CN1994548A - Fluid driven impeller stirred reactor - Google Patents

Fluid driven impeller stirred reactor Download PDF

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Publication number
CN1994548A
CN1994548A CN 200610069999 CN200610069999A CN1994548A CN 1994548 A CN1994548 A CN 1994548A CN 200610069999 CN200610069999 CN 200610069999 CN 200610069999 A CN200610069999 A CN 200610069999A CN 1994548 A CN1994548 A CN 1994548A
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CN
China
Prior art keywords
stirred reactor
fluid driven
impeller
kinetic pump
driven impeller
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.)
Pending
Application number
CN 200610069999
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Chinese (zh)
Inventor
陈罘杲
刘景春
何秀英
Original Assignee
陈罘杲
刘景春
何秀英
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by 陈罘杲, 刘景春, 何秀英 filed Critical 陈罘杲
Priority to CN 200610069999 priority Critical patent/CN1994548A/en
Publication of CN1994548A publication Critical patent/CN1994548A/en
Pending legal-status Critical Current

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Abstract

The invention relates to a fluid driving blade wheel mixing reactor, which comprises reaction container, power pump, liquid inlet tube connected to the inlet of power pump, liquid outlet tube connected to the outlet of power pump, and mixer in the container, wherein the invention is characterized in that: the mixer is formed by blade wheel and wheel axle; the blade wheel via wheel axle is fixed in container; the area near the blade wheel has ejection tube. Compared with present technique, the invention has simple structure and easy operation.

Description

Fluid driven impeller stirred reactor
Affiliated technical field
The present invention relates to a kind of reaction unit, particularly adopt kinetic pump to make fluid driven impeller stirred reactor.
Background technology
At present, the chemical reaction equipment on the market is a lot, and the technical method that its structure generally adopts motor to combine with stirring rod comprises magnetic stirring apparatus that agitator that motor combines with blade and motor combine with magnetic field etc.These agitating devices in use must place the material rotation to reach the purpose of stirring stirring rod or stirring vane and magnetic force rotor.Find during use: there are many weak points in the agitating device in the background technology: the one, and stirring needed rotating speed generally will be on the 60-120 right side of turning left, and present speed adjusting technique mostly adopts the speed regulating method of decelerator and RHVC, equipment cost is increased more than 1/2nd, make the complete machine price reach 5000-30000 unit (1.1KW); The 2nd, operation inconvenience must be put into agitator after each production technology is finished after proposing to clean from charging basket, cause production efficiency low; The 3rd, mixing time is long, and production cost is strengthened; The 4th, complex structure installation and maintenance inconvenience; The 5th, rotation mixing direction unanimity can't be adjusted the Combination of material and stirring intensity.
Summary of the invention
Technical assignment of the present invention is to provide a kind of fluid driven impeller stirred reactor at above the deficiencies in the prior art, and this device has characteristics such as simple in structure, easy to operate, with low cost.
The technical solution adopted for the present invention to solve the technical problems is: fluid driven impeller stirred reactor, comprise reaction vessel, kinetic pump, the feed tube that is connected with the kinetic pump inlet, drain pipe that is connected with the kinetic pump outlet and the agitating device that is arranged on internal tank, be characterized in that this agitating device is made of impeller and wheel shaft, impeller is fixed in the container by wheel shaft, is provided with jet pipe in the zone near impeller.
Be provided with the wheel oar at an end that connects impeller.
On reaction vessel, be provided with 1-5 liquid outlet, and be connected in series with jet pipe by pipeline.
Described pipeline is connected with the liquid outlet of kinetic pump by drain pipe with the common port of jet pipe.
On described feed tube, be provided with the feed liquor valve, on the feed tube between feed liquor valve and the kinetic pump inlet, be provided with feed pipe, on feed pipe, be provided with inlet valve.
Described device is arranged on the flat board that has carriage
During use, material forms the vortex flow rotation in reaction vessel under the effect of kinetic pump, and jet pipe liquid stream drives impeller is rotated simultaneously, reaches the purpose of impeller and the dual stirring of eddy current.
The present invention compared with prior art has following beneficial effect:
1, material rotation mixing direction is inconsistent, makes stirring more abundant, and mixing time is short, has improved operating efficiency, has reduced cost;
2, simple in structure, maintenance is convenient.
Description of drawings
Fig. 1 is the embodiment of the invention one an overall structure schematic diagram.
Fig. 2 is the embodiment of the invention two overall structure schematic diagrames.
The specific embodiment
Now in conjunction with the present invention is done following detailed explanation.
Embodiment one: as shown in Figure 1, fluid driven impeller stirred reactor, comprise reaction vessel (1), kinetic pump (2), the feed tube (11) that is connected with kinetic pump (2) inlet (21), drain pipe (12) that is connected with kinetic pump (2) outlet (22) and the agitating device (3) that is arranged on container (1) inside, its structure is that this agitating device (3) is made of impeller (31) and wheel shaft (32), impeller (31) is fixed in the container (1) by wheel shaft (32), is provided with jet pipe (13) in the zone near impeller (31).Can be provided with wheel oar (33) at an end that connects impeller (31) in order to increase stirring intensity.On reaction vessel (1), be provided with 1-5 liquid outlet (14), and be connected in series with jet pipe (13) by pipeline (15).Pipeline (15) is connected with the outlet (22) of kinetic pump (2) by drain pipe (12) with the common port of jet pipe (13).On feed tube (11), be provided with feed liquor valve (111), on the feed tube (11) between feed liquor valve (11) and kinetic pump (2) inlet (21), be provided with feed pipe (16), on feed pipe (16), be provided with inlet valve (161).Reaction vessel (1) can be circular or square or other shapes, and that kinetic pump (2) can adopt is centrifugal, self-priming, injecting type, heat-resistant anticorrosive pump such as reciprocating type.For flexible operation, convenient moving used, and reaction unit can be located on the flat board (4) that has carriage (41).
During use, close inlet valve (161), material is under the effect of kinetic pump (2), from feed tube (11) process kinetic pump (2), drain pipe (12), at this moment, part material is got back in the container (1) by pipeline (15), liquid outlet (14), and another part penetrates liquid stream by jet pipe (13), impeller (31) rotates under the driving of liquid stream, by in reaction vessel (1), forming the vortex flow rotation, drives impeller (31) is rotated simultaneously, reaches the purpose of impeller (31) and the dual stirring of eddy current.When needs feed in raw material, to close feed liquor valve (111) and open inlet valve (161), material enters reaction vessel (1) under the effect of kinetic pump (2).
Embodiment two: as shown in Figure 2, agitating device (3) can be horizontally installed on the chamber wall, and jet pipe (13) also correspondingly is located at the near zone of impeller (31).Its operation principle and connected mode thereof are identical with embodiment one.

Claims (7)

1, fluid driven impeller stirred reactor, comprise reaction vessel (1), kinetic pump (2), the feed tube (11) that is connected with kinetic pump (2) inlet (21), drain pipe (12) that is connected with kinetic pump (2) outlet (22) and the agitating device (3) that is arranged on container (1) inside, it is characterized in that this agitating device (3) is made of impeller (31) and wheel shaft (32), impeller (31) is fixed in the container (1) by wheel shaft (32), is provided with jet pipe (13) in the zone near impeller (31).
2, fluid driven impeller stirred reactor according to claim 1 is characterized in that: be provided with wheel oar (33) at an end that connects impeller (31).
3, fluid driven impeller stirred reactor according to claim 1 is characterized in that: be provided with liquid outlet (14) on reaction vessel (1), and be connected in series with jet pipe (13) by pipeline (15).
4, fluid driven impeller stirred reactor according to claim 3 is characterized in that: described pipeline (15) is connected with the outlet (22) of kinetic pump (20) by drain pipe (12) with the common port of jet pipe (13).
5, fluid driven impeller stirred reactor according to claim 3 is characterized in that: described liquid outlet (14) is 1-10.
6, fluid driven impeller stirred reactor according to claim 1, it is characterized in that: on described feed tube (11), be provided with feed liquor valve (111), on the feed tube (11) between feed liquor valve (111) and kinetic pump (2) inlet (21), be provided with feed pipe (16), on feed pipe (16), be provided with inlet valve (161).
7, fluid driven impeller stirred reactor according to claim 1 is characterized in that: described device is arranged on the flat board (4) that has carriage (41).
CN 200610069999 2006-11-15 2006-11-15 Fluid driven impeller stirred reactor Pending CN1994548A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN 200610069999 CN1994548A (en) 2006-11-15 2006-11-15 Fluid driven impeller stirred reactor

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN 200610069999 CN1994548A (en) 2006-11-15 2006-11-15 Fluid driven impeller stirred reactor

Publications (1)

Publication Number Publication Date
CN1994548A true CN1994548A (en) 2007-07-11

Family

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Family Applications (1)

Application Number Title Priority Date Filing Date
CN 200610069999 Pending CN1994548A (en) 2006-11-15 2006-11-15 Fluid driven impeller stirred reactor

Country Status (1)

Country Link
CN (1) CN1994548A (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102174366A (en) * 2011-01-10 2011-09-07 李明忠 Clean energy-saving bioreactor
CN102226293A (en) * 2011-06-03 2011-10-26 宁波大学 Two-bath cooling method crystal breeding device with modified inner bath structure
CN102230214A (en) * 2011-06-03 2011-11-02 宁波大学 Double-bath cooling method crystal cultivating device with adoption of stirring technology with better structure matching property
CN104257271A (en) * 2014-09-01 2015-01-07 广东新宝电器股份有限公司 Stirring device driven by fluid
CN111254421A (en) * 2020-01-18 2020-06-09 信泰电子(西安)有限公司 Online concentration analysis medicine system

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102174366A (en) * 2011-01-10 2011-09-07 李明忠 Clean energy-saving bioreactor
CN102226293A (en) * 2011-06-03 2011-10-26 宁波大学 Two-bath cooling method crystal breeding device with modified inner bath structure
CN102230214A (en) * 2011-06-03 2011-11-02 宁波大学 Double-bath cooling method crystal cultivating device with adoption of stirring technology with better structure matching property
CN102230214B (en) * 2011-06-03 2014-04-30 宁波大学 Double-bath cooling method crystal cultivating device with adoption of stirring technology with better structure matching property
CN104257271A (en) * 2014-09-01 2015-01-07 广东新宝电器股份有限公司 Stirring device driven by fluid
CN111254421A (en) * 2020-01-18 2020-06-09 信泰电子(西安)有限公司 Online concentration analysis medicine system

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Open date: 20070711