CN2768892Y - Wet synthetic reactor - Google Patents
Wet synthetic reactor Download PDFInfo
- Publication number
- CN2768892Y CN2768892Y CN 200420069474 CN200420069474U CN2768892Y CN 2768892 Y CN2768892 Y CN 2768892Y CN 200420069474 CN200420069474 CN 200420069474 CN 200420069474 U CN200420069474 U CN 200420069474U CN 2768892 Y CN2768892 Y CN 2768892Y
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- reactive tank
- agitator
- wet method
- guide shell
- synthesis reactor
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Abstract
The utility model relates to a wet method synthesis reactor. The utility model is mainly composed of a diversion barrel, a stirrer and a driving device thereof and a heating device, wherein the diversion barrel and the stirrer and the driving device thereof are arranged inside a cylindrical reacting groove, and the heating device is arranged around the outside of the reacting groove; the upper end and the lower end of the diversion barrel are open, and the diversion barrel is arranged inside the reacting groove through a connection mechanism which can regulate position vertically; the stirrer is arranged on the top of a cylinder of the reacting groove by a lifting device, and the stirrer is coaxially connected with a speed-regulating motor; a plurality of vertical baffle plates are uniformly distributed on the circumference of the inner wall of the cylinder of the reacting groove, and the heating device is composed of an electric heating ring and a heat-insulating layer. Accordingly, the wet method synthesis reactor has the advantages that the utility model is suitable for the synthesis reaction of multiple kinds of metal and compounds; different reaction conditions can be designed according to the needs of users; the granularity distribution range of obtained products is centralized, the phenomenon of aggregation can not be generated, besides, the dispersing property is good; the utility model can simultaneously control reaction temperature, stirring speed and stirring mode of solution so as to obtain powder material or nanometer material with the granularity and the shape of the required product.
Description
Technical field:
The utility model relates to a kind of superfine powdery material and nano-powder material synthetic reaction equipment, particularly a kind of wet method synthesis reactor.
Background technology:
The wet method synthesis reactor that wet method prepares fine powder body material and nano material is used for the synthetic reaction that multiple metal such as aluminium oxide, zinc oxide, zinc powder, nickel powder, cobalt powder, nickel hydroxide and compound powder material thereof generate.Existing wet method synthesis reactor is mainly by in the drum shaped reaction groove guide shell, agitator and transmission device thereof being housed, around reactive tank heater being housed outward forms, existing wet method synthesis reactor guide shell upper end closed is fixed on groove and covers, only fluid is entered in the guide shell at a direction opening, the conductor weak effect, the setting height(from bottom) of existing agitator in reactive tank fixed, and be unadjustable, and the transmission device rotating speed of agitator adjustable speed scarcely; The heater of existing wet method synthesis reactor is to adopt steam heater, is difficult to accurately control temperature and quick adjustment temperature, and the interlayer cover of steam heater belongs to pressure vessel, manufacturing, maintenance difficult.Existing wet method synthesis reactor can not satisfy various powder body materials and generate the granularity of product and the demand of shape because reaction conditions such as reaction temperature, mixing speed are difficult to control.
Summary of the invention:
The purpose of this utility model is to overcome the above-mentioned defective of existing wet method synthesis reactor, designs a kind of reaction temperature, and reaction conditions such as solution mixing speed are easy to regulate, and are suitable for the wet method synthesis reactor of the powder body material of preparation different grain size and shape.
Technical solution of the present utility model is the wet method synthesis reactor, mainly by in the drum shaped reaction groove guide shell, agitator and transmission device thereof being housed, around reactive tank heater being housed outward and forming:
(1) the guide shell upper/lower terminal is uncovered, is loaded in the reactive tank via coupling mechanism that can upper and lower adjusting position;
(2) agitator is loaded on reactive tank drum top via lowering or hoisting gear; Agitator connects with buncher is coaxial;
(3) on the reactive tank drum inwall, the shelves stream plate of some settings of circumference uniform distribution;
(4) heater is that electric heating coil and heat-insulation layer are formed.
The agitator lowering or hoisting gear is made up of worm gear snail pavilion mechanism and pinion and rack, worm-and-wheel gear is installed on the gear-box of reactive tank top cover, the worm screw that ribbon gymnastics is made handle is agitator lift adjustment action bars, worm gear and gears engaged, the wheel and rack engagement, tooth bar is connected on the coupling sleeve of agitator.The coupling mechanism of guide shell and reactive tank is to connect firmly long bolt on the guide shell outer wall, the upper end is loaded on the reactive tank top cover through nut, the guide shell outer wall with connect firmly on the reactive tank cylindrical wall several uniform cantilevers through Bolt Connection, the Bolt Connection hole is for vertically to strip hole.
Description of drawings:
Fig. 1 is a wet method synthesis reactor structure positive view;
Fig. 2 is an agitator lifting device structure schematic diagram;
The specific embodiment:
The utility model further specifies as follows in conjunction with specific embodiments referring to accompanying drawing.
The wet method synthesis reactor, referring to accompanying drawing 1, it is that guide shell 2 is installed in drum shaped reaction groove 1, connect firmly long bolt 5 on guide shell 2 outer walls, long bolt 5 upper ends are loaded on reactive tank 1 top cover 6 through nut, can regulate on the guide shell, upper/lower positions, guide shell 2 outer walls with connect firmly on reactive tank 1 cylindrical wall several uniform suspended wall 3 through Bolt Connection, Bolt Connection connects hole 4 for vertically to strip hole, be convenient to, downward modulation is stream tube position successively, agitator 7 passes guide shell 2, and the impeller shaft of agitator 7 upper end connects with lowering or hoisting gear 8 on reactive tank 1 top cover 6, can regulate agitator 7 on, upper/lower positions.Agitator 7 connects through coupling sleeve 10 and bearing 11 with frequency control motor 9, can regulate agitator 7 mixing speeds.Speed adjustable range is 100rpm-300rpm.
Lowering or hoisting gear 8, referring to accompanying drawing 2, it is made up of worm-and-wheel gear and pinion and rack, and worm-and-wheel gear is installed on the gear-box of installing on reactive tank 1 top cover 6 20, and the worm gear pole 17 that ribbon gymnastics is made handle is the action bars of regulating agitator 7 liftings.Worm gear 18 and gear 16 engagements, gear 16 and tooth bar 19 engagements, tooth bar 19 connects firmly on coupling sleeve 10, is integrated, and coupling sleeve 10 connects with agitator 7 impeller shafts through bearing 11.
The shelves stream plate 12 of some settings of circumference uniform distribution on the reactive tank 1 drum inwall is referring to accompanying drawing 1.
Around reactive tank 1 cylinder heater 13 is installed outward, heater 13 is that electric heating coil and heat-insulation layer are formed, and is close to the cell wall shell, and compact dimensions does not account for volume, and is convenient to regulate temperature, insulation and heat exchange.
Among Fig. 1,14 is overfall, and 15 is underflow opening.
The utility model wet method synthesis reactor, its guide shell upper/lower terminal is uncovered, and the guide shell position can upper and lowerly be regulated, agitator speed can be regulated and the position is upper and lower regulates, the coupling of both relative altitude positions cooperates with the shelves stream plate of reactive tank in addition, can make the solution in the reactive tank form the circulation turbulent flow in reactive tank, fully reaction reaches the reaction optimum state.Thereby can control different reaction conditions, obtain the compound of different grain size and form.
In sum, the utility model wet method synthesis reactor advantage is as follows: (1) adapts to the synthetic reaction of multiple metal and compound; (2) can design different reaction conditions according to user's needs; (3) in the Granularity Distribution range set that obtains, clustering phenomena do not occur, dispersive property is good; (4) can control temperature, agitation speed and the stirring mode of reaction simultaneously, obtain the powder body material or the nano material of required product granularity and shape.
Claims (3)
1, wet method synthesis reactor mainly by in the drum shaped reaction groove guide shell, agitator and transmission device thereof being housed, being equipped with heater outward around reactive tank and forming, and it is characterized in that:
(1) the guide shell upper/lower terminal is uncovered, is loaded in the reactive tank via coupling mechanism that can upper and lower adjusting position;
(2) agitator is loaded on reactive tank drum top via lowering or hoisting gear; Agitator connects with buncher is coaxial;
(3) on the reactive tank drum inwall, the shelves stream plate of some settings of circumference uniform distribution;
(4) heater is that electric heating coil and heat-insulation layer are formed.
2, wet method synthesis reactor according to claim 1, it is characterized in that the agitator lowering or hoisting gear is made up of worm gear snail pavilion mechanism and pinion and rack, worm-and-wheel gear is installed on the gear-box of reactive tank top cover, the worm screw that ribbon gymnastics is made handle is agitator lift adjustment action bars, worm gear and gears engaged, the wheel and rack engagement, tooth bar is connected on the coupling sleeve of agitator.
3, wet method synthesis reactor according to claim 1, the coupling mechanism that it is characterized in that its guide shell and reactive tank is to connect firmly long bolt on the guide shell outer wall, the upper end is loaded on the reactive tank top cover through nut, the guide shell outer wall with connect firmly on the reactive tank cylindrical wall several uniform cantilevers through Bolt Connection, the Bolt Connection hole is for vertically to strip hole.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN 200420069474 CN2768892Y (en) | 2004-12-20 | 2004-12-20 | Wet synthetic reactor |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN 200420069474 CN2768892Y (en) | 2004-12-20 | 2004-12-20 | Wet synthetic reactor |
Publications (1)
Publication Number | Publication Date |
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CN2768892Y true CN2768892Y (en) | 2006-04-05 |
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Family Applications (1)
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CN 200420069474 Expired - Fee Related CN2768892Y (en) | 2004-12-20 | 2004-12-20 | Wet synthetic reactor |
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Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102974248A (en) * | 2012-11-30 | 2013-03-20 | 大连隆星新材料有限公司 | Stirring device for chemical materials |
CN103285767A (en) * | 2013-05-31 | 2013-09-11 | 芜湖精英新型建材有限公司 | Stirrer structure |
CN104493992A (en) * | 2014-12-09 | 2015-04-08 | 广东新志密封技术有限公司 | Polytetrafluoroethylene high-speed mixing method and equipment |
CN106402383A (en) * | 2016-11-18 | 2017-02-15 | 安徽中研理工仪器设备有限公司 | High pressure vessel sealing method |
CN107024375A (en) * | 2017-06-05 | 2017-08-08 | 辽东学院 | A kind of portable sample analyzer front processor and application method |
CN108380087A (en) * | 2018-04-20 | 2018-08-10 | 四川省机械研究设计院 | A kind of self-adapted high-efficient diving mixing agitator |
-
2004
- 2004-12-20 CN CN 200420069474 patent/CN2768892Y/en not_active Expired - Fee Related
Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102974248A (en) * | 2012-11-30 | 2013-03-20 | 大连隆星新材料有限公司 | Stirring device for chemical materials |
CN103285767A (en) * | 2013-05-31 | 2013-09-11 | 芜湖精英新型建材有限公司 | Stirrer structure |
CN104493992A (en) * | 2014-12-09 | 2015-04-08 | 广东新志密封技术有限公司 | Polytetrafluoroethylene high-speed mixing method and equipment |
CN106402383A (en) * | 2016-11-18 | 2017-02-15 | 安徽中研理工仪器设备有限公司 | High pressure vessel sealing method |
CN107024375A (en) * | 2017-06-05 | 2017-08-08 | 辽东学院 | A kind of portable sample analyzer front processor and application method |
CN108380087A (en) * | 2018-04-20 | 2018-08-10 | 四川省机械研究设计院 | A kind of self-adapted high-efficient diving mixing agitator |
CN108380087B (en) * | 2018-04-20 | 2023-09-26 | 四川省机械研究设计院(集团)有限公司 | Self-adaptive efficient submersible mixing stirrer |
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C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
C19 | Lapse of patent right due to non-payment of the annual fee | ||
CF01 | Termination of patent right due to non-payment of annual fee |