CN1978039A - Horizontal oscillation jet-flow mixing integrated device - Google Patents
Horizontal oscillation jet-flow mixing integrated device Download PDFInfo
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- CN1978039A CN1978039A CNA2005101262479A CN200510126247A CN1978039A CN 1978039 A CN1978039 A CN 1978039A CN A2005101262479 A CNA2005101262479 A CN A2005101262479A CN 200510126247 A CN200510126247 A CN 200510126247A CN 1978039 A CN1978039 A CN 1978039A
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- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 27
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/10—Biological treatment of water, waste water, or sewage
Abstract
The present invention relates to a kind of aerating apparatus for making organic waste water and lake water undergo the process of aerobic biological treatment, in particular, it is a horizontal oscillation jet flow mixing integrated equipment. It includes the following several portions: suction chamber, air drain communicated with said suction chamber, high-pressure pump and mixing pipe, in which the mixing pipe is horizontally mounted, and the outlet end of said mixing pipe is equipped with an oscillation device.
Description
Technical field
The present invention relates to a kind of being applicable to the various liquid mediums used in organic wastewater, the bioprocess technology and lake water etc. are carried out the aerator that aerobe is handled, especially a kind ofly in liquid, disperse, the used horizontal oscillation jet-flow mixing integrated device of dissolved gas.
Background technology
At present, when sewage being carried out the aerobe processing, the structure of normally used equipment comprises air compressor and several micro porous aeration heads that are communicated with it by mixing tube.Several micro porous aeration heads need be installed at the bottom of the aeration tank during use, and require the end face of aeration head to be positioned at same elevation, i.e. the cope level of aeration head control is very strict, otherwise the inequality of giving vent to anger has a strong impact on efficient; In addition, because air compressor can produce very large noise, usually need the pneumatics machine room, not only take ground resource, increase capital cost simultaneously, in use also needed the workman to keep in repair regularly, increased maintenance cost, only be suitable for building in the exurb based on above-mentioned each this kind of factor equipment, extensive concentrating carried out sewage disposal.In order to adapt to the needs of purifying waste water in the city, the aeration rotary brush or the aeration runner that are suitable for using in oxidation ditch appearred, it is in oxygenation in sewage, has the plug-flow effect again, but because the scope of its oxygenation is limited to superficial water, be easy to reduce dynamic efficiency in the air because of bubble is escaped into by the water surface, in addition mechanical component is easy to wearing and tearing and reduction reliability, and it is suitable for using in oxidation ditch, inapplicablely uses in river course, lake.Along with science and technology development, the inflator-AIRE-O of another kind of version has appearred
2Inflator, the structure of this inflator comprises high-speed motor and the rotating shaft of the hollow that driven by high-speed motor, and be provided with blade in the other end of rotating shaft, during use, usually be fixed on the ship shape frame, drive rotating shaft by high-speed motor and rotate at a high speed, thereby near blade, produce negative pressure, air is inhaled in the water by the hollow of rotating shaft, and the generation bubble that is integrated with water carries out sewage disposal.AIRE-O
2Inflator is oxygen supply both, cause again current by after push ahead, not only be suitable in oxidation ditch, using, also be suitable in river course, lake, using.But AIRE-O
2Still there is following defective in inflator: one, motor drive rotating shaft and rotate the strong noise of generation at a high speed, cause environmental pollution; Its two, during operation, rotating shaft and blade rotate at a high speed, very easily wearing and tearing, so the life-span lack.Also have a kind of water jet aerator device in the actual life, structure comprises the mixing tube of vertical installation and is positioned at high-pressure nozzle directly over the mixing tube and the high-pressure pump that is communicated with high-pressure nozzle.During use, the current that ejected by high-pressure nozzle carry ambient air and enter mixing tube, and by the outlet ejection of mixing tube bottom, can carry out sewage disposal, because no mechanical loss, so the life-span is long, and noise is low during the work of this kind aerator; But because mixing tube is vertically to install, the fluid column that injects mixing tube can directly strike on the base plate at the bottom of the pond, cause energy loss, be that mechanical energy fully is not used for sewage disposal, the part bubble of Chan Shenging can be raised to water surface fast and be ineffective in addition, so its energy consumption is big, efficient is low, simultaneously, do not possess yet by after the effect of plug-flow forward, be unsuitable in the oxidation ditch of city, using.And when using this kind device,, can impact mud at the bottom of the pond at the bottom of the pond by the fluid column of mixing tube ejection if base plate is not installed, and make water become muddy, clean-up effect is undesirable.
Summary of the invention
(1) technical problem that will solve
The objective of the invention is to overcome above-mentioned the deficiencies in the prior art, the horizontal oscillation jet-flow mixing integrated device that a kind of energy consumption is low, the life-span is long is provided.
(2) technical scheme
To achieve these goals, the present invention takes following scheme:
Horizontal oscillation jet-flow mixing integrated device of the present invention, comprise high-pressure pump, the high-pressure nozzle that is communicated with high-pressure pump and mixing tube, wherein also comprise induction chamber and the ventilation duct that is communicated with induction chamber, wherein said mixing tube is communicated with induction chamber, and with respect to the horizontal plane downward-sloping 0 °～45, described high-pressure nozzle is arranged on the sidewall of induction chamber, and installs with the coaxial collimation of mixing tube.
Wherein said ventilation duct top ends is provided with the shielding cap that prevents that foreign material from falling into, and is provided with the suction of being made by the sound-absorbing material layer of making an uproar in the described shielding cap.
Wherein saidly be connected with gradient tube between induction chamber and mixing tube, this gradient tube is that the bus rotation forms with the smooth curve.
Wherein said high-pressure pump connects together with induction chamber by connecting hose.
Wherein also comprise the oscillation device that is installed in described mixing tube outlet end, link together by connecting hose between oscillator in the oscillation device and the low-lift pump.
Its described high-pressure nozzle comprises cylindric head body, on the diapire of cylindric head body, be provided with circular jet orifice and several special-shaped jet orifices, wherein said circular jet orifice is positioned at diapire central authorities, and the center that described several special-shaped jet orifices are distributed in circular jet orifice is on several different concentric circles of the center of circle, radius; The shape of cross section of described special-shaped jet orifice is kidney-shaped, and bends towards circular jet orifice, and the vertical sectional shape of special-shaped jet orifice is an isosceles trapezoid, and the described inside bottom wall wall upper base that is the isosceles trapezoid hole, and lateral wall is going to the bottom of isosceles trapezoid hole.
The bus that wherein forms gradient tube is an equation of higher degree curve.
Wherein said connecting hose comprises two flanges and the flexible pipe that is connected two flanges.
Wherein said oscillator comprises body, in body, be provided with the oral siphon, vibration chamber and the delivery outlet that are interconnected, high pressure nozzle is installed in the oral siphon, wherein vibration chamber comprises the left side feedback volute chamber of sprue and the rounding off curve form that is positioned at the sprue and arranged on left and right sides) and right feedback volute chamber, at left side feedback volute chamber and oral siphon link position place, the tangent plane of the locular wall face of left side feedback volute chamber and the angle α of oral siphon axis are 100 °～160 °; At right side feedback volute chamber and oral siphon link position place, the tangent plane of the locular wall face of right feedback volute chamber and the angle β of oral siphon axis are 90 °～100 °; Stream point is chosen on a left side to described left and right feedback volute chamber, the stream point is chosen on the right side forming with the delivery outlet junction, correspondingly, left and right feedback volute chamber is near each self-forming of delivery outlet position left side reflection bailing bucket and right reflection bailing bucket, and the volume of left side reflection bailing bucket is 1.1～1.8 times of volume of right reflection bailing bucket; A described left side choose stream point be higher than the right side choose stream sharp 9-2mm; The diameter of delivery outlet at the water inlet place is 1.1 times of diameter of oral siphon; Choose the sharp position of stream near a left side on the The initial segment inwall of delivery outlet and be provided with the choked flow bank that protrudes to the axis.
10. horizontal oscillation jet-flow mixing integrated device as claimed in claim 5, it is characterized in that the described fluidic oscillator of described oscillator, it is characterized in that in the described vibration chamber, the sprue lower position is provided with dividing plate I, be divided into left runner I and right runner I, and be provided with secondary input port and secondary input pipe at dividing plate I middle position, described delivery outlet is communicated with secondary vibration chamber, be provided with dividing plate II in the secondary vibration chamber, be divided into left runner II and right runner II, dividing plate II middle position is provided with three grades of input ports and three grades of input pipes; Three grades of vibration chamber of the delivery outlet of secondary vibration chamber are provided with dividing plate III in three grades of vibration chamber, are divided into left runner III and right runner III, and dividing plate III middle position is provided with level Four input port and level Four input pipe, and described three grades of vibration chamber's delivery outlets are wealthy delivery outlet gradually; The and arranged on left and right sides of the equipped at outlet port of described secondary vibration chamber is provided with lower-left tube connector and bottom right tube connector separately, the delivery port place and arranged on left and right sides of described oral siphon is provided with perpendicular upper left tube connector and bottom right tube connector separately, corresponding lower-left, upper left tube connector are connected with left side feedback runner, bottom right, upper right tube connector are connected with right feedback runner, described left side feedback runner, right feedback runner separately the plane at place perpendicular to each plane, vibration chamber place; Described lower-left tube connector and bottom right tube connector and three grades of vibration chamber's link positions form that the sharp I of stream is chosen on a left side and the sharp I of stream is chosen on the right side.
(3) beneficial effect
The advantage and the good effect of horizontal oscillation jet-flow mixing integrated device of the present invention are: among the present invention, because the with respect to the horizontal plane downward-sloping 0 °～45 of mixing tube, and the coaxial collimation of high-pressure nozzle and mixing tube is installed, like this by the momentum of high-pressure nozzle penchu can big portion be used to promote by the air water emulsion of the mixing tube port of export by after flow forward, and can not lose, the realization Energy Efficient is transmitted, increase service area, so horizontal oscillation jet-flow mixing integrated device energy consumption of the present invention is low, efficient is high; Device of the present invention in addition still belongs to the water jet aerator device, and each parts need not rotation at a high speed in the use, does not have mechanical loss, so the life-span of the present invention is long, noise is low.
Description of drawings
The structural representation of Fig. 1 horizontal oscillation jet-flow mixing integrated device of the present invention;
Fig. 2 is the structural representation of the high-pressure nozzle among the present invention;
Fig. 3 is the structure for amplifying schematic diagram of A part among Fig. 2;
Fig. 4 is the upward view of Fig. 2;
Fig. 5 is the structural representation of first embodiment of the oscillator among the present invention;
Fig. 6 is the A-A profile of Fig. 5;
Fig. 7 is the B-B profile of Fig. 5;
Fig. 8 is the structural representation of second embodiment of the oscillator among the present invention;
Fig. 9 is the C-C profile of Fig. 8.
Among the figure: 1. high-pressure pump; 2. connecting hose; 3. induction chamber; 4. ventilation duct; 5. shielding cap; 6. gradient tube; 7. mixing tube; 8. low-lift pump; 9. oscillator; 10. high-pressure nozzle; 11. oscillation device; 12. flange; 14. flexible pipe; 22. head body; 24. circular jet orifice; 25. special-shaped jet orifice; 26. diapire; 51. interior camber line; 52. outer camber line; 53. semicircle end line; 110. body; 112. oral siphon; 113. dividing plate I; 114. left runner I; 115. right runner I; 116. secondary input port; 117. left runner II; 118. right runner II; 900. the stream point is chosen on the right side; 100. the stream point is chosen on a left side; 111. right feedback volute chamber; 112. left side feedback volute chamber; 130. delivery outlet; 140. three grades of input ports; 220. dividing plate II; 230. the delivery outlet of secondary vibration chamber; 240. dividing plate III; 250. left runner III; 260. right runner III; 270. right reflection bailing bucket; 280. right feedback channel; 290. lower-left tube connector; 300. bottom right tube connector; 310. upper left tube connector; 320. upper right tube connector; 330. left side feedback runner; 340. the sharp I of stream is chosen on a left side; 350. the sharp I of stream is chosen on the right side; 360. choked flow bank.
The specific embodiment
Following examples are used to illustrate the present invention, but are not used for limiting protection scope of the present invention.
As shown in Figure 1, horizontal oscillation jet-flow mixing integrated device of the present invention, comprise have top end opening, the induction chamber 3 of left end opening, right-end openings, wherein the top end opening of induction chamber 3 is communicated with ventilation duct 4; The left end opening part is equipped with high-pressure nozzle 10, and high-pressure nozzle 10 is communicated with high-pressure pump 1; Right-end openings is communicated with gradient tube 6, and the other end of gradient tube 6 is communicated with mixing tube 7, at the outlet end of mixing tube 7 oscillation device 11 is housed.Wherein mixing tube 7, gradient tube 6 and high-pressure nozzle 10 are that coaxial collimation is installed, and that is to say that three's axis is located along the same line, and can reduce the loss in the energy transfer process so to greatest extent, improve charging efficiency and service area.Induction chamber 3 structures shown in Fig. 1 are vertically to install for part threeway commonly used, ventilation duct 4, and mixing tube 7, gradient tube 6 and high-pressure nozzle 10 all are levels.In actual applications, ventilation duct 4 also can tilt, for example, it all is feasible acutangulating or become the obtuse angle with the jet direction of high-pressure nozzle 10, wherein under the obtuse-angulate situation of jet direction of ventilation duct 4 and high-pressure nozzle 10, because the two more reaches unanimity, and helps reducing the resistance that carries air, benefits and increases work efficiency.Mixing tube 7 also can with respect to the horizontal plane downward-sloping certain angle, as 15 °, 25 °, 30 °, 40 °, 45 ° at the oblique angle of dipping down etc., with respect to the horizontal plane downward-sloping in a word 0 °～45 ° all is feasible, at this moment, in order to guarantee, the coaxial collimation of gradient tube 6, high-pressure nozzle 10 and mixing tube 7, gradient tube 6, high-pressure nozzle 10 are also wanted downward-sloping corresponding angle simultaneously.
High-pressure nozzle 10 among the present invention is communicated with high-pressure pump 1 by connecting hose 2, also links together by connecting hose between oscillator 9 in the oscillation device 11 and the low-lift pump 8.Connecting hose 2 comprises two flanges 12 and the flexible pipe 14 that is connected two flanges 12.Adopt the connecting hose 2 this benefits that are flexible coupling to be: not only easy for installation, and be beneficial to the reduction noise, be beneficial to environmental protection.Ventilation duct 4 top ends are provided with shielding cap 5, fall into the obstruction ventilation duct to prevent foreign material such as branch, are provided with the suction of being made by the sound-absorbing material layer of making an uproar in the shielding cap 5, to reduce noise of the present invention.Gradient tube 6 is with equation of higher degree curve: R=ax
n+ bx
m+ cx
p+ dx
qFor bus rotation forms, the gradient tube of this kind shape helps sucking more gas, and is beneficial to gas and water fully mixes, and reduces resistance, further cuts down the consumption of energy.Gradient tube 6 also can be that bus forms by the smooth curve of other shapes.
Referring to Fig. 2 to Fig. 4.High-pressure nozzle among the present invention, comprise cylindric head body 22, on the diapire 26 of cylindric head body 22, be provided with several jet orifices, described several jet orifices are made up of circular jet orifice 24 and several special-shaped jet orifices 25 of being arranged on diapire central authorities, the center that wherein said several special-shaped jet orifices 25 are distributed in circular jet orifice 24 is the center of circle, on different several concentric circles of radius, and 25 layouts straggly of the special-shaped jet orifice on adjacent concentric circles, help strengthening surrounding air like this and in the middle of the fluid column that sprays, gather effect, that is to say, be involved in wherein in that the fluid column ambient air is easier, thereby improve aeration quantity.Among the present invention, the number that is distributed with the special-shaped jet orifice of arranging on the concentrically ringed number of special-shaped jet orifice 25 and each concentric circles 25 and processed water depth, to add factors such as water pressure size relevant.
As shown in Figure 4, the high-pressure nozzle among the present invention, the cross section of special-shaped jet orifice 25 (promptly vertical with the axis of cylindric head body 22 cross section) shape is kidney-shaped, and bends towards circular jet orifice 24, promptly bends towards the axis direction of head body 22.Wherein said kidney-shaped further is interpreted as: the shape of cross section of special-shaped jet orifice 25 is formed by connecting in turn by four lines head and the tail, these four lines be respectively the center of circle with circular jet orifice 24 be the center of circle interior camber line 51, the outer camber line 52 done and connect in two semicircle end lines 53 compositions of camber line 51 and outer camber line 52.In the liquid course of injection, the pressure P1 on plane, camber line 51 place is smaller in acting on, and acts on the P on plane, outer camber line 52 place
2Pressure bigger, i.e. P
1＜P
2, so just increased the function of entrainmenting air, promptly easier air between each jet orifice is drawn in the liquid, be beneficial to the air content that improves liquid.In the high-pressure nozzle among the present invention, the longitudinal section (promptly parallel with the axis of cylindric head body 22 cross section) of abnormity jet orifice 25 is shaped as isosceles trapezoid, and described diapire 26 madial walls are the upper base in isosceles trapezoid hole, lateral wall is going to the bottom of isosceles trapezoid hole, base angle is 20 °-80 °, be preferably 30 °-60 °, best angle is 45 °.This longitudinal section of the present invention is the fluid column profile undulate that the diameter of isosceles trapezoid and fluid column porch ejects less than the jet orifice of the diameter in exit, the surface tension of fluid column can produce positive feedback effect, the crest of waveform fluid column and the radially difference of trough are aggravated gradually along the fluid column axial direction, cause the fluid column of end to fragment into drop at last, the kinetic energy of drop passes to the air of contact with it by bump, realized the momentum conversion, thereby made gas, water quicken to merge.So effect of the special-shaped jet orifice of this given shape, be not only the contact area that has increased air and liquid, the drop that positive feedback effect caused that main is is produced by the fluid column surface tension quickens with air, the benign cycle of fully fusion and increase substantially the tolerance of taking of liquid.About the positive feedback principle, in PHYSICAL FLUID DYANMICS one book of the D.J.Tritton of Britain work, among the 201st page of the 17th chapter InstabilityPhenomena detailed introduction is arranged.
Referring to Fig. 5, Fig. 6 and Fig. 7.Referring to Fig. 5, Fig. 6 and Fig. 7.First kind of embodiment of fluidic oscillator of the present invention, comprise body 110, in body 110, be provided with the oral siphon 112 that is interconnected, vibration chamber and gradually wealthy delivery outlet 130, wherein vibration chamber comprises sprue and is positioned at a sprue left side, the left side feedback volute chamber 120 of the rounding off curve form of right both sides and right feedback volute chamber 111, a left side, right feedback volute chamber is chosen stream point 100 forming a left side with wealthy delivery outlet 130 junctions gradually, stream point 900 is chosen on the right side, correspondingly, a left side, right feedback volute chamber is each self-forming left side reflection bailing bucket 160 and the right bailing bucket 270 that reflects in close gradually wealthy delivery outlet 130 positions, and high pressure nozzle is installed in the oral siphon.At left side feedback volute chamber 120 and oral siphon 112 link position places, the angle α of the tangent plane of the locular wall face of left side feedback volute chamber 120 and the axis of oral siphon 112 is 150 °, and this angle all is feasible in 100 °～160 ° scopes; At right side feedback volute chamber 111 and oral siphon 112 link position places, the angle β of the tangent plane of the locular wall face of right feedback volute chamber 111 and the axis of oral siphon 112 is 90 °, this angle all is feasible in 90 °～100 ° scopes, and the axis of oral siphon 112 is offset to left side feedback volute chamber 120 1 sides with respect to the axis of wealthy delivery outlet 130 gradually.Among the present invention, left and right vibration chamber differences in shape is bigger, it no longer is the shape of existing basic symmetry, particularly α is 150 °, and being 90 °, β so just strengthened modulation depth, make the jet that sprays by nozzle effectively be attached to more rapidly on the locular wall of left side feedback volute chamber 120, and formation cutout on the locular wall of right side feedback volute chamber 111, thereby make the fluidic oscillation in exit violent more; The volume of left side reflection bailing bucket 160 is greater than 1.5 times of the volumes of right side reflection bailing bucket 270 among the present invention, and this multiple all is feasible in 1.1～1.8 times of scopes; The diameter of gradually wealthy delivery outlet 130 at the water inlet place is 1.1 times of diameter of oral siphon 112; A left side is chosen stream point 100 and is higher than the right side and chooses the sharp 9009-2mm of stream, choose sharp 100 positions of stream near a left side on the The initial segment inwall of delivery outlet 1300 and be provided with the choked flow bank 360 that protrudes to the axis, to form vortex, make the break-off of Karman vortex street more remarkable, cause the resistance fluctuations of equipped at outlet port, make the jet switching alternately, form water hammer, make the pulsed quantity intensity of feedback stronger, change and come flow path direction, improved outlet pressure.Through the reality test, when inlet pressure was 100Mpa, the outlet pressure crest value can reach 150Mpa, can exceed 45% usually.And traditional situation is: when inlet pressure was 100Mpa, outlet pressure had only 50Mpa usually.
The course of work of this embodiment is: at first, jet major part by the nozzle ejection enters gradually wealthy delivery outlet 130 along sprue, the small part jet is chosen stream point 100 by a left side and is chosen back, shown in solid arrow among Fig. 5, being attached to a left side feeds back on the locular wall of volute chamber 120 mobile clockwise, exit to oral siphon 112, promote the jet major part by flowing to gradually wealthy delivery outlet 130 in the sprue, also having simultaneously the small part jet is chosen stream point 11 by the right side and chooses back, shown in dotted arrow among Fig. 5, being attached to the right side feeds back on the locular wall of volute chamber 111 mobile counterclockwise, exit to oral siphon 112, promote the jet major part by flowing to gradually wealthy delivery outlet 130 in the sprue, have the small part jet to be attached to a left side again and feed back on the locular wall of volute chamber 120 mobile clockwise ... so move in circles alternate oscillation.
Referring to Fig. 8, Fig. 9.The structure of second kind of multistage oscillator of embodiment of the present invention, comprise body 110, in body 110, be provided with the oral siphon 112 that is interconnected, vibration chamber, in the vibration chamber, the sprue lower position is provided with dividing plate I113, be divided into left runner I114 and right runner I115, and be provided with secondary input port 116 and secondary input pipe in the dividing plate I113 central authorities position of taking back, delivery outlet 1300 is communicated with secondary vibration chamber, be provided with dividing plate II220 in the secondary vibration chamber, be divided into left runner II117 and right runner II118, the dividing plate II220 central authorities position of taking back is provided with three grades of input ports 140 and three grades of input pipes; 230 3 grades of vibration chamber of the delivery outlet of secondary vibration chamber, be provided with dividing plate III240 in three grades of vibration chamber, be divided into left runner III250 and right runner III260, the dividing plate III240 central authorities position of taking back is provided with level Four input port 360 and level Four input pipe, and three grades of vibration chamber's delivery outlets are wealthy delivery outlet gradually; The and arranged on left and right sides at delivery outlet 230 places of secondary vibration chamber is provided with lower-left tube connector 290 and bottom right tube connector 300 separately, and lower-left tube connector 290 and bottom right tube connector 300 and three grades of vibration chamber's link positions form that the sharp I340 of stream is chosen on a left side and the sharp I350 of stream is chosen on the right side.The delivery port place and arranged on left and right sides of oral siphon 112 is provided with perpendicular upper left tube connector 310 and bottom right tube connector 320 separately, and corresponding lower-left, upper left tube connector are connected with left side feedback runner 330, and bottom right, upper right tube connector are connected with right feedback runner.The plane at place is perpendicular to each plane, vibration chamber place separately for left side feedback runner 330, right feedback runner, and the final stage delivery outlet 60 of the multistage oscillator of present embodiment is wealthy delivery outlet gradually.Because left and right feedback runner and vibration chamber are vertically arranged, have overcome a difficult problem of being stopped up by silt easily in the prior art, are beneficial to life-saving, can use for a long time.
In addition, also to can be used in the process for making with gas be that working media is strengthened in the ladle disturbance to molten steel to multistage oscillator of the present invention.
Have three vibration chamber that are interconnected in the present embodiment, last vibration chamber, promptly the delivery outlet of three grades of vibration chamber is wealthy delivery outlet gradually; And the delivery outlet of all the other vibration chamber is the gradually closing formula.The quantity of vibration chamber is not only limited to three, can also have more a plurality of.
Among the present invention, the jet that is penetrated by last delivery outlet forms the plural serial stage amplifier through the repeatedly stack of oscillating jet, and total magnification is the product of multiplication factors at different levels, so violent unusually, violent.Multistage oscillator of the present invention also can be made up of two single-stage oscillators or more a plurality of single-stage oscillator.
The course of work of the multistage oscillator of present embodiment is: shown in solid arrow among Fig. 8, jet by the nozzle ejection, successively through left runner I114, right runner II118, left side runner III250, by last gradually wealthy delivery port ejection, choosing the sharp I340 of stream via a left side when being, the small part jet is chosen into lower-left tube connector 290, through left side feedback runner 330, upper left tube connector 310, promotion changes direction by the jet of nozzle ejection, shown in dotted arrow among Fig. 8, successively through right runner I115, left side runner II117, right runner III260, by last gradually wealthy delivery port ejection, when choosing the sharp I350 of stream via the right side, the small part jet is chosen into bottom right tube connector 300, through right side feedback runner, upper right tube connector 32 promotes again to change direction by the jet of nozzle ejection, so move in circles, constantly vibration.
Oscillation device can form the shear strain field in the waters around, thereby produce the less bubble of a large amount of sizes, service area reaches thousands of square meters, promptly consume identical electric energy, the bubble that produces is more, service area is bigger, and just the energy consumption of horizontal oscillation jet-flow mixing integrated device of the present invention is low.
Among the present invention, the momentum flux (momentum flux) at the nozzle place is:
(mv)=ρ
WaterQ
nU
n=F
Dash
Wherein, Q
nBe the flow (m of nozzle ejection
3/ s);
U
nBe the speed (m/s) of the water of nozzle ejection;
ρ
WaterBe the density (kg/m of water
3).
Part in this momentum flux is used for the reaction to the hydrostatic pressure of supporting kang mixing tube exit, another part just is used for forwards promoting current, the water that promptly drives neighborhood flows forward, so horizontal oscillation jet-flow mixing integrated device of the present invention can make full use of primary power, the needs of oxidation ditch plug-flow have been adapted to again.
Horizontal oscillation jet-flow mixing integrated device of the present invention not only can be fixed to floating frame and bubble through the water column and carry out work, and carry out under the situation of work being unsuitable for bubbling through the water column, in the section if any pleasure-boat, cargo ship, or all can use when driving flood, at this moment, with the present invention with the built-in bank that is installed in, the top inlet that only need expose ventilation duct gets final product, thereby, can avoid main channel, not hinder the shipping of pleasure-boat, cargo ship, also can make the smooth and easy circulation of flood, do not influence flood passage, so the scope of application of the present invention is more extensive.
More than be preferred forms of the present invention, according to content disclosed by the invention, some identical, replacement schemes that those of ordinary skill in the art can expect apparently all should fall into the scope of protection of the invention.
Claims (10)
1. horizontal oscillation jet-flow mixing integrated device, comprise high-pressure pump (1), the high-pressure nozzle (10) that is communicated with high-pressure pump (1) and mixing tube (7), it is characterized in that also comprising induction chamber (3) and the ventilation duct (4) that is communicated with induction chamber (3), wherein said mixing tube (7) is communicated with induction chamber (3), and with respect to the horizontal plane downward-sloping 0 °～45, described high-pressure nozzle (10) is arranged on the sidewall of induction chamber (3), and installs with the coaxial collimation of mixing tube (7).
2. horizontal oscillation jet-flow mixing integrated device as claimed in claim 1 is characterized in that described ventilation duct (4) top ends is provided with the shielding cap (5) that prevents foreign material and fall into, and is provided with the suction of being made by the sound-absorbing material layer of making an uproar in the described shielding cap (5).
3. horizontal oscillation jet-flow mixing integrated device as claimed in claim 1 is characterized in that describedly being connected with gradient tube (6) between induction chamber (3) and mixing tube (7), and this gradient tube (6) is that the bus rotation forms with the smooth curve.
4. horizontal oscillation jet-flow mixing integrated device as claimed in claim 1 is characterized in that described high-pressure pump (1) connects together with induction chamber (3) by connecting hose (2).
5. horizontal oscillation jet-flow mixing integrated device as claimed in claim 1, it is characterized in that also comprising the oscillation device (11) that is installed in described mixing tube (7) outlet end, link together by connecting hose between oscillator (9) in the oscillation device (11) and the low-lift pump (8).
6. horizontal oscillation jet-flow mixing integrated device as claimed in claim 1, it is characterized in that described high-pressure nozzle (10) comprises cylindric head body (22), on the diapire (26) of cylindric head body (22), be provided with circular jet orifice (24) and several special-shaped jet orifices (25), wherein said circular jet orifice (24) is positioned at diapire (26) central authorities, and the center that described several special-shaped jet orifices (25) are distributed in circular jet orifice (24) is on several different concentric circles of the center of circle, radius; The shape of cross section of described special-shaped jet orifice (25) is kidney-shaped, and bend towards circular jet orifice (24), the vertical sectional shape of abnormity jet orifice (25) is an isosceles trapezoid, and described diapire (26) madial wall is the upper base in isosceles trapezoid hole, and lateral wall is going to the bottom of isosceles trapezoid hole.
7. horizontal oscillation jet-flow mixing integrated device as claimed in claim 3, the bus that it is characterized in that forming gradient tube (6) is an equation of higher degree curve.
8. as claim 4 or 5 described horizontal oscillation jet-flow mixing integrated devices, it is characterized in that described connecting hose (2) comprises two flanges (12) and the flexible pipe (14) that is connected two flanges (12).
9. horizontal oscillation jet-flow mixing integrated device as claimed in claim 5, it is characterized in that described oscillator (9) comprises body (110), in body (110), be provided with the oral siphon (112) that is interconnected, vibration chamber and delivery outlet (130), high pressure nozzle is installed in the oral siphon, wherein vibration chamber comprises sprue and is positioned at a sprue left side, the left side feedback volute chamber (120) of the rounding off curve form of right both sides and right feedback volute chamber (111), at left side feedback volute chamber (120) and oral siphon (112) link position place, the tangent plane of the locular wall face of left side feedback volute chamber (120) and the angle α of oral siphon (112) axis are 100 °～160 °; At right side feedback volute chamber (111) and oral siphon (112) link position place, the tangent plane of the locular wall face of right feedback volute chamber (111) and the angle β of oral siphon (112) axis are 90 °～100 °; Stream point (100) is chosen on a left side to described left and right feedback volute chamber, stream point (900) is chosen on the right side forming with delivery outlet (130) junction, correspondingly, left and right feedback volute chamber is near each self-forming of delivery outlet (130) position left side reflection bailing bucket (160) and right reflection bailing bucket (270), and the volume of left side reflection bailing bucket (160) is 1.1～1.8 times of the right volume that reflects bailing bucket (270); A described left side is chosen stream point (100) and is higher than the right side and chooses stream point (900) 9-2mm; The diameter of delivery outlet (130) at the water inlet place is 1.1 times of diameter of oral siphon (112); Choose stream point (100) position near a left side on the The initial segment inwall of delivery outlet (130) and be provided with the choked flow bank (360) that protrudes to the axis.
10. horizontal oscillation jet-flow mixing integrated device as claimed in claim 5, it is characterized in that the described fluidic oscillator of described oscillator (9), it is characterized in that in the described vibration chamber, the sprue lower position is provided with dividing plate I (113), be divided into left runner I (114) and right runner I (115), and be provided with secondary input port (116) and secondary input pipe at dividing plate I (113) middle position, described delivery outlet (130) is communicated with secondary vibration chamber, be provided with dividing plate II (220) in the secondary vibration chamber, be divided into left runner II (117) and right runner II (118), dividing plate II (220) middle position is provided with three grades of input ports (140) and three grades of input pipes; (230) three grades of vibration chamber of the delivery outlet of secondary vibration chamber, be provided with dividing plate III (240) in three grades of vibration chamber, be divided into left runner III (250) and right runner III (260), dividing plate III (240) middle position is provided with level Four input port (360) and level Four input pipe, and described three grades of vibration chamber's delivery outlets are wealthy delivery outlet gradually; The and arranged on left and right sides that the delivery outlet (230) of described secondary vibration chamber is located is provided with lower-left tube connector (290) and bottom right tube connector (300) separately, the delivery port place and arranged on left and right sides of described oral siphon (112) is provided with perpendicular upper left tube connector (310) and bottom right tube connector (320) separately, corresponding lower-left, upper left tube connector are connected with left side feedback runner (330), bottom right, upper right tube connector are connected with right feedback runner, described left side feedback runner (330), right feedback runner separately the plane at place perpendicular to each plane, vibration chamber place; Described lower-left tube connector (290) and bottom right tube connector (300) and three grades of vibration chamber's link positions form a left side and choose stream sharp I (340) and the right side and choose and flow sharp I (350).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB2005101262479A CN100467105C (en) | 2005-11-30 | 2005-11-30 | Horizontal oscillation jet-flow mixing integrated device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB2005101262479A CN100467105C (en) | 2005-11-30 | 2005-11-30 | Horizontal oscillation jet-flow mixing integrated device |
Publications (2)
| Publication Number | Publication Date |
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| CN1978039A true CN1978039A (en) | 2007-06-13 |
| CN100467105C CN100467105C (en) | 2009-03-11 |
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| CNB2005101262479A Expired - Fee Related CN100467105C (en) | 2005-11-30 | 2005-11-30 | Horizontal oscillation jet-flow mixing integrated device |
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Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107807090A (en) * | 2017-10-31 | 2018-03-16 | 中煤科工集团重庆研究院有限公司 | U-shaped spectrum absorption integrated air chamber |
| CN108144470A (en) * | 2017-12-18 | 2018-06-12 | 大连通亚重工有限公司 | A kind of gas-liquid mixed pipe |
| CN114917780A (en) * | 2022-06-09 | 2022-08-19 | 东南大学 | Mixing device for cylindrical granular materials |
| CN117960415A (en) * | 2024-03-28 | 2024-05-03 | 箭牌家居集团股份有限公司 | Oscillator unit and water outlet device |
| CN117960420A (en) * | 2024-03-28 | 2024-05-03 | 箭牌家居集团股份有限公司 | Water outlet device |
-
2005
- 2005-11-30 CN CNB2005101262479A patent/CN100467105C/en not_active Expired - Fee Related
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107807090A (en) * | 2017-10-31 | 2018-03-16 | 中煤科工集团重庆研究院有限公司 | U-shaped spectrum absorption integrated air chamber |
| CN108144470A (en) * | 2017-12-18 | 2018-06-12 | 大连通亚重工有限公司 | A kind of gas-liquid mixed pipe |
| CN114917780A (en) * | 2022-06-09 | 2022-08-19 | 东南大学 | Mixing device for cylindrical granular materials |
| CN114917780B (en) * | 2022-06-09 | 2023-01-31 | 东南大学 | Mixing device for cylindrical granular materials |
| CN117960415A (en) * | 2024-03-28 | 2024-05-03 | 箭牌家居集团股份有限公司 | Oscillator unit and water outlet device |
| CN117960420A (en) * | 2024-03-28 | 2024-05-03 | 箭牌家居集团股份有限公司 | Water outlet device |
Also Published As
| Publication number | Publication date |
|---|---|
| CN100467105C (en) | 2009-03-11 |
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