CN2508846Y - Air flow stirring apparatus - Google Patents

Air flow stirring apparatus Download PDF

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Publication number
CN2508846Y
CN2508846Y CN01268689.1U CN01268689U CN2508846Y CN 2508846 Y CN2508846 Y CN 2508846Y CN 01268689 U CN01268689 U CN 01268689U CN 2508846 Y CN2508846 Y CN 2508846Y
Authority
CN
China
Prior art keywords
air
blowpipe
valves
stirring
gas
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
CN01268689.1U
Other languages
Chinese (zh)
Inventor
吕兆军
刘安培
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.)
Individual
Original Assignee
Individual
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 Individual filed Critical Individual
Priority to CN01268689.1U priority Critical patent/CN2508846Y/en
Application granted granted Critical
Publication of CN2508846Y publication Critical patent/CN2508846Y/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Abstract

An air stirrer relates to the stirring technical field and is characterized in that the air outlet of a blower (an air compressor) (1) is communicated with a blowpipe (8), and the blowpipe (8) is arranged at the bottom of a stirring container (9). The utility model has the advantages that the stirrer has no cutting effect on fluid when in stirring; and the stirring intensity can be a stepless control; a separate air stirrer can stir a plurality of containers at one time.

Description

Air flow stirring apparatus
One, technical field
Relate to the stirring technique field, particularly a kind of agitating device of forcing multiple solution to mix.
Two, background technology
The power alr mode of agitated liquid mainly is the propeller agitation mode at present in open container.The relative complex structure of propeller machine agitating device, most and container is mounted to one, and can not stir a plurality of containers simultaneously.In addition, the propeller agitation mode is difficult to stirring intensity is carried out electrodeless adjusting.This novel practical invention be exactly a kind of can be simultaneously to a plurality of containers stir and stirring intensity is adjustable device.
Three, summary of the invention:
The invention of this novel practical provides a kind of can the stirring a plurality of containers simultaneously, and stirring intensity is carried out the agitating device of electrodeless adjusting.The utility model is taked following technical scheme: include air blast (or air compressor machine) 1, gas-distributing pipe 2, air valve 3, appendix 4, choke valve 5, check-valves 6, air gauge 7, blowpipe 8, container 9, gas-distributing pipe 2 is connected in air blast (air compressor machine) 1 gas outlet, gas-distributing pipe 2 connects some air valves 3, air valve 3 another termination appendixs, another termination check-valves 6 of appendix, check-valves 6 other ends are connected blowpipe 8, are provided with air gauge 7 between check-valves 6 and the blowpipe 8, and blowpipe 8 is arranged on the bottom of stirred vessel 9.The pressure air that produces enters in each gas transmission arm 4 through gas-distributing pipe 2 and valve 3, enters in the liquid through choke valve 5 and blowpipe 8, and form big and small one by one bubble among liquid.Because the proportion of bubble is far smaller than the proportion of liquid, so bubble can rise and constantly division or polymerization in uphill process rapidly.Bubble is understood explosion and is entered air near liquid surface the time.The part that drives its liquid of parcel that rises rapidly of bubble rises simultaneously, makes liquid " convection current ".The liquid of bubble around in uphill process, also can pushing, the vibrations that produce when the adding bubble eruption impact of chamber wall (when the comprising liquid convection to), liquid presents the boiling phenomenon of similar boiling water.Under the effect of this " boiling " phenomenon, the solution that participates in mixing can mix very soon.The utility model has following beneficial effect: during agitated liquid, liquid is not had dissection, this polymer substance dilution to long strand is stirred has Practical significance.When for example the mixing of high polymer coagulant and waste water stirs, can not adopt the alr mode of dissection.To avoid strand to be prescinded drug effect is reduced; The intensity that stirs can electrodelessly be regulated; Independent air flow stirring apparatus can stir several containers simultaneously.
Four, description of drawings:
Fig. 1 is the structural representation of the utility model embodiment.
Five, the specific embodiment:
As required, a cover air flow stirring apparatus can simultaneously or not stir a plurality of containers simultaneously.The gas-distributing pipe diameter is big (also can be pot container), has the volume that holds a certain amount of pressure air, so that make stream pressure steady.Every appendix is controlled the break-make of air-flow, the switch of the work of cell therefor stirring just respectively by stop valve.Choke valve can be regulated the stirring intensity of each container respectively, with the character (as the difference of viscosity) that adapts to different solutions.The operator can also demarcate stirring intensity by air gauge.
Blowpipe generally is installed in the bottom of container, and the distance that bubble is risen in liquid is longer, stirring action the best.The shape of blowpipe can be diversified.Can evenly distribute according to the container section shape.The manufactured materials of blowpipe can be selected PVC plastics, fiberglass, stainless steel or the like according to the character of liquid.
Carry the pipeline of air to enter container from the top of container to blowpipe and link to each other, in case liquid refluence inlet pipe road with blowpipe.The effect of check valve also is to stop the liquid into gas-distributing pipe that flows backwards.

Claims (1)

1, a kind of air flow stirring apparatus, include air blast (or air compressor machine) (1), gas-distributing pipe (2), air valve (3), appendix (4), choke valve (5), check-valves (6), air gauge (7), blowpipe (8), container (9), it is characterized in that: gas-distributing pipe (2) is connected in air blast (air compressor machine) (1) gas outlet, gas-distributing pipe (2) connects some air valves (3), another termination appendix (4) of air valve (3), another termination check-valves (6) of appendix (4), check-valves (6) other end is connected blowpipe (8), be provided with air gauge (7) between check-valves (6) and the blowpipe (8), blowpipe (8) is arranged on the bottom of stirred vessel (9).
CN01268689.1U 2001-12-05 2001-12-05 Air flow stirring apparatus Expired - Fee Related CN2508846Y (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN01268689.1U CN2508846Y (en) 2001-12-05 2001-12-05 Air flow stirring apparatus

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN01268689.1U CN2508846Y (en) 2001-12-05 2001-12-05 Air flow stirring apparatus

Publications (1)

Publication Number Publication Date
CN2508846Y true CN2508846Y (en) 2002-09-04

Family

ID=33674834

Family Applications (1)

Application Number Title Priority Date Filing Date
CN01268689.1U Expired - Fee Related CN2508846Y (en) 2001-12-05 2001-12-05 Air flow stirring apparatus

Country Status (1)

Country Link
CN (1) CN2508846Y (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102627303A (en) * 2012-04-01 2012-08-08 大连交通大学 Method for preparing superfine magnesium hydroxide dispersible suspension
CN106492700A (en) * 2016-12-29 2017-03-15 南宁苏格尔科技有限公司 A kind of flocculant gas-moving device
CN106582420A (en) * 2016-12-29 2017-04-26 南宁苏格尔科技有限公司 Flocculant pneumatic transmission method

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102627303A (en) * 2012-04-01 2012-08-08 大连交通大学 Method for preparing superfine magnesium hydroxide dispersible suspension
CN102627303B (en) * 2012-04-01 2014-04-02 大连交通大学 Method for preparing superfine magnesium hydroxide dispersible suspension
CN106492700A (en) * 2016-12-29 2017-03-15 南宁苏格尔科技有限公司 A kind of flocculant gas-moving device
CN106582420A (en) * 2016-12-29 2017-04-26 南宁苏格尔科技有限公司 Flocculant pneumatic transmission method

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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