CN205007971U - Synthetic reactor stirrer of trifluoro ethyl acetoacetate - Google Patents
Synthetic reactor stirrer of trifluoro ethyl acetoacetate Download PDFInfo
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- CN205007971U CN205007971U CN201520697954.2U CN201520697954U CN205007971U CN 205007971 U CN205007971 U CN 205007971U CN 201520697954 U CN201520697954 U CN 201520697954U CN 205007971 U CN205007971 U CN 205007971U
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- agitator
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Abstract
本实用新型公开了一种三氟乙酰乙酸乙酯合成反应釜搅拌器,包括电机、减速器和搅拌轴,所述电机和减速器设有搅拌轴的顶端,所述搅拌轴上设有两级搅拌器,分别为第一搅拌器和第二搅拌器,所述第一搅拌器和第二搅拌器均为三叶推进式搅拌器,所述第一搅拌器和第二搅拌器的搅拌叶片与搅拌轴之间具有一定的倾角。本实用新型采用两级三叶推进式搅拌器,且搅拌叶片与搅拌轴之间具有一定的倾角,能够带动物料上下翻滚,提高对物料的搅拌率,进而加快传热、传质效率。两级搅拌器相对设置,能够更好地将物料提起来,加强对物料的搅拌力度,提高搅拌效率。
The utility model discloses a stirrer for a synthesis reaction kettle of ethyl trifluoroacetoacetate, which comprises a motor, a reducer and a stirring shaft, the motor and the reducer are provided with the top of the stirring shaft, and the stirring shaft is provided with two stages The agitator is respectively a first agitator and a second agitator, the first agitator and the second agitator are three-blade propulsion agitators, the stirring blades of the first agitator and the second agitator are connected with There is a certain inclination between the stirring shafts. The utility model adopts a two-stage three-leaf propulsion type agitator, and there is a certain inclination angle between the agitating blade and the agitating shaft, which can drive the material to roll up and down, improve the agitation rate of the material, and accelerate the heat transfer and mass transfer efficiency. The two-stage agitator is set opposite to each other, which can better lift the material, strengthen the mixing force of the material, and improve the mixing efficiency.
Description
技术领域 technical field
本实用新型属于化工设备领域,具体涉及一种三氟乙酰乙酸乙酯合成反应釜搅拌器。 The utility model belongs to the field of chemical equipment, in particular to a stirrer for a reaction kettle for synthesis of ethyl trifluoroacetoacetate.
背景技术 Background technique
三氟乙酰乙酸乙酯合成工艺一般在反应釜内进行,反应釜内设有搅拌器,现有的三氟乙酰乙酸乙酯合成反应釜一般采用锚式搅拌器,但由于三氟乙酰乙酸乙酯的料液粘度不是很大,采用锚式搅拌器不能对料液进行很好地搅拌,影响料液的混合,进而影响反应效果。 The synthesis process of ethyl trifluoroacetoacetate is generally carried out in a reactor, and an agitator is provided in the reactor. The existing ethyl trifluoroacetoacetate synthesis reactor generally adopts an anchor stirrer, but due to the ethyl trifluoroacetoacetate The viscosity of the feed liquid is not very high, and the anchor stirrer cannot be used to stir the feed liquid well, which will affect the mixing of the feed liquid, and then affect the reaction effect.
实用新型内容 Utility model content
针对现有技术的不足,本实用新型的目的在于提供一种三氟乙酰乙酸乙酯合成反应釜搅拌器,能够将物料更好地聚集起来从而快速、充分地搅拌物料,提高搅拌效率。 Aiming at the deficiencies of the prior art, the purpose of this utility model is to provide a stirrer for a reaction kettle for the synthesis of ethyl trifluoroacetoacetate, which can better gather the materials to stir the materials quickly and fully, and improve the stirring efficiency.
为实现上述目的,本实用新型采用的技术方案是:一种三氟乙酰乙酸乙酯合成反应釜搅拌器,包括电机、减速器和搅拌轴,所述电机和减速器设有搅拌轴的顶端,所述搅拌轴上设有两级搅拌器,分别为第一搅拌器和第二搅拌器,所述第一搅拌器和第二搅拌器均为三叶推进式搅拌器,所述第一搅拌器和第二搅拌器的搅拌叶片与搅拌轴之间具有一定的倾角。 In order to achieve the above object, the technical solution adopted in the utility model is: a kind of ethyl trifluoroacetoacetate synthesis reaction kettle stirrer, comprises motor, speed reducer and stirring shaft, and described motor and speed reducer are provided with the top of stirring shaft, The stirring shaft is provided with two-stage stirrers, respectively the first stirrer and the second stirrer, the first stirrer and the second stirrer are three-blade propulsion stirrers, and the first stirrer There is a certain inclination angle between the stirring blade and the stirring shaft of the second stirrer.
进一步,所述搅拌叶片与搅拌轴之间的倾角为10°。 Further, the inclination angle between the stirring blade and the stirring shaft is 10°.
进一步,所述第一搅拌器和第二搅拌器相对设置,所述第一搅拌器的倾角向下,所述第二搅拌器的倾角向上。 Further, the first agitator and the second agitator are arranged opposite to each other, the inclination angle of the first agitator is downward, and the inclination angle of the second agitator is upward.
进一步,所述第一搅拌器为左旋三叶推进式搅拌器,所述第二搅拌器为右旋三叶推进式搅拌器。 Further, the first agitator is a left-handed three-blade propulsion type agitator, and the second agitator is a right-handed three-blade propulsion type agitator.
进一步,所述第一搅拌器和第二搅拌器的搅拌叶片的直径为反应釜内径的1/3,搅拌叶片与反应釜内壁的距离为30-40cm。 Further, the diameter of the stirring blades of the first stirrer and the second stirrer is 1/3 of the inner diameter of the reactor, and the distance between the stirring blades and the inner wall of the reactor is 30-40 cm.
本实用新型的有益效果是:采用两级三叶推进式搅拌器,且搅拌叶片与搅拌轴之间具有一定的倾角,能够带动物料上下翻滚,提高对物料的搅拌率,进而加快传热、传质效率。两级搅拌器相对设置,能够更好地将物料提起来,加强对物料的搅拌力度,提高搅拌效率。第一搅拌器为左旋、第二搅拌器为右旋,两个搅拌器搅拌方向相对,也可以增加对物料的搅拌力度,进一步提高搅拌效率。 The beneficial effect of the utility model is that: a two-stage three-blade propulsion type agitator is adopted, and there is a certain inclination angle between the agitating blade and the agitating shaft, which can drive the material to roll up and down, improve the agitation rate of the material, and then accelerate heat transfer, quality efficiency. The two-stage agitator is set opposite to each other, which can better lift the material, strengthen the mixing force of the material, and improve the mixing efficiency. The first agitator is left-handed, the second agitator is right-handed, and the two agitators have opposite agitation directions, which can also increase the agitation strength of the material and further improve the agitation efficiency.
附图说明 Description of drawings
图1为本实用新型的结构示意图。 Fig. 1 is the structural representation of the utility model.
图2为第一搅拌器的结构示意图。 Fig. 2 is a structural schematic diagram of the first agitator.
图3为第二搅拌器的结构示意图。 Fig. 3 is a schematic structural diagram of the second agitator.
图中:1-电机,2-减速器,3-搅拌轴,4-反应釜,5-第一搅拌器,6-第二搅拌器。 In the figure: 1-motor, 2-reducer, 3-stirring shaft, 4-reactor, 5-first agitator, 6-second agitator.
具体实施方式 detailed description
下面结合附图及具体实施例对本实用新型作进一步详细的说明。 Below in conjunction with accompanying drawing and specific embodiment the utility model is described in further detail.
如图所示:一种三氟乙酰乙酸乙酯合成反应釜搅拌器,包括电机1、减速器2和搅拌轴3,所述电机1和减速器2设有搅拌轴3的顶端,所述搅拌轴3上设有两级搅拌器,分别为第一搅拌器5和第二搅拌器6,所述第一搅拌器5和第二搅拌器6均为三叶推进式搅拌器,所述第一搅拌器5和第二搅拌器6的搅拌叶片与搅拌轴3之间具有10°的倾角,所述第一搅拌器5和第二搅拌器6相对设置,所述第一搅拌器5的倾角向下,所述第二搅拌器6的倾角向上,所述第一搅拌器5为左旋三叶推进式搅拌器,所述第二搅拌器6为右旋三叶推进式搅拌器,所述第一搅拌器5和第二搅拌器6的搅拌叶片的直径为反应釜4内径的1/3,搅拌叶片与反应釜4内壁的距离为30-40cm。 As shown in the figure: a kind of ethyl trifluoroacetoacetate synthesis reactor stirrer, comprises motor 1, speed reducer 2 and stirring shaft 3, and described motor 1 and speed reducer 2 are provided with the top of stirring shaft 3, and described stirring The shaft 3 is provided with two-stage agitators, which are respectively the first agitator 5 and the second agitator 6, and the first agitator 5 and the second agitator 6 are all three-blade propulsion agitators, and the first agitator There is an inclination angle of 10° between the stirring blades of the agitator 5 and the second agitator 6 and the stirring shaft 3, the first agitator 5 and the second agitator 6 are relatively arranged, and the inclination angle of the first agitator 5 is toward Next, the inclination angle of the second agitator 6 is upward, the first agitator 5 is a left-handed three-blade propulsion type agitator, the second agitator 6 is a right-handed three-blade propulsion type agitator, and the first The diameter of the stirring blades of the agitator 5 and the second agitator 6 is 1/3 of the inner diameter of the reactor 4, and the distance between the stirring blades and the inner wall of the reactor 4 is 30-40 cm.
以上所述仅为本实用新型的较佳实施例,并非是对本实用新型的限制。本领域的普通技术人员在本实用新型的实质范围内所做出的变化、改型、添加或替换,也应属于本实用新型的保护范围。 The above descriptions are only preferred embodiments of the present utility model, and are not limitations of the present utility model. Changes, modifications, additions or replacements made by those skilled in the art within the essential scope of the present utility model should also belong to the protection scope of the present utility model.
Claims (6)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520697954.2U CN205007971U (en) | 2015-09-10 | 2015-09-10 | Synthetic reactor stirrer of trifluoro ethyl acetoacetate |
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| CN201520697954.2U CN205007971U (en) | 2015-09-10 | 2015-09-10 | Synthetic reactor stirrer of trifluoro ethyl acetoacetate |
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| CN205007971U true CN205007971U (en) | 2016-02-03 |
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| CN201520697954.2U Expired - Lifetime CN205007971U (en) | 2015-09-10 | 2015-09-10 | Synthetic reactor stirrer of trifluoro ethyl acetoacetate |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110370451A (en) * | 2019-08-05 | 2019-10-25 | 重庆市智翔铺道技术工程有限公司 | Continuous mixer is used in a kind of mixing of multicomponent high viscosity material containing sand material |
| CN112412758A (en) * | 2020-11-18 | 2021-02-26 | 青岛农业大学 | Follow-up sheet valve mixing and stirring piezoelectric pump |
-
2015
- 2015-09-10 CN CN201520697954.2U patent/CN205007971U/en not_active Expired - Lifetime
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110370451A (en) * | 2019-08-05 | 2019-10-25 | 重庆市智翔铺道技术工程有限公司 | Continuous mixer is used in a kind of mixing of multicomponent high viscosity material containing sand material |
| CN112412758A (en) * | 2020-11-18 | 2021-02-26 | 青岛农业大学 | Follow-up sheet valve mixing and stirring piezoelectric pump |
| CN112412758B (en) * | 2020-11-18 | 2022-08-23 | 青岛农业大学 | Follow-up sheet valve mixing and stirring piezoelectric pump |
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| GR01 | Patent grant | ||
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Granted publication date: 20160203 |