CN203517122U - Collection water segregator with gradual enlarging water inlet pipe and with water inlet and outlet pipes arranged in dissymmetric mode - Google Patents

Abstract

The utility model provides a collection water segregator with a gradual enlarging water inlet pipe and with water inlet and outlet pipes arranged in dissymmetric mode, and belongs to the technical field of water current gathering and dispensing equipment. The collection water segregator with the gradual enlarging water inlet pipe and with the water inlet and outlet pipes arranged in dissymmetric mode comprises an equal-diameter water inlet pipe, a gradual enlarging pipe, a collection water segregator tank and a water outlet pipe, and is characterized in that the gradual enlarging pipe is arranged between the equal-diameter water inlet pipe and the collection water segregator tank, the divergence angle of the gradual enlarging pipe is 8-16 degrees, the equal-diameter water inlet pipe is connected with the gradual enlarging pipe, the gradual enlarging pipe is connected with the collection water segregator tank, the outlet diameter of the gradual enlarging pipe is larger than the inlet diameter of the gradual enlarging pipe, the inlet diameter of the gradual enlarging pipe is equal to the diameter of the equal-diameter water inlet pipe, and the outlet diameter of the gradual enlarging pipe is smaller than the diameter of the collection water segregator tank. According to the collection water segregator, the water inlet pipe and the water outlet pipe are connected onto the wall of the collection water segregator tank in dissymmetric arrangement mode, the water inlet and outlet pipes are reasonably arranged, the water inlet and outlet pipes are reasonably selected when the collection water segregator runs, and therefore energy loss caused by direct impact of water currents in the collection water segregator tank is avoided. The gradual enlarging pipe is used on the collection water segregator for water inflow, and the water inlet and outlet pipes are reasonably arranged in dissymmetric mode, and therefore vibration of the collection water segregator tank and the pipels is greatly reduced, water delivery efficiency is improved, and furthermore the collection water segregator ensures that running of a collection water segregator water delivery device is safe, stable and efficient.

Description

A kind of condensate correcting-distribuing device that adopts flaring intake pipe, turnover water pipe asymmetric arrangement

Technical field

The utility model relates to a kind of condensate correcting-distribuing device, relates to particularly a kind of condensate correcting-distribuing device that adopts flaring intake pipe, turnover water pipe asymmetric arrangement, belongs to water supply, heating field.

Background technique

At present, the condensate correcting-distribuing device inlet tube and outlet tube adopting in engineering adopts isometrical straight tube conventionally.Isometrical straight tube and middle condensate correcting-distribuing device tank linkage structure are simple, but the diameter that enters condensate correcting-distribuing device tank due to intake pipe is less, flow velocity and momentum that water delivery enters condensate correcting-distribuing device tank are larger, and flow section sudden enlargement, produce large-scale separation of flow vortex, flow extremely unstable, intake pipe goes out stream and condensate correcting-distribuing device tank is impacted serious, vortex causes condensate correcting-distribuing device vibration aggravation, and condensate correcting-distribuing device fixed bearing and condensate correcting-distribuing device tank and pipeline itself easily damage.Condensate correcting-distribuing device inlet and outlet pipe lines arranges that when unreasonable, condensate correcting-distribuing device tank water flow inside easily liquidates, and causes flow energy loss serious.

Model utility content

The purpose of this utility model is exactly the deficiency existing for above-mentioned existing condensate correcting-distribuing device, by theory analysis and flow numerical simulation, carry out innovative design, provide a kind of rational in infrastructure, the condensate correcting-distribuing device of flaring intake pipe, turnover water pipe asymmetric arrangement is stablized, adopted efficiently to security of operation.

The purpose of this utility model is achieved in that a kind of condensate correcting-distribuing device that adopts flaring intake pipe, turnover water pipe asymmetric arrangement, as shown in Figure 3, by current order, straight intake pipe, increaser, condensate correcting-distribuing device tank, outlet pipe four parts such as comprises.It is characterized in that, at straight intake pipe such as described grade and the tank connected end of condensate correcting-distribuing device, adopt increaser, increaser outlet diameter is greater than inlet diameter, increaser inlet diameter is identical with isometrical intake pipe diameter, increaser outlet diameter is less than or is slightly smaller than condensate correcting-distribuing device tank diameter, and the bilateral angle of flare of increaser is 8 °～16 °.Isometrical intake pipe connects increaser import, and increaser outlet connects condensate correcting-distribuing device tank.

The utility model adopts increaser to be connected with condensate correcting-distribuing device tank at condensate correcting-distribuing device intake pipe end, guarantee that increaser had both had enough angles of flare, along with increaser area of passage constantly increases, in increaser, flow rate of water flow constantly reduces, minimum at increaser outlet port flow rate of water flow, and go out stream and be flaring shape, reduced the flow velocity that outlet pipe water outlet enters condensate correcting-distribuing device tank, thereby reduce its shock to condensate correcting-distribuing device tank, guarantee again the diffusion loss of head that unlikely generation is larger.On the other hand, owing to entering the flow rate of water flow of condensate correcting-distribuing device tank by increaser, greatly reduce, and what enter condensate correcting-distribuing device tank is gradually expanding shape current, the intensity of the separation of flow vortex that while greatly having reduced the straight intake pipes such as employing, the sudden enlargement of condensate correcting-distribuing device tank internal cause flow section causes.

During condensate correcting-distribuing device design, inlet tube and outlet tube asymmetric arrangement is connected on condensate correcting-distribuing device tank skin, requirement is flowed out from intake pipe the current enter condensate correcting-distribuing device tank and in condensate correcting-distribuing device tank, along equidirectional, is flowed to outlet pipe import and enter outlet pipe, while avoiding moving in condensate correcting-distribuing device tank current liquidate, consumed energy.

Vibration when this model utility can effectively alleviate condensate correcting-distribuing device operation, improves emptying effectiveness, guarantees condensate correcting-distribuing device water delivery device safety, stable, efficiently operation, is specially adapted to the place that condensate correcting-distribuing device can not fixedly secure.

Use ANSYS CFX software, adopt the common condensate correcting-distribuing device of standard k-ε turbulence model numerical calculation, adopt the condensate correcting-distribuing device of increaser and the condensate correcting-distribuing device interior flow field that increases condensate correcting-distribuing device tank diameter.By analytic set water knockout drum interior flow field, further analyze intake pipe outlet port current to condensate correcting-distribuing device influence of vibration.

Condensate correcting-distribuing device of the present utility model can be widely used in the engineerings such as HVAC and water supply, application attestation, adopt the condensate correcting-distribuing device significant reduction in vibration of flaring intake pipe, even disappear, guaranteed that condensate correcting-distribuing device is stable, safety and reliable operation, inlet tube and outlet tube asymmetric arrangement has reduced hydraulic loss, remarkable in economical benefits simultaneously.

Condensate correcting-distribuing device internal flow numerical computation method comprises following step:

A. according to the concrete size of condensate correcting-distribuing device that adopts condensate correcting-distribuing device, common condensate correcting-distribuing device and the increase condensate correcting-distribuing device tank diameter of increaser, adopt above-mentioned multi-form condensate correcting-distribuing device numerical calculation model, wherein Fig. 2 turnover water pipe diameter is that 0.2m, condensate correcting-distribuing device tank diameter are 0.35m, and Fig. 3 turnover water pipe diameter is that 0.2m, condensate correcting-distribuing device tank diameter are 0.5m.

B. the geometric model of having set up is carried out to non-structured grid division, in water-in and water-out pipeline and the local cypher of condensate correcting-distribuing device tank joining place.

C. the governing equation of numerical calculation comprises equation of continuity, momentum conservation equation, adopts k-ε turbulence model.

Equation of continuity $\frac{\∂\mathrm{\ρ}}{\∂t}+\▿\·\left(\mathrm{\ρu}\right)=0---\left(1\right)$

Momentum conservation equation $\frac{\∂\left(\mathrm{\ρ}{u}_i\right)}{\∂t}+\frac{\∂\left(\mathrm{\ρ}{u}_i{u}_j\right)}{\∂x_j}=\mathrm{\ρ}{f}_i-\frac{\∂p}{\∂x_i}+\frac{\∂{\mathrm{\τ}}_{\mathrm{ij}}}{\∂x_j}---\left(2\right)$ In formula: ρ is fluid density; P is fluid micellar pressure; u _i, f _i, x _ibe respectively speed, unit mass power and the coordinate of i direction; τ _ijfor fluid micellar surface viscosity shearing stress component.

K equation: $\frac{\∂}{\∂x_j}[\mathrm{\ρ}{v}_{j}k-(\mathrm{\μ}+\frac{{\mathrm{\μ}}_t}{{\mathrm{\σ}}_k})\frac{\∂k}{\∂x_j}]=\mathrm{\ρ}(p_k-\mathrm{\ϵ})---\left(3\right)$

ε equation: $\frac{\&PartialD;}{\&PartialD;x_j}[\mathrm{\&rho;}{v}_j\mathrm{\&epsiv;}-(\mathrm{\&mu;}+\frac{{\mathrm{\&mu;}}_t}{{\mathrm{\&sigma;}}_{\mathrm{\&epsiv;}}})\frac{\&PartialD;\mathrm{\&epsiv;}}{\&PartialD;x_j}]=\mathrm{\&rho;}\frac{\mathrm{\&epsiv;}}{k}(C_{\mathrm{\&epsiv;}1}{p}_k-C_{\mathrm{\&epsiv;}2}\mathrm{\&epsiv;})---\left(4\right)$ In formula: μ _tfor whirlpool group coefficient of viscosity, ${\mathrm{\&mu;}}_t=C_{\mathrm{\&mu;}}\frac{{\mathrm{<figure-callout\; id="2"\; label="k"\; filenames="131019145441.png"\; state="\{\{state\}\}">k</figure-callout>}}^2}{\mathrm{\&epsiv;}};$ P _kfor tubulence energy generating item, $p_k=\frac{{\mathrm{\&mu;}}_t}{\mathrm{\&rho;}}(\frac{\&PartialD;v_i}{\&PartialD;v_j}+\frac{\&PartialD;v_j}{\&PartialD;v_i})\frac{\&PartialD;v_i}{\&PartialD;v_j};$ Empirical coefficient C _{1 ε}=1.44, C _{2 ε}=1.92, C _μ=0.09, σ _k=1.0, σ _ε=1.3

D. the finite volume method of the discrete employing staggered mesh of equation.By variable p, k, ε, α is placed in control volume center, speed control volume and pressure control volume interlaced arrangement, the discrete employing power function of convection current-diffusion term.

E. given computational domain boundary conditions.This computational domain adopts quality import, pressure export, flows and adopt Wall-function in pipeline near-wall region, and wall adopts without slippage, adiabatic boundary condition.

F. the multi-form condensate correcting-distribuing device internal flow of numerical calculation, and result of calculation is studied, analyzed.

By more multi-form condensate correcting-distribuing device interior flow field, analyze the impact of water impact effect on multi-form condensate correcting-distribuing device operation.

Accompanying drawing explanation

Fig. 1 is common condensate correcting-distribuing device structural representation.

Fig. 2 is for increasing the condensate correcting-distribuing device structural representation of condensate correcting-distribuing device tank diameter.

Fig. 3 is the condensate correcting-distribuing device structural representation that the utility model adopts increaser water inlet.

Fig. 4 is common condensate correcting-distribuing device by-level longitudinal section velocity flow profile schematic diagram.

Fig. 5 is for increasing the condensate correcting-distribuing device by-level longitudinal section velocity flow profile schematic diagram of condensate correcting-distribuing device tank diameter.

Fig. 6 is the condensate correcting-distribuing device by-level longitudinal section velocity flow profile schematic diagram that the utility model adopts increaser water inlet.

In figure: 1 intake pipe, 2 increasers, 3 condensate correcting-distribuing device tanks, 4 outlet pipes.

Embodiment

Adopt a condensate correcting-distribuing device for flaring intake pipe, turnover water pipe asymmetric arrangement, by etc. straight intake pipe, increaser, condensate correcting-distribuing device tank and outlet pipe etc. form.Etc. being provided with increaser between straight intake pipe and condensate correcting-distribuing device tank, intake pipe connects increaser, and increaser connects condensate correcting-distribuing device tank, and the outlet diameter of increaser is greater than inlet diameter, the inlet diameter of increaser is identical with intake pipe diameter, and increaser outlet diameter is less than condensate correcting-distribuing device tank diameter.The angle of flare of increaser is 8 °～16 °.Intake pipe and outlet pipe asymmetric arrangement are connected on condensate correcting-distribuing device tank skin, and turnover water pipe adopts asymmetric arrangement, avoids opposite jet flow off-energy.

Below in conjunction with concrete case, calculate interior flow field, analytic explanation feature of the present utility model and effect.But present case should not be construed as restriction of the present utility model.

Condensate correcting-distribuing device is established 4 intake pipes, and 3 outlet pipes adopt 3 intake pipe water inlets while normally moving, and another 1 intake pipe is as standby.Adopt method for numerical simulation to calculate condensate correcting-distribuing device interior flow field as Fig. 4～Fig. 6.Fig. 4 is velocity flow profile in common condensate correcting-distribuing device pipe level central longitudinal section.By Fig. 4, known, because condensate correcting-distribuing device tank diameter is less, intake pipe outlet port flow velocity is larger, and current are stronger to condensate correcting-distribuing device tank internal face percussion, and in tank, separation of flow whirlpool is stronger, flows very unstable.By Fig. 5, known, by condensate correcting-distribuing device tank enlarged diameter, during to 0.5m, in the tank of intake pipe outlet port, flow velocity slightly reduces compared with Fig. 4, and current slightly weaken condensate correcting-distribuing device tank skin face percussion.By Fig. 6, known, adopt the condensate correcting-distribuing device of increaser water inlet, increase along with increaser flow section, flow velocity in increaser constantly reduces, and the flow velocity in increaser outlet port is significantly less than the flow velocity in Fig. 4 and the common condensate correcting-distribuing device intake pipe of Fig. 5 outlet port, and current are diffusion outflow, after entering condensate correcting-distribuing device tank, spread rapidly, impact to tank skin obviously reduces, and the current of rapidly diffusion are full of space in tank very soon, has obviously reduced the intensity of separation of flow vortex.Application shows, the vibration while adopting the condensate correcting-distribuing device operation of increaser water inlet obviously reduces, and even disappears.Condensate correcting-distribuing device inlet and outlet pipe lines reasonable Arrangement, has avoided condensate correcting-distribuing device water flow inside to liquidate, and has reduced energy loss, has improved emptying effectiveness.

Claims (4)

1. a condensate correcting-distribuing device that adopts flaring intake pipe, turnover water pipe asymmetric arrangement, straight intake pipe, increaser, condensate correcting-distribuing device tank and the outlet pipe such as comprise, it is characterized in that, condensate correcting-distribuing device tank has adopted flaring intake pipe, and condensate correcting-distribuing device tank inlet tube and outlet tube adopts asymmetric arrangement.

2. a kind of condensate correcting-distribuing device that adopts flaring intake pipe, turnover water pipe asymmetric arrangement according to claim 1, it is characterized in that, between straight intake pipe such as described grade and condensate correcting-distribuing device tank, be provided with increaser, etc. straight intake pipe, connect increaser, increaser connects condensate correcting-distribuing device tank, the inlet diameter of increaser with etc. straight intake pipe diameter identical, increaser outlet diameter is less than condensate correcting-distribuing device tank diameter.

3. a kind of condensate correcting-distribuing device that adopts flaring intake pipe, turnover water pipe asymmetric arrangement according to claim 1, is characterized in that, the angle of flare of described increaser is 8 ° ~ 16 °.

4. a kind of condensate correcting-distribuing device that adopts flaring intake pipe, turnover water pipe asymmetric arrangement according to claim 1, it is characterized in that, described intake pipe and outlet pipe asymmetric arrangement are connected on condensate correcting-distribuing device tank skin, reasonable Arrangement inlet tube and outlet tube, choose reasonable inlet tube and outlet tube during operation, avoids opposite jet flow in condensate correcting-distribuing device tank to cause energy loss.

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