The Venturi blender that special inlet tube is contained in a kind of throat
Technical field
The utility model relates to a kind of venturi mixer, is specifically related to the Venturi blender that special inlet tube is contained in a kind of throat.
Background technology
Venturi mixer is as a kind of important gas-liquid or liquid liquid mixing arrangement, in engineering reality, have a wide range of applications, the classical venturi tube of common Venturi tube mixer Wei Yige throat perforate, main flow fluid is flow through by classical venturi tube, introducing fluid flows into through single perforate, utilize the pressure variation of two kinds of fluids will introduce fluid and main flow blending of falling liquid film, existing venturi mixer is comprised of main flow Venturi tube and single inlet tube, if main current flow rate of flow of fluid is too high or flow is excessive, near main flow fluid center line can not mix fully with introducing fluid, introduce fluid and can not flow near the main current flow tagma of center line, easily there is the problem that mixing efficiency is low, and due to the existence in boundary layer, rate of flow of fluid near wall place is lower, therefore easily occur that fluid mixes uneven phenomenon.
Utility model content
For solving above-mentioned problems of the prior art, the Venturi blender that provides a kind of throat to contain special inlet tube is provided the purpose of this utility model, not only improved main flow fluid and introduced near the mix situation of fluid center line, also destroyed the boundary layer of fluid-mixing, having improved near the flow field of throat's wall flows, fully reduced the impact of boundary layer on mixed effect, avoid occurring that main current flow rate of flow of fluid is higher, or introduce the inhomogeneous and low problem of mixing efficiency of mixing that fluid flow causes more greatly, and make the utility model be applicable to the introducing fluid of wider scope and the flowrate proportioning of main flow fluid.
In order to achieve the above object, the technical scheme that the utility model adopts is:
The Venturi blender that special inlet tube is contained in a kind of throat, comprise the main flow Venturi tube flow ipe 1 being connected successively, main flow Venturi tube converging transition 2, main flow Venturi tube throat 3, main flow Venturi tube diffuser 5 and main flow Venturi tube flow out pipeline 6, in described main flow Venturi tube throat 3, be provided with symmetrical, the first inlet tube 7 being communicated with main flow Venturi tube throat 3 tilting to main flow Venturi tube diffuser 5, the second inlet tube 8, the 3rd inlet tube 9 and the 4th inlet tube 10, described the first inlet tube 7, the second inlet tube 8, the 3rd inlet tube 9 and the 4th inlet tube 10 centers have introduces the perforate 4 that fluid flows into.
Described the first inlet tube 7, the second inlet tube 8, the 3rd inlet tube 9 and the 4th inlet tube 10 are arranged on main flow Venturi tube throat 3 and apart from main flow fluid, flow into the 1/2L of end, and wherein L is the length of venturi mixer throat.
Described the first inlet tube 7, the second inlet tube 8, the 3rd inlet tube 9 and the 4th inlet tube 10 are all 21.6 ° with horizontal axis.
The fluid that described the first inlet tube 7, the second inlet tube 8, the 3rd inlet tube 9 and the 4th inlet tube 10 are introduced converges at 1/5L place, upstream, main flow Venturi tube throat center, form and liquidate, and wherein L is the length of venturi mixer throat.
Described main flow Venturi tube flow ipe 1, main flow Venturi tube converging transition 2, main flow Venturi tube throat 3, main flow Venturi tube diffuser 5, main flow Venturi tube flow out pipeline 6 and are revolving body.
Compared to the prior art, the utlity model has following advantage:
The fluid introduction structure of the utility model venturi mixer throat is comprised of special inlet tube, overcome the low shortcoming of original venturi mixer mixing efficiency, effectively improved the mixing efficiency of venturi mixer, compare with the single inlet tube of tradition, the jet that the fluid that 4 introducing modes that liquidate are introduced from different azimuth produces can interact, the distribution of introducing fluid is more even, has strengthened perturbation action, has avoided mixing the appearance of uneven phenomenon.If main current flow rate of flow of fluid is too high or flow is excessive, near main flow fluid center line can not mix fully with introducing fluid, in main flow Venturi tube central area, easily form " giving up the idea ", introduce fluid and can not flow near the main current flow tagma of center line, four inlet tubes described in the utility model are all 21.6 ° of angles with main flow Venturi tube horizontal axis, the mode that inlet tube is in tilted layout makes the flow path direction that comes of main flow fluid and introducing fluid be certain angle, the fluid that described four inlet tubes are introduced is all located to converge in main flow Venturi tube throat 3 center, upstream 1/5L (L is the length of venturi mixer throat), and form strong reversed hedge, make the fluid in pipe more easily change turbulent flow into, having improved near the flow field of throat's wall flows, destroyed original boundary layer, fully reduced the impact of boundary layer on mixed effect, improve main flow fluid and introduced near the mixed effect of fluid center line, avoid occurring that main current flow rate of flow of fluid is higher, or introduce the inhomogeneous and low problem of mixing efficiency of mixing that fluid flow causes more greatly, make main flow fluid more even with mixing of introducing fluid, strengthened the mixed effect of main flow Venturi tube, make the utility model be applicable to the introducing fluid of wider scope and the flowrate proportioning of main flow fluid.
Accompanying drawing explanation
The generalized section of the venturi mixer that special inlet tube is contained in Tu1Wei the utility model throat.
The side view of the venturi mixer that special inlet tube is contained in Tu2Wei the utility model throat.
Fig. 3 is the partial schematic diagram of the utility model inlet tube.
The specific embodiment
Below in conjunction with the drawings and specific embodiments, the utility model is described in further detail.
As depicted in figs. 1 and 2, the Venturi blender that special inlet tube is contained in a kind of throat of the utility model, comprise the main flow Venturi tube flow ipe 1 being connected successively, main flow Venturi tube converging transition 2, main flow Venturi tube throat 3, main flow Venturi tube diffuser 5 and main flow Venturi tube flow out pipeline 6, in described main flow Venturi tube throat 3, be provided with symmetrical, the first inlet tube 7 being communicated with main flow Venturi tube throat 3 tilting to main flow Venturi tube diffuser 5, the second inlet tube 8, the 3rd inlet tube 9 and the 4th inlet tube 10, described the first inlet tube 7, the second inlet tube 8, the 3rd inlet tube 9 and the 4th inlet tube 10 centers have introduces the perforate 4 that fluid flows into.If main current flow rate of flow of fluid is too high or flow is excessive, near main flow fluid center line can not mix fully with introducing fluid, in main flow Venturi tube central area, easily form " giving up the idea ", introduce fluid and can not flow near the main current flow tagma of center line, the angle of inlet tube described in the utility model and main flow venturi mixer horizontal axis is 21.6 °, the mode that inlet tube is in tilted layout makes the flow path direction that comes of main flow fluid and introducing fluid be certain angle, main flow fluid flow through throat 3 with introduce fluid and locate to converge at main flow Venturi tube throat upstream center 1/5L (L is the length of venturi mixer throat), liquidate, strengthened the flow-disturbing effect in this region, impel jet to involve whole throat section, form strong reversed hedge, make the fluid in main flow Venturi tube produce strong disturbance, its perturbation action makes the fluid in pipe more easily change turbulent flow into, improve fully main flow fluid and introduced near the mixed effect of fluid center line, not only make former central area " giving up the idea " to disappear, also fully reduced the impact of boundary layer on mixed effect, 4 introducing modes that liquidate are introduced fluid from different azimuth, the jet producing can interact, strengthened perturbation action, further strengthened mixed effect, avoided mixing the appearance of uneven phenomenon, expanded the scope of application of venturi mixer.
As preferred embodiment of the present utility model, as shown in Figure 3, described the first inlet tube 7, the second inlet tube 8, the 3rd inlet tube 9 and the 4th inlet tube 10 are arranged on main flow Venturi tube throat 3 and apart from main flow fluid, flow into the 1/2L of end, and the fluid that described the first inlet tube 7, the second inlet tube 8, the 3rd inlet tube 9 and the 4th inlet tube 10 are introduced converges at 1/5L place, upstream, main flow Venturi tube throat center, form and liquidate.
As preferred embodiment of the present utility model, as shown in Figure 3, described the first inlet tube 7, the second inlet tube 8, the 3rd inlet tube 9 and the 4th inlet tube 10 are all 21.6 ° of angles with horizontal axis, 4 introducing modes that liquidate make main flow fluid fully mix at throat center with introducing fluid, improve main flow fluid and introduced near the mixed effect of fluid center line, fully reduce the impact of boundary layer on mixed effect, further avoided mixing uneven phenomenon.
As preferred embodiment of the present utility model, described main flow Venturi tube flow ipe 1, main flow Venturi tube converging transition 2, main flow Venturi tube throat 3, main flow Venturi tube diffuser 5, main flow Venturi tube flow out pipeline 6 and are revolving body, are convenient to processing.