CN201189459Y - Toroidal swirl type pneumatic stirring device - Google Patents

Toroidal swirl type pneumatic stirring device Download PDF

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Publication number
CN201189459Y
CN201189459Y CNU2008201145718U CN200820114571U CN201189459Y CN 201189459 Y CN201189459 Y CN 201189459Y CN U2008201145718 U CNU2008201145718 U CN U2008201145718U CN 200820114571 U CN200820114571 U CN 200820114571U CN 201189459 Y CN201189459 Y CN 201189459Y
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CN
China
Prior art keywords
gas
stirring device
nozzle
horizontal plane
guide sleeves
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
CNU2008201145718U
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Chinese (zh)
Inventor
曹进富
刘建华
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
TANGSHAN CHEMICAL MACHINERY CO Ltd
Original Assignee
TANGSHAN CHEMICAL MACHINERY CO Ltd
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 TANGSHAN CHEMICAL MACHINERY CO Ltd filed Critical TANGSHAN CHEMICAL MACHINERY CO Ltd
Priority to CNU2008201145718U priority Critical patent/CN201189459Y/en
Application granted granted Critical
Publication of CN201189459Y publication Critical patent/CN201189459Y/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Abstract

The utility model relates to a stirring device, in particular to a rotational-flow type pneumatic stirring device, which comprises a gas transmission pipe, guiding pipes, nozzles and a gas-gathering flow divider. The gas transmission pipe is arranged on the gas-gathering flow divider; a plurality of guide sleeves are arranged on the outer sidewall of the gas-gathering flow divider; the guide sleeves are respectively connected with the guiding pipes; the other end of each guiding pipe is provided with a nozzle; and the horizontal plane where the nozzles position is lower than the horizontal plane where the guide sleeves position. The stirring device has the advantages of large mixing force, low power of non-motile mechanical components, low energy consumption, good stirring effect, adaptability for stirring solid-liquid materials easy to settle and thicken, as well as large applicable temperature range.

Description

The pneumatic agitating device of spiral-flow type
Technical field
The utility model relates to agitating device, the pneumatic agitating device of specifically a kind of spiral-flow type.
Background technology
Stirring operation is widely used in industries such as chemical industry, medicine, food, oil plant, its objective is make mixing of materials evenly, make gas in liquid phase, well disperse, make solid particle, powder in liquid phase, to suspend, make inconsistent another liquid phase evenly to suspend uniformly or fully emulsified, hardening constituent between mass transfer and augmentation of heat transfer etc.The realization of stirring is divided into mechanical agitation usually and air-flow stirs, mechanical agitation is by mechanical movement, driving mixing component rotates, it then is to utilize the gas bubbling that air-flow stirs, by liquid level liquid is produced stirring action, or the gas foam group rises by means of so-called gas lift effect promotion liquid generation convection circulation with high density state.Wherein: mechanical agitation must have moving component, and running power is big, energy consumption is big; Compare with mechanical agitation, it is to only depend on the effect of bubble that liquid is stirred that gas stirs, and the stirring dynamics is more weak, and the high viscosity liquid of several thousand milli handkerchiefs more than second also is difficult to be suitable for, and range of application is narrow and small.
Summary of the invention
Goal of the invention of the present utility model is to provide a kind of simple in structure for overcoming the deficiencies in the prior art, the pneumatic agitating device of the spiral-flow type that mixing effect is good.
For achieving the above object, the utility model is by the following technical solutions: the pneumatic agitating device of this spiral-flow type, comprise appendix, guide pipe, nozzle, also comprise the gather qi together current divider, appendix is equipped with in the upper end of this gather qi together current divider, and its lateral wall is provided with some guide pin bushings, and guide pin bushing is connected with guide pipe respectively, the other end of each guide pipe all is equipped with nozzle, and nozzle place horizontal plane is lower than guide pin bushing place horizontal plane.
Compared with prior art, the beneficial effects of the utility model are: this agitating device mixing great efforts, and nonmotile mechanical part power is little, energy consumption is low, and mixing effect is good; Be applicable to the stirring of solid-liquid material easy deposition, thickness; Temperature applicable range is big.
Description of drawings
Fig. 1 is an overall structure schematic diagram of the present utility model.
Among the figure: appendix 1, gather qi together current divider 2, guide pin bushing 3, guide pipe 4, clip 5, nozzle 6.
The specific embodiment
The utility model is described in further detail below in conjunction with drawings and Examples.
Referring to accompanying drawing, in the present embodiment, the pneumatic agitating device of this spiral-flow type is made of appendix 1, gather qi together current divider 2, guide pin bushing 3, guide pipe 4, clip 5 and nozzle 6.Wherein the upper end of gather qi together current divider 2 is socketed with appendix 1, also uniformly on the lateral wall of gather qi together current divider 2 be connected with three guide pin bushings 3, each guide pin bushing 3 and gather qi together current divider 2 internal communication, the other end of guide pin bushing 3 also is threaded with the guide pipe 4 that is " J " shape respectively, the other end of each guide pipe 4 is fixedly connected with the nozzle 6 of duckbill structure with clip 5, guide pipe 4 is " J " shape except that having certain radian, himself also downward-sloping certain angle causes nozzle 6 place horizontal planes a little less than guide pin bushing 3 place horizontal planes.
Operation principle of the present utility model is as follows: with this agitating device as for container bottom, the air-flow that has certain pressure enters gather qi together current divider 2 by appendix 1, because gather qi together current divider 2 inner spaces are bigger, to flowing into the effect that its inner air-flow plays buffering, and then penetrate by each nozzle 6 through three guide pipes 4, because revolving by certain angle, puts by guide pipe 4, can be decomposed into the impulse force of circumferential and axial both direction simultaneously by the air-flow of nozzle 6 ejaculations, circumferentially impulse force impels liquid in rotation, and the solid particle bottom axially impulse force will deposit to downwards takes up thereupon, force material to circulate from top to bottom, and destroyed the eddy flow that produces by axial impulse force, thereby produce a kind of flow pattern that involves whole material.Can reach best mixed effect by the power of regulation and control air inflow.

Claims (1)

1, the pneumatic agitating device of a kind of spiral-flow type, comprise appendix, guide pipe, nozzle, it is characterized in that: also comprise the gather qi together current divider, appendix is equipped with in the upper end of this gather qi together current divider, its lateral wall is provided with some guide pin bushings, guide pin bushing is connected with guide pipe respectively, and the other end of each guide pipe all is equipped with nozzle, and nozzle place horizontal plane is lower than guide pin bushing place horizontal plane.
CNU2008201145718U 2008-05-26 2008-05-26 Toroidal swirl type pneumatic stirring device Expired - Fee Related CN201189459Y (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CNU2008201145718U CN201189459Y (en) 2008-05-26 2008-05-26 Toroidal swirl type pneumatic stirring device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CNU2008201145718U CN201189459Y (en) 2008-05-26 2008-05-26 Toroidal swirl type pneumatic stirring device

Publications (1)

Publication Number Publication Date
CN201189459Y true CN201189459Y (en) 2009-02-04

Family

ID=40333612

Family Applications (1)

Application Number Title Priority Date Filing Date
CNU2008201145718U Expired - Fee Related CN201189459Y (en) 2008-05-26 2008-05-26 Toroidal swirl type pneumatic stirring device

Country Status (1)

Country Link
CN (1) CN201189459Y (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105966147A (en) * 2016-06-30 2016-09-28 江门市合益印刷有限公司 Automatic chemical glue conveying device
CN112388996A (en) * 2020-09-28 2021-02-23 桑文新 Production equipment and method for preparing super-hydrophobic membrane based on calcium carbonate particle template method

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105966147A (en) * 2016-06-30 2016-09-28 江门市合益印刷有限公司 Automatic chemical glue conveying device
CN112388996A (en) * 2020-09-28 2021-02-23 桑文新 Production equipment and method for preparing super-hydrophobic membrane based on calcium carbonate particle template method

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Legal Events

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: 20090204

Termination date: 20160526