CN202570171U - Double-layer warming air-adding stirring reaction kettle - Google Patents
Double-layer warming air-adding stirring reaction kettle Download PDFInfo
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- CN202570171U CN202570171U CN 201220269949 CN201220269949U CN202570171U CN 202570171 U CN202570171 U CN 202570171U CN 201220269949 CN201220269949 CN 201220269949 CN 201220269949 U CN201220269949 U CN 201220269949U CN 202570171 U CN202570171 U CN 202570171U
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Abstract
The utility model discloses a double-layer warming air-adding stirring reaction kettle which is composed of a motor, a reducer, a magnetic sealing device, an air inlet pipe, a stirring rod, an air discharging pie, a heat transfer coil pipe, a middle air exhausting disc, a spiral plate clamping pipe, a stirring blade, a bottom air exhausting disc, a heat transfer coil pipe heat outlet pipe, a spiral plate clamping pipe heat outlet pipe, a discharging pipe, a central fixing shaft, a heat transfer coil pipe heat inlet pipe, a spiral plate clamping pipe heat inlet pipe, a kettle body and a feeding pipe. Due to the fact that a double-layer heating device of the spiral plate clamping pipe and the heat transfer coil pipe is adopted, and the bottom air exhausting disc and the middle air exhausting disc with a plurality of air outlets are arranged on the stirring rod, the double-layer warming air-adding stirring reaction kettle has the advantages that a kettle body is heated evenly, the internal heat transfer coil pipe can increase material temperature fast, heated time is shortened, heat energy is saved, and reaction is complete and thorough due to the fact that gas is injected in scattered mode.
Description
Technical field
The utility model relates to the technical field of agitated reactor, especially refers to a kind of bilayer aerating stirred autoclave of heating.
Background technology
Agitated reactor is the rustless steel container of physics or chemical reaction; Be widely used in the research of type of production users such as oil, chemical industry, rubber, agricultural chemicals, dyestuff, medicine, food and various scientific experiment projects, be used for accomplishing the container of technical process such as hydrolysis, neutralization, crystallization, distillation, evaporation, storage, hydrogenation, hydrocarbonylation, polymerization, condensation, heating are mixed, isothermal reaction; Traditional agitated reactor is in the aerating course of reaction, and it is simple to exist aerating method, and it is not enough that gas disperses in agitated reactor, and the interlayer of agitated reactor heats and put forward heat and exist kettle temperature is inconsistent up and down, and the reaction time is long, the defective that wastes energy.
Summary of the invention
A kind of bilayer of the utility model aerating stirred autoclave of heating; Can solve the deficiency of said technology; Adopt the double-deck heater of spiral plate clamp and heat exchange coil; And bottom air dipelling disk and the middle part air dipelling disk with a plurality of ventholes is set on puddler, realize the purpose of the outside evenly temperature raising of kettle, the even aerating stirring reaction of inner Fast Heating and center.
To achieve these goals, technical solution of the present invention is: a kind of bilayer aerating stirred autoclave of heating comprises that going out heat pipe, spiral plate clamp by motor, decelerator, magnetic seal device, air inlet pipe, puddler, blast pipe, heat exchange coil, middle part air dipelling disk, spiral plate clamp, stirring vane, bottom air dipelling disk, heat exchange coil goes out heat pipe, discharge nozzle, central fixed shaft, heat exchange coil and advance heat pipe, spiral plate clamp and advance heat pipe, kettle, feed pipe and form; Feed pipe is set on kettle top and the center decelerator is connected with kettle by the magnetic seal device with motor; The kettle interlayer is provided with the spiral plate clamp, and the kettle inboard is provided with heat exchange coil, and the outside side of kettle is provided with that the spiral plate clamp advances heat pipe and heat exchange coil advances heat pipe, opposite side is provided with blast pipe; The kettle bottom is provided with discharge nozzle, heat exchange coil goes out heat pipe and the spiral plate clamp goes out heat pipe; The puddler that the kettle inside center is provided with the band breather pipe is connected with decelerator; Insert in the central fixed shaft its bottom; Puddler sets gradually bottom air dipelling disk, stirring vane and middle part air dipelling disk from the bottom, the bottom air dipelling disk is provided with a plurality of ventholes with the middle part air dipelling disk and is connected with the breather pipe of puddler; Air inlet pipe extends to the bottom by the entering of kettle top along inwall and is connected with the breather pipe of puddler.
The utility model beneficial effect is: can effectively stratification of hot gas be injected in the material that is stirred through the middle part air dipelling disk that is provided with on the puddler and bottom air dipelling disk and go, have scattered advantage; The spiral plate clamp of kettle interlayer setting can make the kettle thermally equivalent, and inner heat exchange coil can improve temperature of charge rapidly, shortens heated time and practices thrift heat energy.
Description of drawings
Below in conjunction with the accompanying drawing and the specific embodiment utility model is further described.
Accompanying drawing is a kind of bilayer aerating stirred autoclave sketch map of heating.
Among the figure: 1, motor, 2, decelerator, 3, the magnetic seal device, 4, air inlet pipe, 5, puddler; 6, blast pipe, 7, heat exchange coil, 8, the middle part air dipelling disk, 9, the spiral plate clamp, 10, stirring vane; 11, bottom air dipelling disk, 12, heat exchange coil goes out heat pipe, 13, the spiral plate clamp goes out heat pipe, 14, discharge nozzle; 15, central fixed shaft, 16, heat exchange coil advances heat pipe, 17, the spiral plate clamp advances heat pipe, 18, kettle, 19, feed pipe.
The specific embodiment
Shown in accompanying drawing, a kind of bilayer aerating stirred autoclave of heating comprises by loose gas 8 dishes, spiral plate clamp 9, stirring vane 10, bottom air dipelling disk 11, heat exchange coil of motor 1, decelerator 2, magnetic seal device 3, air inlet pipe 4, puddler 5, blast pipe 6, heat exchange coil 7, middle part going out heat pipe 12, spiral plate clamp and going out heat pipe 13, discharge nozzle 14, central fixed shaft 15, heat exchange coil and advance heat pipe 16, spiral plate clamp and advance heat pipe 17, kettle 18, feed pipe 19 and form; Feed pipe 19 is set on kettle 18 tops and center decelerator 2 is connected with kettle 18 by magnetic seal device 3 with motor 1; The interlayer of kettle 18 is provided with spiral plate clamp 9, and kettle 18 inboards are provided with heat exchange coil 7, and kettle 18 outside sides are provided with the spiral plate clamp and advance that heat pipe 17 advances heat pipe 16 with heat exchange coil, opposite side is provided with blast pipe 6; Kettle 19 bottoms are provided with discharge nozzle 14, heat exchange coil goes out heat pipe 12 and the spiral plate clamp goes out heat pipe 13; The puddler 5 that kettle 18 inside center are provided with the band breather pipe is connected with decelerator 2; Insert in the central fixed shaft 15 its bottom; Puddler 5 sets gradually bottom air dipelling disk 11, stirring vane 10 and middle part air dipelling disk 8 from the bottom, bottom air dipelling disk 11 is provided with a plurality of ventholes with middle part air dipelling disk 8 and is connected with the breather pipe of puddler 5; Air inlet pipe 4 extends to the bottom by the entering of kettle 18 tops along inwall and is connected with the breather pipe of puddler 6.
During operation, add materials by feed pipe 19, evenly heated by 9 pairs of kettlies 18 of spiral plate clamp of kettle 18 interlayers, heat exchange coil 7 can carry out quick temperature raising to the materials in the kettle 18; During stirring reaction such as need material is carried out gasification reaction, can be by air inlet pipe 4 injecting gas, spill in the material through the venthole that is arranged on bottom air dipelling disk 11 and middle part air dipelling disk 8 on the puddler 5, make its reaction more fully with thoroughly; The residual air of reaction can be discharged from the blast pipe 6 on kettle 18 tops.
The above; Embodiment only is that preferred implementation of the present invention is described; Be not that scope of the present invention is limited; Under the prerequisite of the spirit that does not break away from the present invention's technology, various distortion and improvement that this area engineers and technicians make technical scheme of the present invention all should fall in the definite protection domain of claims of the present invention.
Claims (2)
1. bilayer aerating stirred autoclave of heating is characterized in that: go out heat pipe, spiral plate clamp by motor, decelerator, magnetic seal device, air inlet pipe, puddler, blast pipe, heat exchange coil, middle part air dipelling disk, spiral plate clamp, stirring vane, bottom air dipelling disk, heat exchange coil and go out heat pipe, discharge nozzle, central fixed shaft, heat exchange coil and advance heat pipe, spiral plate clamp and advance heat pipe, kettle, feed pipe and form; Feed pipe is set on kettle top and the center decelerator is connected with kettle by the magnetic seal device with motor; The kettle interlayer is provided with the spiral plate clamp, and the kettle inboard is provided with heat exchange coil, and the outside side of kettle is provided with that the spiral plate clamp advances heat pipe and heat exchange coil advances heat pipe, opposite side is provided with blast pipe; The kettle bottom is provided with discharge nozzle, heat exchange coil goes out heat pipe and the spiral plate clamp goes out heat pipe.
2. a kind of bilayer according to claim 1 aerating stirred autoclave of heating; It is characterized in that: the puddler that the kettle inside center is provided with the band breather pipe is connected with decelerator; Insert in the central fixed shaft its bottom; Puddler sets gradually bottom air dipelling disk, stirring vane and middle part air dipelling disk from the bottom, the bottom air dipelling disk is provided with a plurality of ventholes with the middle part air dipelling disk and is connected with the breather pipe of puddler; Air inlet pipe extends to the bottom by the entering of kettle top along inwall and is connected with the breather pipe of puddler.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201220269949 CN202570171U (en) | 2012-06-10 | 2012-06-10 | Double-layer warming air-adding stirring reaction kettle |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201220269949 CN202570171U (en) | 2012-06-10 | 2012-06-10 | Double-layer warming air-adding stirring reaction kettle |
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| Publication Number | Publication Date |
|---|---|
| CN202570171U true CN202570171U (en) | 2012-12-05 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN 201220269949 Expired - Fee Related CN202570171U (en) | 2012-06-10 | 2012-06-10 | Double-layer warming air-adding stirring reaction kettle |
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Cited By (15)
| Publication number | Priority date | Publication date | Assignee | Title |
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| CN103239913A (en) * | 2013-05-20 | 2013-08-14 | 张家港市振方化工有限公司 | Stirring and filtering device |
| CN103239881A (en) * | 2013-05-20 | 2013-08-14 | 张家港市振方化工有限公司 | Distillation device |
| CN103386291A (en) * | 2013-08-13 | 2013-11-13 | 广州利确节能科技有限公司 | Synergistic reactor for improving fuel gas energy of novel energy sources |
| CN103394418A (en) * | 2013-08-15 | 2013-11-20 | 蚌埠玻璃工业设计研究院 | Scrubbing, stewing and dipping machine |
| CN103861547A (en) * | 2014-03-31 | 2014-06-18 | 苏州润弘贸易有限公司 | Chemical reaction kettle |
| CN103861549A (en) * | 2014-03-31 | 2014-06-18 | 苏州润弘贸易有限公司 | Reaction kettle for producing scouring agent |
| CN103861543A (en) * | 2014-03-31 | 2014-06-18 | 苏州润弘贸易有限公司 | Reaction kettle for producing printing and dyeing auxiliary agent |
| CN103861548A (en) * | 2014-03-31 | 2014-06-18 | 苏州润弘贸易有限公司 | Printing and dyeing auxiliary production equipment |
| CN103894133A (en) * | 2014-03-24 | 2014-07-02 | 苏州润弘贸易有限公司 | Reaction device for printing and dyeing chemical industry |
| CN103894135A (en) * | 2014-03-24 | 2014-07-02 | 苏州润弘贸易有限公司 | Printing and dyeing chemical reaction kettle |
| CN103933918A (en) * | 2014-04-09 | 2014-07-23 | 陆曹生 | Reaction kettle |
| CN104001466A (en) * | 2014-03-24 | 2014-08-27 | 苏州润弘贸易有限公司 | Temperature-controllable refining agent reaction kettle |
| CN104383867A (en) * | 2014-11-05 | 2015-03-04 | 广州一翔农业技术有限公司 | Cyclic shearing reaction kettle of suspension liquid fertilizer |
| CN107824129A (en) * | 2017-12-04 | 2018-03-23 | 陕西盟创纳米新型材料股份有限公司 | A kind of drying system of alcohol supercritical methanol technology production aeroge |
| CN110227403A (en) * | 2019-06-14 | 2019-09-13 | 南京博源医药科技有限公司 | A kind of process units of β-D- galactolipin pentaacetate |
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2012
- 2012-06-10 CN CN 201220269949 patent/CN202570171U/en not_active Expired - Fee Related
Cited By (26)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103239913B (en) * | 2013-05-20 | 2015-03-25 | 张家港市振方化工有限公司 | Stirring and filtering device |
| CN103239881A (en) * | 2013-05-20 | 2013-08-14 | 张家港市振方化工有限公司 | Distillation device |
| CN103239913A (en) * | 2013-05-20 | 2013-08-14 | 张家港市振方化工有限公司 | Stirring and filtering device |
| CN103386291A (en) * | 2013-08-13 | 2013-11-13 | 广州利确节能科技有限公司 | Synergistic reactor for improving fuel gas energy of novel energy sources |
| CN103386291B (en) * | 2013-08-13 | 2015-09-02 | 广州利确节能科技有限公司 | A kind of enhanced reaction of modification device for promoting new energy gas energy |
| CN103394418A (en) * | 2013-08-15 | 2013-11-20 | 蚌埠玻璃工业设计研究院 | Scrubbing, stewing and dipping machine |
| CN103894133B (en) * | 2014-03-24 | 2015-12-23 | 苏州润弘贸易有限公司 | A kind of printing and dyeing chemical industry reaction unit |
| CN104001466B (en) * | 2014-03-24 | 2015-12-23 | 苏州润弘贸易有限公司 | Can the scouring agent reactor of temperature control |
| CN103894135B (en) * | 2014-03-24 | 2015-11-18 | 苏州润弘贸易有限公司 | A kind of printing and dyeing chemical reaction still |
| CN103894133A (en) * | 2014-03-24 | 2014-07-02 | 苏州润弘贸易有限公司 | Reaction device for printing and dyeing chemical industry |
| CN103894135A (en) * | 2014-03-24 | 2014-07-02 | 苏州润弘贸易有限公司 | Printing and dyeing chemical reaction kettle |
| CN104001466A (en) * | 2014-03-24 | 2014-08-27 | 苏州润弘贸易有限公司 | Temperature-controllable refining agent reaction kettle |
| CN103861543A (en) * | 2014-03-31 | 2014-06-18 | 苏州润弘贸易有限公司 | Reaction kettle for producing printing and dyeing auxiliary agent |
| CN103861549B (en) * | 2014-03-31 | 2016-02-10 | 苏州润弘贸易有限公司 | For the production of the reactor of scouring agent |
| CN103861543B (en) * | 2014-03-31 | 2016-09-21 | 苏州润弘贸易有限公司 | A kind of reactor for producing printing and dyeing assistant |
| CN103861547B (en) * | 2014-03-31 | 2016-02-10 | 苏州润弘贸易有限公司 | A kind of chemical reaction still |
| CN103861548A (en) * | 2014-03-31 | 2014-06-18 | 苏州润弘贸易有限公司 | Printing and dyeing auxiliary production equipment |
| CN103861549A (en) * | 2014-03-31 | 2014-06-18 | 苏州润弘贸易有限公司 | Reaction kettle for producing scouring agent |
| CN103861547A (en) * | 2014-03-31 | 2014-06-18 | 苏州润弘贸易有限公司 | Chemical reaction kettle |
| CN103861548B (en) * | 2014-03-31 | 2016-02-10 | 苏州润弘贸易有限公司 | Printing and dyeing assistant production equipment |
| CN103933918A (en) * | 2014-04-09 | 2014-07-23 | 陆曹生 | Reaction kettle |
| CN103933918B (en) * | 2014-04-09 | 2015-08-05 | 林鸿志 | A kind of reactor |
| CN104383867A (en) * | 2014-11-05 | 2015-03-04 | 广州一翔农业技术有限公司 | Cyclic shearing reaction kettle of suspension liquid fertilizer |
| CN107824129A (en) * | 2017-12-04 | 2018-03-23 | 陕西盟创纳米新型材料股份有限公司 | A kind of drying system of alcohol supercritical methanol technology production aeroge |
| CN107824129B (en) * | 2017-12-04 | 2024-03-12 | 陕西盟创纳米新型材料股份有限公司 | Drying system for producing aerogel by alcohol supercritical method |
| CN110227403A (en) * | 2019-06-14 | 2019-09-13 | 南京博源医药科技有限公司 | A kind of process units of β-D- galactolipin pentaacetate |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C17 | Cessation of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20121205 Termination date: 20130610 |