CN203990591U - A kind of reactor - Google Patents

A kind of reactor Download PDF

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Publication number
CN203990591U
CN203990591U CN201420297737.XU CN201420297737U CN203990591U CN 203990591 U CN203990591 U CN 203990591U CN 201420297737 U CN201420297737 U CN 201420297737U CN 203990591 U CN203990591 U CN 203990591U
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CN
China
Prior art keywords
tank body
gas
chamber
heat
reactor
Prior art date
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.)
Expired - Fee Related
Application number
CN201420297737.XU
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Chinese (zh)
Inventor
白荣誉
雷克微
卢琼
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Ningbo University
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Ningbo University
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Publication date
Application filed by Ningbo University filed Critical Ningbo University
Priority to CN201420297737.XU priority Critical patent/CN203990591U/en
Application granted granted Critical
Publication of CN203990591U publication Critical patent/CN203990591U/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Abstract

The utility model discloses a kind of reactor, by pressue device (as air pump etc.), gas compression is become to gases at high pressure, importing in plenum chamber by pipeline, plenum chamber is extruded the rotation of driven rotary wheel body by pore by gas, in the paddle rotation driving by rotating shaft in tank body, thereby stirring body liquor, simultaneously when in the time that tank body needs gas, by valve regulated conducting plenum chamber and tank body; In the time that tank body needs gas, by valve, gas is discharged in air, depart from traditional motor and driven stirring, utilizing gases at high pressure to drive stirs, can provide gas for the reaction that needs gas simultaneously simultaneously, simplified the structure of reactor, the while has effectively been avoided the problems such as the convenience of spring bearing materials'use life problems and dismounting.

Description

A kind of reactor
Technical field
The utility model relates to a kind of reactor technical field, specifically a kind of reactor.
Background technology
In the reactor of lab scale and pilot-scale, from document, can retrieve various stirring systems, as Gas Stirring, mechanical agitation system etc., mechanical agitation system has the directly mechanical agitation system of the connected magnetic drives separating with motor with axle of motor and shaft.Motor is directly connected with shaft, relates to the movable sealing problem of axle and reactor, because heatproof, the withstand voltage properties etc. of encapsulant make such reactor especially in the possibility that has leakage and microbiological contamination at aspects such as microorganism cultivations.And in the mechanical agitation system of magnetic drives, the sealing of axle and reactor adopts static seal, reduce like this possibility that has leakage and microbiological contamination at aspects such as microorganism cultivations.In the mechanical agitation system of magnetic drives, existing both-end supports, but the magnetic agitation system that both-end supports exists the problems such as the convenience of apical support bearing material problem in service life and dismounting to overcome.
Conventional desk-top reactor is simple and easy for pursuing, and often adopts the direct Electric heating of water leg at the heating part of temperature-controlling system, and cooling segment adopts the running water type of cooling, therefore controls and lags, and dynamic fluctuation is large, low precision, and also running water consumption is large.More have for Simple Design, adopt immersion heater mode.Therefore cause the inequality of being heated finally all can have influence on process result.
Utility model content
The purpose of this utility model is to provide a kind of reactor, to solve the problem proposing in above-mentioned background technology.
For achieving the above object, the utility model provides following technical scheme:
A kind of reactor, comprise tank body, described tank body top is provided with lid, lid is provided with the second exhaust pipe road that runs through lid, second exhaust pipe is nested with condenser outside road, described tank base is provided with heat-exchanging chamber, heat-exchanging chamber middle part is provided with a rotating shaft that runs through tank body and heat-exchanging chamber, one end that described rotating shaft is arranged in tank body is connected with paddle, under described paddle, be provided with nozzle chamber, nozzle chamber is provided with some air nozzles, the other end of described rotating shaft connects rotary wheel, described rotary wheel is just being transferred and is being provided with flow pad, one side of flow pad is provided with pore, flow pad below is provided with plenum chamber and is communicated with by pore, described plenum chamber connects pressue device by the pipeline of bottom, on described rotary wheel and between heat-exchanging chamber, be provided with downtake pipe road, the admission line that described nozzle chamber connects is connected by valve with downtake pipe road, one side of described heat-exchanging chamber is provided with water inlet pipe and outlet pipe.
As further program of the utility model: described rotary wheel is provided with blade, and blade and horizontal plane are in angle of 45 degrees.
As further program of the utility model: described second exhaust pipe road is bend pipe.
Compared with prior art, the beneficial effects of the utility model are: by pressue device (as air pump etc.), gas compression is become to gases at high pressure, importing in plenum chamber by pipeline, plenum chamber is extruded the rotation of driven rotary wheel body by pore by gas, in the paddle rotation driving by rotating shaft in tank body, thereby stirring body liquor, simultaneously when in the time that tank body needs gas, by valve regulated conducting plenum chamber and tank body; In the time that tank body needs gas, by valve, gas is discharged in air, depart from traditional motor and driven stirring, utilizing gases at high pressure to drive stirs, can provide gas for the reaction that needs gas simultaneously simultaneously, simplified the structure of reactor, the while has effectively been avoided the problems such as the convenience of spring bearing materials'use life problems and dismounting.
Brief description of the drawings
Fig. 1 is structural representation of the present utility model.
In figure: downtake pipe road 1, admission line 2, valve 3, air nozzle 4, paddle 5, tank body 6, lid 7, second exhaust pipe road 8, condenser 9, nozzle chamber 10, heat-exchanging chamber 11, water inlet pipe 12, outlet pipe 13, rotating shaft 14, pore 15, plenum chamber 16, flow pad 17, rotary wheel 18.
Detailed description of the invention
Below in conjunction with the accompanying drawing in the utility model embodiment, the technical scheme in the utility model embodiment is clearly and completely described, obviously, described embodiment is only the utility model part embodiment, instead of whole embodiment.Based on the embodiment in the utility model, those of ordinary skill in the art are not making the every other embodiment obtaining under creative work prerequisite, all belong to the scope of the utility model protection.
Refer to Fig. 1, in the utility model embodiment, a kind of reactor, comprise tank body 6, described tank body 6 tops are provided with lid 7, lid 7 is provided with the second exhaust pipe road 8 that runs through lid 7 and is used for getting rid of the gas of tank body 6 interior evaporations, described second exhaust pipe road 8 is that bend pipe is so that condensation of gas, second exhaust pipe road 8 is outer is nested with condenser 9 in order to by cooling the steam in boil-off gas, thereby flow backwards back reactor, described tank body 6 bottoms are provided with heat-exchanging chamber 11, heat-exchanging chamber 11 middle parts are provided with a rotating shaft 14 that runs through tank body 6 and heat-exchanging chamber 11, one end that described rotating shaft 14 is arranged in tank body 6 is connected with paddle 5, under described paddle 5, be provided with nozzle chamber 10, nozzle chamber 10 is provided with some air nozzles 4, the other end of described rotating shaft 14 connects rotary wheel 18, described rotary wheel 18 is just being transferred and is being provided with flow pad 17, one side of flow pad 17 is provided with pore 15, flow pad 17 belows are provided with plenum chamber 16 and are communicated with by pore 15, described plenum chamber 16 connects pressue device by the pipeline of bottom.
Further, on described rotary wheel 18 and between heat-exchanging chamber 11, be provided with downtake pipe road 1, the admission line 2 that described nozzle chamber 10 connects is connected by valve 3 with downtake pipe road 1, in the time that tank body 6 needs gas, regulates conducting plenum chamber 16 and tank body 6 by valve 3; In the time that tank body 6 needs gas, by valve 3, gas is discharged in air.
Further, a side of described heat-exchanging chamber 11 is provided with water inlet pipe 12 and outlet pipe 13, when tank body 6 needs heating, cooling and when insulation, by heat, cold-peace Warm water circulation, reaches the object of temperature adjusting.
Further, described rotary wheel 18 is provided with blade, and blade and horizontal plane are in angle of 45 degrees, so that gas drives.
Operation principle of the present utility model is: by pressue device (as air pump etc.), gas compression is become to gases at high pressure, importing by pipeline in plenum chamber 16, plenum chamber 16 is extruded driven rotary wheel body 18 by pore 15 by gas and is rotated, driving the paddle 5 in tank body 6 to rotate by rotating shaft 14, thereby stirring body liquor, when in the time that tank body 6 needs gas, regulate conducting plenum chamber 16 and tank body 6 by valve 3 simultaneously; In the time that tank body 6 needs gas, by valve 3, gas is discharged in air, depart from traditional motor and driven stirring, utilizing gases at high pressure to drive stirs, can provide gas for the reaction that needs gas simultaneously simultaneously, simplified the structure of reactor, the while has effectively been avoided the problems such as the convenience of spring bearing materials'use life problems and dismounting.
To those skilled in the art, obviously the utility model is not limited to the details of above-mentioned example embodiment, and in the situation that not deviating from spirit of the present utility model or essential characteristic, can realize the utility model with other concrete form.Therefore, no matter from which point, all should regard embodiment as exemplary, and be nonrestrictive, scope of the present utility model is limited by claims instead of above-mentioned explanation, is therefore intended to all changes that drop in the implication and the scope that are equal to important document of claim to include in the utility model.Any Reference numeral in claim should be considered as limiting related claim.
In addition, be to be understood that, although this description is described according to embodiment, but be not that each embodiment only comprises an independently technical scheme, this narrating mode of description is only for clarity sake, those skilled in the art should make description as a whole, and the technical scheme in each embodiment also can, through appropriately combined, form other embodiments that it will be appreciated by those skilled in the art that.

Claims (3)

1. a reactor, comprise tank body, it is characterized in that, described tank body top is provided with lid, lid is provided with the second exhaust pipe road that runs through lid, second exhaust pipe is nested with condenser outside road, described tank base is provided with heat-exchanging chamber, heat-exchanging chamber middle part is provided with a rotating shaft that runs through tank body and heat-exchanging chamber, one end that described rotating shaft is arranged in tank body is connected with paddle, under described paddle, be provided with nozzle chamber, nozzle chamber is provided with some air nozzles, the other end of described rotating shaft connects rotary wheel, described rotary wheel is just being transferred and is being provided with flow pad, one side of flow pad is provided with pore, flow pad below is provided with plenum chamber and is communicated with by pore, described plenum chamber connects pressue device by the pipeline of bottom, on described rotary wheel and between heat-exchanging chamber, be provided with downtake pipe road, the admission line that described nozzle chamber connects is connected by valve with downtake pipe road, one side of described heat-exchanging chamber is provided with water inlet pipe and outlet pipe.
2. a kind of reactor according to claim 1, is characterized in that, described rotary wheel is provided with blade, and blade and horizontal plane are in angle of 45 degrees.
3. a kind of reactor according to claim 1, is characterized in that, described second exhaust pipe road is bend pipe.
CN201420297737.XU 2014-05-29 2014-05-29 A kind of reactor Expired - Fee Related CN203990591U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201420297737.XU CN203990591U (en) 2014-05-29 2014-05-29 A kind of reactor

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Application Number Priority Date Filing Date Title
CN201420297737.XU CN203990591U (en) 2014-05-29 2014-05-29 A kind of reactor

Publications (1)

Publication Number Publication Date
CN203990591U true CN203990591U (en) 2014-12-10

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Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106040153A (en) * 2016-06-30 2016-10-26 惠州市格雷戈里科技有限公司 Automatic stirring equipment
CN107175047A (en) * 2017-07-11 2017-09-19 南通协鑫热熔胶有限公司 A kind of autoclave steam retracting device
CN108160012A (en) * 2017-12-21 2018-06-15 海南汉地阳光石油化工有限公司 A kind of cold hydrogen box for reactor temperature control
CN117486349A (en) * 2023-12-29 2024-02-02 安徽皖欣环境科技有限公司 Novel high concentration chemical wastewater wet oxidation device

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106040153A (en) * 2016-06-30 2016-10-26 惠州市格雷戈里科技有限公司 Automatic stirring equipment
CN107175047A (en) * 2017-07-11 2017-09-19 南通协鑫热熔胶有限公司 A kind of autoclave steam retracting device
CN108160012A (en) * 2017-12-21 2018-06-15 海南汉地阳光石油化工有限公司 A kind of cold hydrogen box for reactor temperature control
CN108160012B (en) * 2017-12-21 2020-11-13 海南汉地阳光石油化工有限公司 Cold hydrogen box for reactor temperature control
CN117486349A (en) * 2023-12-29 2024-02-02 安徽皖欣环境科技有限公司 Novel high concentration chemical wastewater wet oxidation device
CN117486349B (en) * 2023-12-29 2024-04-02 安徽皖欣环境科技有限公司 Wet oxidation device for high-concentration chemical wastewater

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Date Code Title Description
C14 Grant of patent or utility model
GR01 Patent grant
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20141210

Termination date: 20170529

CF01 Termination of patent right due to non-payment of annual fee