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In the present paper an extensive study of rectangular cross-sectioned C-duct and C-diffuser is made by the help of 2-D mean velocity contours. Study of flow characteristics through constant area duct is a fundamental research area of basic fluid mechanics since the concepts of potential flow and frictional losses in conduit flow were established. C-ducts are used in aircraft intakes, combustors, internal cooling systems of gas turbines, ventilation ducts, wind tunnels etc., while diffuser is mechanical device usually made in the form of a gradual conical expander intended to raise the static pressure of the fluid flowing through it. Flow through curved ducts is more complex compared to straight duct due to the curvature of the duct axis and centrifugal forces are induced on the flowing fluid resulting in the development of secondary motion (normal to the primary flow direction) which is manifested in the form of a pair of contra-rotating vortices. For a diffuser in addition to the secondary flow, the diverging flow passage, which causes an adverse stream wise pressure gradient, can lead to flow separation. The combined effect may result n non uniformity of total pressure and total pressure loss at the exit. A comparative study of different turbulent models available in the Fluent using y as guidance in selecting the appropriate grid configuration and turbulence models are done. Standard k-ε model and RSM models are used to solve the closure problem for both the constant area duct and the diffuser. It has been observed that the Standard k-e model predicts the flow through the constant area duct and the diffuser within a reasonable domain of the y range.
2008
The development of bounded flows with streamwise curvature in curved ducts and diffusers are distinguished by the generation of streamwise vorticity or 'secondary motion'. The imbalance between radial pressure gradient and centrifugal forces imposed by circular motion forms the secondary motion. The positive streamwise pressure gradient close to the convex surface and the negative streamwise pressure gradient near the concave surface causing a radial pressure gradient. This leads to fluid acceleration closer to the convex surface and deceleration closer to the concave surface. In the present study; computations of two-and three-dimensional turbulent curved flows through two types of square sectioned U-bend duct flows (with mild and strong curvatures) and through 180° curved diffuser have been carried out using five turbulence models, provided in the FLUENT code.
S-shaped diffusing ducts are extensively used in aircrafts. These ducts normally operate at steady and symmetric conditions but, during some maneuvers, the nature of inlet flow (inflow) ingested by the S-duct may vary with the conditions. Similarly, due to space constraint in aircraft design, the diffusers may need to be curved to a great extent. An attempt has been made to computationally analyze the combined effects of inflow conditions and turning angles () on the overall performance of rectangular S-duct rectangular diffusers with area ratio of 1.33. The detailed investigations are carried out using a finite-volume technique based commercial CFD code FLUENT using RNG kε turbulence model. The effects of various inflow conditions, namely experimental, uniform and turbulent, to same area ratio (1.33) S-duct diffusers but with different turning angles ( = 20, 40 and 60) are studied. The results show that the duct performance in terms of static pressure recovery reduces with ...
Computers & Fluids, 1994
Almtract-A numerical study of turbulent flow in a straight duct of square cross-section is made. An order-of-magnitude analysis of the 3-D, time-averaged Navier-Stokes equations resulted in a parabolic form of the Navier-Stokes equations. The governing equations, expressed in terms of a new vectorpotential formulation, are expanded as a multi-deck structure with each deck characterized by its dominant physical forces. The resulting equations are solved using a finite-element approach with a bicubic element representation on each cross-sectional plane. The numerical integration along the streamwise direction is carded out with finite-difference approximations until a fully-developed state is reached. The computed results agree well with other numerical studies and compare very favorably with the available experimental data. One important outcome of the current investigation is the interpretation analytically that the driving force of the secondary flow in a square duct comes mainly from the second-order terms of the difference in the gradients of the normal and transverse Reynolds stresses in the axial vorticity equation. NOMENCLATURE CI =Empirical value of 1.5 from Ref. [16] for turbulence modeling, equations (5) C~ = Value of 0.090 for k-~ modeling, equations (8) Cd = Value of 1.44 for k~ modeling, equations (8) Ca = Value of 1.92 for k~ modeling, equations (8) Cf=Dimensionless skin friction coefficient, 2f,,/ put Dh = Hydraulic diameter of the square duct k = Non-dimensional turbulence kinetic energy Ll = Streamwise length scale (duct length) for nondimensionalizing purposes, O (L2/ LL) = /-2-Dh, Transverse streamwise length scale for non-dimensionalizing purposes L' = Turbulent characteristic length for non-dimensionalizing purposes, (L "/ L2
1978
of 105 and an inlet Mach number of 0.1. One case had a circular cross section, the other an elliptic cross section with shape factor 1.1. Flow in an axisymmetric diffuser and in a transition duct are additional cases discussed for completeness.
2017
1M.Tech Scholar, Government Engineering College, Jagdalpur 2Assistant professor, Dept. of Mechanical Engineering, GEC Jagdalpur, Chhattisgarh, India 3Lecturer, Dept. of Mechanical Engineering, GEC Jagdalpur, Chhattisgarh, India ---------------------------------------------------------------------***--------------------------------------------------------------------Abstract In this paper, a three dimensional comparative CFD analysis of an three arbitrary cross sectional pipe i.e. circular, triangular and rectangular pipe have been performed. While analysis the flow, all the three pipes have same cross sectional area so that the fully developed flow can be visualized. The partial differential governing equation i.e Naiver stokes equation has been solved by using computational FEV solver tool i.e. ANSYS Fluent. Through this investigation fully developed turbulent flow in arbitrary shaped pipe has been studied for higher Reynolds number. During analysis k-ε turbulence model has been se...
Journal of the American Helicopter Society
Several rotorcraft applications such as circulation control and tip jet-driven rotors involve internal spanwise flow along a ducted rotor blade. The primary goal of this work was to study a self-pumping pneumatically driven duct flow by both generating a quasi one-dimensional model for such flows and providing a validation data set for rotorcraft applications. The flow behavior inside a 1.32-m-long cylindrical duct, with a duct cross-sectional diameter of 52 mm, and rotating at speeds up to 1050 RPM was studied. Spanwise pressure distribution, duct velocity, hub forces, and moments from the numerical model showed good correlation with experiments. A considerable internal mass flow rate (∼0.3 kg/s) was also observed for a steadily rotating duct. In the presence of a time-varying valve at the inlet, transient spanwise pressure variations showed periodic fluctuations in pressure that diminished once the valve was fully open. The experimental results were compared with results of two computational models-a quasi one-dimensional finite volume Euler equation solver and a full threedimensional computational fluid dynamics solver. The ability to model a range of boundary conditions, time-varying duct cross-sectional area to simulate a flow control valve, frictional losses, duct sweep, and centrifugal as well as Coriolis effects on the flow is included. The experiments revealed key information about pressure at the duct's outlet. It was observed that when the duct's inlet is closed, the duct's outlet pressure is less than its ambient value. The knowledge of these boundary conditions is key in modeling flow through rotating ducts.
S-duct diffusers are widely used in air-intake system of several jet aircrafts to get less drag and lowering the engine position compared to straight through design. In this study the distorted flow condition parameter like static pressure recovery and total pressure loss are investigated by adding vortex generators. Geometry selected based on fox and Kline on linear area-ratio from inlet to exit. Modeling CATIA V5 is used for design of diffuser and ANSYS fluent are employed in the investigation of S-Duct and S-Duct with SVG in different locations for the Mach number values of 0.6 and 1.0 to improve the total pressure recovery of the S-duct. From the results 3 SVG pairs attached to both the sidewalls at plane-4 and SVG in top and bottom of inflexion planes offers the best performance. The design objective is to improve the static pressure recovery of the S-duct and reduce the total pressure loss.
Journal of emerging technologies and innovative research, 2021
Air conditioning systems are considered operating successfully based on the efficient supply of air in the air-conditioned space. Estimation of pressure losses in ducts is vital for the selection of duct size. The installation cost of duct in air conditioning system is about 20 to 30% of the total cost of equipment selection and power consumption of supply fans also adds to the running cost. Hence, it's important to minimize the capital and running cost of the duct system. Duct design is the design of enclosed passage for supplying conditioned air and then distributing the sir to specified areas according to the need. There are various advantages of efficiently designed and constructed interior ducts. One of the advantages is enhanced energy efficiency through the cancellation of duct leakage and reducing conductive heat gains/losses. This paper focuses on a study of design and improving air duct using computational fluid dynamics (CFD) analysis considering all the parameters related to air flow and its characteristics for enhancing duct system efficiency. The necessity of optimization of duct system is to improve supply air flow. It integrates theoretical and software tools to provide detailed comparative analysis of the advantages involved in selecting a particular shape (rectangular duct with Y-shaped bend and with 90-degree corner with sharp bend) of duct for a specified conditions. The focus of this paper will be on using CFD simulation tools to study velocity distribution of air in the duct at various sections, pressure difference at various outlets and distributions of air flow.
This paper presents the results of an experimental work with measurement of wall static pressure of 90°C shaped Curved duct. The test duct is made up of transparent perspex sheets to facilitate the flow visualization study. The duct has an inlet to exit area ratio of 1.0 with centerline distance of 750 mm. The inlet aspect ratio of the test duct has been fixed at 1.0. The velocities for the proposed investigations are to be measured by using a Pitot tube.Wall pressures are measured with the help of an inclinedmanometer with the inclination of 35°. The manometer had two tubes emanating from it: one left open to the atmosphere and the other connected to the steel pipes attached to the four walls of the curved duct. The difference in the readings helped us calculate the static pressure and thereby the normalized pressure. Wall pressure distribution along the curved and parallel walls of the duct at 0°, 22.5°, 45°, 67.5° and 90° measuring sections was measured. All the experimental data has been processed by an Intel i3 CPU, 3 GB RAM PC and analyzed to give the distribution of static pressure in the square duct.The main purpose of this investigation is to show the development of secondary flow which happens when the flow takes place through the bend in the curvature. This secondary flow arises as a result of a centrifugal force acting when the flow moves through the bend. The investigation is carried out at three different velocities 20 m/s, 40 m/s and 60 m/s. The distribution of normalized pressure which is the ratio of static pressure to the dynamic pressure is mapped and shown in the form of contours by using the software package SURFER.The trend of wall static pressure development on the walls of C shaped duct shows that as the flow proceeds towards the curvature, there exists a high pressure gradient between the outside face and inside face due the centrifugal force acting along the curvature. This shows the bulk shifting of flow towards the inside face. This is due to the generation of secondary motion in a plane perpendicular to the primary flow.
Journal of Fluid Mechanics, 1972
The paper presents the outcome of experimental research on turbulence-induced secondary flows in square-sectioned ducts. The main emphasis of the experiments has been on the measurement of the secondary flows in a duct with equally roughened surfaces. Here the secondary flow is a substantially larger proportion of the axial flow than is the case in smooth-walled ducts. With the secondary velocities normalized by the friction velocity, however, the resultant profiles for smooth and rough surfaces are the same, within the precision of the measurements.
This paper presents the observations of an experimental work dealing with the measurement of normalized mean velocity and wall static pressure of a 90° C-shaped curved duct. The test duct is made up of transparent perspexsheet to facilitate the flow visualization study. The duct has a centerline distance of 750mm. The Inlet and Outlet aspect ratio of the test duct used is 1.0. Wall pressures are measured with the help of an inclined manometer withthe inclination of 35°. The manometer had two tubes emanating from it: one left open to the atmosphere and the other connected to the steel pipes attached to the four walls of the curved duct. The difference in the readings helped calculate the static pressure and thereby the normalized pressure. Wall pressure distribution along the curved and parallel walls of the duct at 0°, 22.5°, 45°, 67.5° and 90° measuring sections was measured. The investigation for wall static pressure distribution is carried out at the velocity of 40m/s. This paper also presents an experimental work carried out with measurement of normalized mean velocity of the mentioned curved square C shaped duct, taken at the same velocity. The trend of the normalized mean velocity contour development inside the C duct shows continuous decrease of the normalized velocity as we move from the Inlet Section towards the Outlet Section. The distribution of wall static pressure and normalized mean velocity contours are mapped by using SURFER software package. The trend of wall static pressure development on the walls of C shaped duct shows that as the flow proceeds towards the curvature, there exists a high pressure gradient between the Outside Face and Inside Face due the centrifugal force acting along the curvature. This shows the bulk shifting of flow towards the Inside Face. This is due to the generation of secondary motion in a plane perpendicular to the primary flow. The main purpose of this investigation is to show the development of secondary flow which happens when the flow takes place through the bend in the curvature. This secondary flow arises as a result of a centrifugal force acting when the flow moves through the bend.
2007
Curved channels are very often present in real hydraulic systems, e.g. curved diffusers of hydraulic turbines, Sshaped bulb turbines, fittings, etc. Curvature brings change of velocity profile, generation of vortices and production of hydraulic losses. Flow simulation using CFD techniques were performed to understand these phenomena. Cases ranging from single elbow to coupled elbows in shapes of U, S and spatial right angle position with circular cross-section were modeled for Re = 60000. Spatial development of the flow was studied and consequently it was deduced that minor losses are connected with the transformation of pressure energy into kinetic energy and vice versa. This transformation is a dissipative process and is reflected in the amount of the energy irreversibly lost. Least loss coefficient is connected with flow in U-shape elbows, biggest one with flow in S-shape elbows. Finally, the extent of the flow domain influenced by presence of curvature was examined. This is impo...
International Journal of Aerodynamics, 2010
A computational investigation is carried out to study the flow and performance characteristics of a Y-shaped diffusing duct having two inlets and one outlet with an overall area ratio of 2 using a commercial CFD code, FLUENT. The CFD code is validated with the experimental results and it was found that the code applying the RNG k-e turbulence model has the capability of predicting the flow and performance characteristics for the similar geometry. The Y-shaped diffusing duct is formed by merging two symmetrical S-shaped diffusing ducts (area ratio = 4, curvilinear length = 600 mm, angle of turn = 22.5°/22.5°) at the centreline of outlet. The flow and performance characteristics of the duct are analysed for a uniform flow profile at the inlet that is observed in the experiments. The results are presented in the form of contour plots for the axial velocity distribution and the cross-flow velocity distribution in terms of vector plots. The analysis reveals the fact that however the flow at the diffuser inlet is uniform, secondary flows are induced as an effect of curvature and change in the cross-sectional area.
International Journal of Turbo & Jet-Engines, 2019
The effect of aspect ratio (AS = 0.5, 1.0, 2.0) and Reynolds number (Re = 1, 2, 4, 8 × 105) on the flow and performance characteristics of a 90° curved rectangular diffuser was examined with the aid of the commercial CFD code ANSYS FLUENT. The results from computational analysis revealed the presence of stream vorticity indicative of secondary flow brought about by the curvature of the diffusing duct. As the fluid flow developed, the inertial core flow was pushed to the outer concave wall by overbearing centrifugal forces. The fluid flow sustained marginal changes with increasing aspect ratio and Reynolds number. However, the flow uniformity at the exit was enhanced. The rise in coefficient of static pressure (Cp) recovery and the drop in coefficient of total pressure loss (Closs) with increasing Reynolds number suggested improved diffuser performance. The flow uniformity index was found to be the highest for the diffuser of aspect ratio 1.
Transstellar Journals, 2019
This paper discusses about the Flow analysis of Aerospace ducts of Equipment cooling system of an aircraft. Equipment Cooling is provided to maintain assigned temperature conditions in equipment compartment for satisfactory working of Line Replaceable units (LRUs), which are installed inside equipment compartment. Forced air cooling is provided to these LRUs using Air Conditioning system (ACS) air. The life span of aircraft is approximately 30-40 years, and various up-gradations are required to be carried out to meet the operational &mission requirements. Up-gradation programmes of aircraft required installation of new LRUs, thus a requirement of redistribution of flow through complex duct geometries to meet their additional cooling requirements is mandatory. In the present practice, designers carryout the redistribution of flow of air through these complex ducts using Continuity & Bernoulli's equation. It was experienced that new LRUs at so many times not function properly due to inadequate cooling condition resulting malfunctioning of LRUs. This Paper aims to identify the reason for not achieving the designed cooling condition at designated LRUS. To analyse the flow through Aerospace ducts in transient condition, an experimental Environmental Control System (ECS) test rig has been newly designed to simulate the actual layout of installation of Aerospace ducts into aircraft. Theoretical analysis correlated by experimental trials analysis was carried out on Environmental Control System Test Rig. The results analysed and concluded the reason for not achieving the required cooling to LRUs. Notations ρ = Density of air µ = Dynamic Viscosity ν = Kinematic Viscosity m* =Mass flow rate m 13 = air mass flow rate in branch 13 V= Initial Velocity of the air f = Darcy friction factor Re = Reynolds no of flow (h f) 01 = Head loss due To Friction in section 0 to1 h f) 13 = Head loss due To Friction in section 1 to3 V 01 = Mean velocity between section 0 & 1 V 13 = Mean velocity between section 1 & 3. E 0 = Energy at the section 0 E 1 = Energy at the section 1 E 3 = Energy at the section 3 P 0 = Pressure drop at section 0 P 1 = Pressure drop at section 1 P 3 = Pressure drop at section 3 D 01 = Diameter of sections 0 to 1 D 13 = Diameter of sections 1 to 3 A 01 = Area of sections 0 to 1 A 13 = Area of sections 1 to 3 L 01 = Length of sections 0 to 1 L 13 = Length of sections 1 to 3 ε = Surface roughness
Journal of Fluids Engineering, 1990
The pressure driven, fully developed turbulent flow of an incompressible viscous fluid in curved ducts of square cross-section is studied numerically by making use of a finite volume method. A nonlinear K -1 model is used to represent the turbulence. The results for both straight and curved ducts are presented. For the case of fully developed turbulent flow in straight ducts, the secondary flow is characterized by an eight-vortex structure for which the computed flowfield is shown to be in good agreement with available experimental data. The introduction of moderate curvature is shown to cause a substantial increase in the strength of the secondary flow and to change the secondary flow pattern to either a double-vortex or a four-vortex configuration.
2021
In this paper, the velocity and pressure drop distribution in flowing water through circular, square, rectangular with aspect ratio of 2:1 and 4:1 as well as an equilateral triangle cross-sectional ducts with the same duct length and hydraulic diameter have been numerically studied using ANSYS FLUENT tools. The boundary conditions used for the simulation are: at the entrance a velocity inlet of 0.2 m/s at 25 C constant temperature, at exit a pressure outlet with zero gage pressure and a non-slip is used for the duct walls condition. A steady state and kepsilon turbulence flow model is used. The results have shown that velocity in the ducts gradually increases from zero at the walls to the maximum at the center. In the circular duct 20.327%, 15.273%, 13.5% and 6.834% more pressure is lost than in triangular, square, rectangular aspect ratio of 2:1 and rectangular aspect ratio of 4:1 ducts respectively. In turn, circular duct requires the highest pumping power while triangular one nee...
Transstellar Journals, 2019
After burners are employed in an aero engine of a fighter aircrafts, to achieve maximum thrust during takeoff , climb and during some special combat maneuvers. Since the fuel consumption is high during the afterburning operation it is employed only when necessary. The diffuser duct is the first component of the afterburner system, situated immediately next to the exit of the low-pressure turbine. The struts are the supporting structures, which connect the parts of diffuser duct. These struts will guide the flow in the diffuser duct. The presence of the struts will cause some pressure losses. The flow is decelerated in the diffuser duct. The Mach number also reduces along the length of the diffuser. The design of the diffuser duct should be made so that the recirculation should be minimum at the exit of the diffuser and the thermodynamics properties at the exit should meet the requirement for the proper mixing of the fuel and air with the hot gases passing through the diffuser & hence ensures complete combustion in the upstream zones of the diffuser. The flow inside an afterburner is highly complex due to the presence of the diffuser, flame stabilizer, variable area nozzle and the interaction between core and bypass flow through anti-screech holes. Therefore the performance of afterburner depends to a great extent on the internal aerodynamics. Experimental analysis of such flow is a difficult task. Cost and time involved for optimization design are very high. Computational fluid dynamics (CFD) provides a cost effective solution in analyzing. Its suitability to support the combustion process for the design of short efficient reheats system. Hence in this study, the flow in the diffuser duct in details by carrying out the analysis of subsonic flows in a three-dimensional model of an afterburner duct using CFD. The flow in the bypass region of the duct is considered, as it does not have any impact on diffuser performance. In the current study two stages viz. diffuser duct with struts and without struts were carried out and for both cases the pressure recovery, total pressure loss, essential flow properties like Mach number, velocity, statics pressure, swirl are compared for both the cases. Considering the periodicity of geometry, analysis has been carried out using 45-degree sector model of the diffuser duct with and without struts. Using ICEM-CFD pre-processor an unstructured grid has been generated and Navier-stroke equation is applied to carry out using ANSYS CFX CFD software, flow simulated by solving governing equation of mass, momentum, energy. Turbulence closure is achieved with k-epsilon turbulence model with standard wall functions.
Powder Technology, 2009
Gas-solid two-phase flow in 180°curved duct is simulated using a two-way coupling Eulerian-Lagrangian approach. Reynolds averaged Navier-Stokes equations (RANS) and four turbulence models namely; standard k-ε model, RNG (Renormalization Group) based k-ε model, Low-Re k-ε model and an extended version of the standard k-ε model are adopted. The effects of particle rotation and lift forces are included in the particle tracking model. The present predictions are compared with published experimental data for single-phase and two-phase flows. The comparisons show that the RNG based k-ε model predicts the flow behaviour better than other models. Furthermore, the particles concentration and velocity are compared very well with published data. The effects of inlet gas velocity, bend geometry, loading ratio and particle size on the flow behaviour and bend pressure drop are also discussed. The results show that the flow behaviour is greatly affected by these parameters.
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