle of ring match, and lower skateboard (6) and madial wall are 60 ° of angles.
3. the stirring apparatus for reaction kettle being applicable to high viscosity material according to claim 1 and 2, is characterized in that: described one-level stirring vane (3) is at least evenly distributed with 3 sectors; Described secondary stirring vane (4) is equidistantly divided three layers, and every layer is at least evenly distributed with 3 paddle blades; Described three grades of stirring vanes (5) are 1.
CN201420869520.1U 2014-12-23 2014-12-23 Be applicable to the stirring apparatus for reaction kettle of high viscosity material Active CN204503067U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201420869520.1U CN204503067U (en) 2014-12-23 2014-12-23 Be applicable to the stirring apparatus for reaction kettle of high viscosity material

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201420869520.1U CN204503067U (en) 2014-12-23 2014-12-23 Be applicable to the stirring apparatus for reaction kettle of high viscosity material

Publications (1)

Publication Number Publication Date
CN204503067U true CN204503067U (en) 2015-07-29

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Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106890580A (en) * 2017-03-17 2017-06-27 叶雨玲 Chinese herbal ointment formula stirring-head
CN109046214A (en) * 2018-09-10 2018-12-21 包头轻工职业技术学院 Reaction kettle
CN110126112A (en) * 2019-05-29 2019-08-16 南通方志新材料科技有限公司 A kind of mixing apparatus for water-borne plastic coatings production
CN114618342A (en) * 2020-12-09 2022-06-14 于梦婷 Beverage production equipment with good mixing effect

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106890580A (en) * 2017-03-17 2017-06-27 叶雨玲 Chinese herbal ointment formula stirring-head
CN109046214A (en) * 2018-09-10 2018-12-21 包头轻工职业技术学院 Reaction kettle
CN110126112A (en) * 2019-05-29 2019-08-16 南通方志新材料科技有限公司 A kind of mixing apparatus for water-borne plastic coatings production
CN114618342A (en) * 2020-12-09 2022-06-14 于梦婷 Beverage production equipment with good mixing effect
CN114618342B (en) * 2020-12-09 2023-05-02 广东省香雪亚洲食品有限公司 Beverage production equipment with good mixing effect

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Address after: Room 501, C-1 R&D Building, KB4-4 Block, Hefei High-tech Zone, Anhui Province, 230088

Patentee after: Anhui Jiuwu Tianhong Environmental Protection Technology Co., Ltd.

Address before: Room 501, C-1 R&D Building, KB4-4 Block, Hefei High-tech Zone, Anhui Province, 230088

Patentee before: Anhui Tianhong Lvzhou Environmental Protection Technology Co., Ltd.