The even flow field diffuser
Technical field:
The invention belongs to weaving hydrodynamics Application Areas, it relates to a kind of even flow field diffuser.
Technical background:
In many workplaces, the flow field whether stablize the stability characteristic (quality) that directly has influence on duty.It is by prolonging the diffusion length H of anemostat 13 that existing even flow field diffuser 1 fluid state changes
1Realize the even continous-stable in flow field, as shown in Figure 1, common diffusion tube lengths H
1Be 3 times of diffusion area equivalent diameter.Gather the anemostat that spins or closely spin etc. on the equipment but be applied at present, because it is arranged on the bottom in slit between two row's rove lift spindles on the spinning locomotive or holder ingot, its locus is very little, can't pass through diffusion length H
1Realize that fluid is continuous, even, stable, solve, will directly affect the output and the quality of final products as not managing.
Summary of the invention:
In order to solve above-mentioned this technical barrier, be convenient in less space, realize the even diffusion in flow field, stable with the flow field that reaches negative pressure or malleation duty, the present invention utilizes the DIFFUSION IN TURBULENCE principle to provide the diffusion length of anemostat obviously to reduce, and can guarantee the new idea of a kind of even flow field diffuser that even flow field is stable again.
The technical scheme of technical solution problem of the present invention is as follows:
A kind of even flow field diffuser, it comprises air inlet 21, gas outlet 22, anemostat 23, the length a that it is characterized in that described anemostat 23 is 0.30~5.50 meter, the width b of anemostat 23 is 0.10~2.50 meter, the height c of anemostat 23 is 0.10~2.50 meter, it also comprises the first homogenizing plate A of the band rectangular opening that its periphery is connected with anemostat 23, the length a of the first homogenizing plate A of its band rectangular opening
1Be 0.30~5.50 meter, the width b of the first homogenizing plate A of band rectangular opening
1Be 0.10~2.50 meter, the thickness w of the first homogenizing plate A of band rectangular opening
1Be 0.50~1.50 millimeter, the first homogenizing plate A of band rectangular opening is apart from the height c of anemostat 23 upper surfaces
1It is 0.10~2.50 meter and by reinforcing the corresponding second homogenizing plate B that is suspended in anemostat 23 tops of 4 steel wires of 4 apertures on the second homogenizing plate B, the length a of its second homogenizing plate B
2Be 0.20~4.50 meter, the width b of the second homogenizing plate B
2Be 0.08~2.20 meter, the thickness w of the second homogenizing plate B
2Be 0.50~1.50 millimeter, the second homogenizing plate B is apart from the height c of anemostat 23 upper surfaces
2Be 0.05~1.75 meter, its periphery should with 0.05~0.50 meter at interval of anemostat 23.
Described anemostat 23, the first homogenizing plate A of described band rectangular opening, the described second homogenizing plate B all adopts aluminium alloy plate or iron sheet or steel plate to make.
Advantage compared with prior art of the present invention is:
Traditional even flow field diffuser generally all takes to spread conduit, normal conditions are to connect flat, circle with circle to connect rectangle, roundlet and connect the change that various forms such as great circle is realized the flow field form, simultaneously guarantee that again the flow field of working region is the current stabilization attitude, above-mentioned various interface form all needs quite long spatial transition, is difficult to realize in the regional space small range.The present invention then can be installed in the narrow and small scope of regional space, is applicable to require to suck air-flow each branch flow on whole distribution of lengths and the occasion of negative pressure uniformity, can satisfy technological requirement again.So the present invention have current-sharing length weak point, even fluid distribution, the advantage such as little that takes up space.
Description of drawings:
The existing even flow field diffuser of Fig. 1 schematic diagram
Among Fig. 1, the existing even flow field diffuser of 1-, 11-air inlet, 12-gas outlet, 13-anemostat, H
1-diffusion length;
Fig. 2 even flow field diffuser of the present invention schematic diagram
Among Fig. 2,2-even flow field diffuser, 21-air inlet, 22-gas outlet, 23-anemostat, the length of a-anemostat 23, the width of b-anemostat 23, the height of c-anemostat 23, first homogenizing plate of A-band rectangular opening, a
1The length of the first homogenizing plate A of-band rectangular opening, b
1The width of the first homogenizing plate A of-band rectangular opening, w
1The thickness of the first homogenizing plate A of-band rectangular opening, c
1The first homogenizing plate A of-band rectangular opening is apart from the height of anemostat 23 upper surfaces; B-second homogenizing plate, a
2The length of-the second homogenizing plate B, b
2The width of-the second homogenizing plate B, w
2The thickness of-the second homogenizing plate B, c
2-the second homogenizing plate B is apart from the height of anemostat 23 upper surfaces.
The specific embodiment:
Be placed in to gather and spin or the tight even flow field anemostat of the bottom in two row's rove lift spindles or holder ingot slit on the spinning equipment, the length a of its anemostat 23 is 0.30~25.50 meter, the width b of anemostat 23 is 0.10~2.50 meter, the height c of anemostat 23 is 0.20~5.00 meter, and air inlet 21 and gas outlet 22 are arranged, in anemostat 23, be provided with the first homogenizing plate A of band rectangular opening, the length a of the first homogenizing plate A of its band rectangular opening
1Be 0.30~25.50 meter, the width b of the first homogenizing plate A of band rectangular opening
1Be 0.10~2.50 meter, the thickness w of the first homogenizing plate A of band rectangular opening
1Be 0.50~1.50 millimeter, the first homogenizing plate A of band rectangular opening is apart from the height c of anemostat 23 upper surfaces
1Be 0.10~2.50 meter, its periphery is connected with anemostat 23 inwalls; In anemostat 23, also be provided with by reinforcing the corresponding second homogenizing plate B that is suspended in anemostat 23 tops of 4 steel wires of 4 apertures on the second homogenizing plate B, the length a of its second homogenizing plate B
2Be 0.20~4.50 meter, the width b of the second homogenizing plate B
2Be 0.08~2.20 meter, the thickness w of the second homogenizing plate B
2Be 0.50~1.50 millimeter, the second homogenizing plate B is apart from the height c of anemostat 23 upper surfaces
2Be 0.05~1.75 meter, its periphery should with 0.05~0.50 meter at interval of anemostat 23.The material of this device all adopts aluminium alloy plate or iron sheet or steel plate to make.Operation principle:
The present invention is installed in the even flow field anemostat with two homogenizing plates, utilize the DIFFUSION IN TURBULENCE principle in flow field, inside and outside DIFFUSION IN TURBULENCE by two homogenizing plates, make bottom half become the plenum chamber of fluid, the bottom half internal gas pressure equates everywhere, utilize this principle under the situation that diffusion length obviously reduces, the air flow rate and the air pressure of each air admission hole of bottom are consistent.The present invention can be installed in the narrower and small zone, space mounting position, is applicable to the occasion of sending down the air current flow of inhaling and requires suction air-flow each branch flow on whole distribution of lengths and the occasion of negative pressure uniformity, can satisfy technological requirement again.