Analysis of the possibility to optimize the passive pressure pulsations dampers using CFD

Similar documents
ABSTRACT I. INTRODUCTION

[Prasanna m a*et al., 5(6): July, 2016] ISSN: IC Value: 3.00 Impact Factor: 4.116

Predictionof discharge coefficient of Venturimeter at low Reynolds numbers by analytical and CFD Method

Sound attenuation analysis of waterfilled perforated pipe silencers using three-dimensional time-domain computational fluid dynamics approach

Detailed Outline, M E 320 Fluid Flow, Spring Semester 2015

Proceedings of Meetings on Acoustics

Experiment (4): Flow measurement

The Expansibility Factor Equations in ISO and ISO : Do They Deliver What They Promise?

ME 305 Fluid Mechanics I. Part 8 Viscous Flow in Pipes and Ducts. Flow in Pipes and Ducts. Flow in Pipes and Ducts (cont d)

Experimental and Numerical Investigation of Two- Phase Flow through Enlarging Singularity

A Computational Study on the Thrust Performance of a Supersonic Pintle Nozzle

LECTURE 6- ENERGY LOSSES IN HYDRAULIC SYSTEMS SELF EVALUATION QUESTIONS AND ANSWERS

Analysis And Control Of Severe Vibration Of A Screw Compressor Outlet Piping System

Consideration of the pulsation as a design criterion for a newly developed oil-injected process gas screw compressor

Fluid structure interaction dynamic analysis of a mixed-flow waterjet pump

FLOW MEASUREMENT IN PIPES EXPERIMENT

William В. Brower, Jr. A PRIMER IN FLUID MECHANICS. Dynamics of Flows in One Space Dimension. CRC Press Boca Raton London New York Washington, D.C.

Discharge Coefficient Behaviour in Presence of Four Perforated Plates Flow Conditioners

Experimental and CFD analysis of flow through venturimeter to determine the coefficient of discharge

Mechanical Measurements and Metrology Prof. S. P. Venkateshan Department of Mechanical Engineering Indian Institute of Technology, Madras

CFD and Thermal Stress Analysis of Helium-Cooled Divertor Concepts

93. Study on the vibration characteristics of structural of hydrocyclone based on fluid structure interaction

Chemical Engineering 3P04 Process Control Tutorial # 1 Learning goals

FLUID MECHANICS D203 SAE SOLUTIONS TUTORIAL 2 APPLICATIONS OF BERNOULLI SELF ASSESSMENT EXERCISE 1

Applied Fluid Mechanics

ACCOUNTING FOR FRICTION IN THE BERNOULLI EQUATION FOR FLOW THROUGH PIPES

Piping Systems and Flow Analysis (Chapter 3)

ME 305 Fluid Mechanics I. Chapter 8 Viscous Flow in Pipes and Ducts

ABSTRACT I. INTRODUCTION

Engineering Noise Control

Hydraulics and hydrology

APPLIED FLUID DYNAMICS HANDBOOK

1-Reynold s Experiment

Instruction Manual. Equipment for Engineering Education

FLOW MEASUREMENT. INC 102 Fundamental of Instrumentation and Process Control 2/2560

Calibration of Orifice Flow Meter and Venturi Flow Meter

Applied Fluid Mechanics

V/ t = 0 p/ t = 0 ρ/ t = 0. V/ s = 0 p/ s = 0 ρ/ s = 0

Attenuation. Witt&Sohn AG Oct-14

Applied Fluid Mechanics

Lesson 37 Transmission Of Air In Air Conditioning Ducts

Introduction to Chemical Engineering Thermodynamics. Chapter 7. KFUPM Housam Binous CHE 303

A Comparison of Thermal Deformation of Scroll Profiles inside Oil-free Scroll Vacuum Pump and Compressor via CAE/CFD Analysis

Lesson 6 Review of fundamentals: Fluid flow

ROLLER BEARING FAILURES IN REDUCTION GEAR CAUSED BY INADEQUATE DAMPING BY ELASTIC COUPLINGS FOR LOW ORDER EXCITATIONS

Effect of effective length of the tube on transmission loss of reactive muffler

Pressure and Flow Characteristics

Review of pipe flow: Friction & Minor Losses

CALCULATION OF COEFFICIENT OF DISCHARGE OF ORIFICE PLATE AND FLOW NOZZLE

Particles Removal from a Moving Tube by Blowing Systems: A CFD Analysis

Sizing of Gas Pipelines

Canada. CFD-Experiments Integration in the Evaluation of Six Turbulence Models for Supersonic Ejectors Modeling

Effect of Length and Porosity on the Acoustic Performance of Concentric Tube Resonators

CFD MODELLING AND VALIDATION OF HEAD LOSSES IN PIPE BIFURCATIONS

Discharge coefficient behaviour in presence of four perforated plates flow conditioners - Numerical investigation Part 1-

10 minutes reading time is allowed for this paper.

Major and Minor Losses

Stratified scavenging in two-stroke engines using OpenFOAM

SEM-2016(03)-II MECHANICAL ENGINEERING. Paper -11. Please read each of the following instructions carefully before. attempting questions.

The effect of geometric parameters on the head loss factor in headers

Sourabh V. Apte. 308 Rogers Hall

INSTITUTE OF AERONAUTICAL ENGINEERING Dundigal, Hyderabad AERONAUTICAL ENGINEERING QUESTION BANK : AERONAUTICAL ENGINEERING.

Exercise 8 - Turbocompressors

Jet Aircraft Propulsion Prof. Bhaskar Roy Prof. A.M. Pradeep Department of Aerospace Engineering

Studies on flow through and around a porous permeable sphere: II. Heat Transfer

Measurement of fluid flow in closed conduits

DESIGN AND PERFORMANCE OF THE CONVERGING-DIVERGING VORTEX FLOWMETER

EXPERIMENT No.1 FLOW MEASUREMENT BY ORIFICEMETER

Self-Excited Vibration in Hydraulic Ball Check Valve

FE Exam Fluids Review October 23, Important Concepts

MCE380: Measurements and Instrumentation Lab

THE EFFECT OF TWO PHASE (AIR-WATER) FLOW CHARACTERISTICS ON MOMENTUM FLUX DUE TO FLOW TURNING ELEMENTS AT ATMOSPHERIC CONDITIONS

Water Circuit Lab. The pressure drop along a straight pipe segment can be calculated using the following set of equations:

B.E/B.Tech/M.E/M.Tech : Chemical Engineering Regulation: 2016 PG Specialisation : NA Sub. Code / Sub. Name : CH16304 FLUID MECHANICS Unit : I

Laboratory work No 2: Calibration of Orifice Flow Meter

Discharge Coefficient Prediction for Multi hole Orifice Plate in a Turbulent Flow through Pipe: Experimental and Numerical Investigation

Flowmeter Discharge Coefficient Estimation

Determination of Pressure Losses in Hydraulic Pipeline Systems by Considering Temperature and Pressure

Comparison between Numerical and Experimental for UVP Measurement in Double Bent Pipe with Out-of-Plane Angle

INSTRUCTIONS FOR LABORATORY EXPERIMENT IN FLUID MECHANICS

INTERNATIONAL JOURNAL OF ENGINEERING SCIENCES & RESEARCH TECHNOLOGY

Answers to questions in each section should be tied together and handed in separately.

DISCHARGE COEFFICIENT OF SMALL SONIC NOZZLES

Steven Burian Civil & Environmental Engineering September 25, 2013

UNIT I Basic concepts and Work & Heat Transfer

Head loss coefficient through sharp-edged orifices

Sudden Expansion Exercise

When water (fluid) flows in a pipe, for example from point A to point B, pressure drop will occur due to the energy losses (major and minor losses).

Available online at ScienceDirect. Procedia Engineering 113 (2015 )

Dimensions represent classes of units we use to describe a physical quantity. Most fluid problems involve four primary dimensions

data Subsonic, helium release H 2 release concentrations Choked, Steady-state, concentrations release Transient, Subsonic, concentrations Subsonic,

STRUCTURAL ANALYSIS OF A WESTFALL 2800 MIXER, BETA = 0.8 GFS R1. By Kimbal A. Hall, PE. Submitted to: WESTFALL MANUFACTURING COMPANY

COMPARISION OF FLOW ANALYSIS THROUGH A DIFFERENT GEOMETRY OF FLOWMETERS USING FLUENT SOFTWARE

Experimental Study and Analysis of Flow Induced Vibration in a pipeline

Model Selection 1. Process Valves. Air. Vacuum

Test bench of head losses in incompressible flow

Industries & Applications

Contents. 2 Basic Components Aerofoils Force Generation Performance Parameters xvii

Analysis of flow characteristics of a cam rotor pump

inter.noise 2000 The 29th International Congress and Exhibition on Noise Control Engineering August 2000, Nice, FRANCE

Transcription:

Analysis of the possibility to optimize the passive pressure pulsations dampers using CFD MSc eng. Przemysław Młynarczyk Supervisor: Prof. dr hab. inż. Piotr Cyklis Abstract Vibration and noise caused by pressure pulsations in volumetric compressor manifolds are one of the most important problem in compressor operation. Passive damping of those pulsations is possible using specially shaped nozzle placed in place of the straight tube. Experimental analysis of the pressure pulsations damping caused by a nozzle is possible however only some nozzle shapes can be investigated. In this case the CFD simulations could be helpful. Some parameters obtained in the experimental investigations in the compressor manifold can be related with the parameters obtained in the steady state flow nozzle simulation. In this paper the experimental and numerical results comparison is showed and, thus, the analysis of the possibility to use CFD simulations to optimize the nozzle shape is described. Keywords Compressors, Pressure pulsations, CFD 1. Problem analysis Periodic work flow of the volumetric compressors causes the pressure and mass flow pulsations. Pressure pulsations in volumetric compressor manifolds have a high impact on compression power requirement and the reliability of manifold operation. They induce vibrations, noise and in some cases even mechanical failure of piping or compressor valves. Nowadays there is a lot of publications that describes pressure pulsations as a one of the major problem in the compressor manifold operation [1][2]. Widely introduced variable revolution speed compressors makes it difficult to find a universal solution that will attenuate pressure pulsations in a wide range of compressor revolution speed so other possibilities of pressure pulsations damping than the standard way are really wanted [3]. In some cases there is no need to supress the pressure pulsations in high rate but attenuation in the 20%-30% is desirable [4]. The point is to suppress the pulsations generated at various operating parameters of the compressor. There are many articles described that the CFD application for simulation of impulse and constant flows through the nozzle can give estimation of the nozzle effect in advance [4][5][6]. In this article the comparison of some parameters obtained in the experimental results and numerical simulations results are presented. 2. Investigated geometries For simulation and experimental investigation several nozzle designs have been prepared. The shapes are two Venturi nozzles and two Venturi orifices, which are normalized shapes described in the ISO standards, and two Hyperboloidal nozzles. All of the nozzles have the outter diameter equal to 35 milimeters and the only difference between two the same nozzles is inner diameter which is 20 or 15 mm. The nozzle shapes are shown in the fig. 1. There are

also investigated combination of this shapes, like twin hyperboloid nozzles in a different combinations, and the nozzles reversed shapes. Fig. 1. Shape and main dimensions of the a) Venturi nozzle, b) Hiperboloidal nozzle, c) Venturi orifice 3. Experimental investigations In the experimental investigations the DEMAG screw compressor powered by diesel engine with the variable speed control was used. The unit consist of 3 cylinders, 2.2 liters engine, with nominal revolution speed equal to 3000 revolutes per minute and screw compressor which nominal efficiency is 4.2 cubic meters per minute at 7 bars discharge pressure. In the fig. 2. The test stand is shown. In the experimental investigations of pressure pulsations damping the nozzles were placed 17 mm above the screw compressor discharge chamber. Fig. 2. Measuring system, where: 1- Engine, 2- Torque meter on the propeller shaft, 3- Screw compressor, 4- Pressure pulsations sensors, 5- Oil Separator, 6- Static pressure transducer, 7- Throttle valve, 8- Metering orifice, 9- Outflow

The ICP Dynamic Pressure Sensors made by PCB Piezotronics were used. The signal from sensors goes through the 4-channel ICP Sensor Line Power unit to the NI USB-6251 data acquisition module. The LabView data acquisition software was used to acquire the pressure pulsation data. The measurements data were recorded as soon as the compressor and manifold reached steady operation. 4. Simulation procedure and benchmark test For the numerical calculations the Ansys Fluent software was used. Simulation procedure for all investigated shapes was determined as an ideal gas isentropic flow in the two-dimensional axisymmetric model. Geometry for all cases was designed as a combination of the straight pipe and passive damper shape. The mesh model contains two areas with different element size. In the area of nozzle geometry smaller elements were defined than in the straight pipe geometry. The Raynolds stress model was chosen as a most accuracy turbulence model. Mesh detail are shown in the fig.3. Fig. 3. Hyperboloidal nozzle φ20 mesh detail Two different numerical calculations were performed for each element. In this paper the steady state flow simulations results are described. At the pipe inlet the mass flow equal to 0.05 [kg/s] has been applied. Pressure drop obtained in the steady state flow simulations can be related to the pressure drop in the installation during experimental investigations or to the other corresponding parameter. To check the prepared flow codes simply benchmark test was conducted. Numerical simulations results of the pressure drop for standard nozzles shapes were compared to the analytical results calculated according to the normalised, known methods for pressure loss in a pipe or standard nozzle. This methods are shown below: - Darcy-Weisbach method for tube pressure loss under steady flow conditions [7]: where Darcy s coefficient is taken from Moody s diagram or Colebrook s equations: according to Haaland: or Swamee-Jain: - For Venturi orifice and Venturi nozzle ISO 5167 standard formula may be applied, for pressure drop on the nozzle : (1) (2) (3) (4)

In fact, this comparison is not exactly the same as a real nozzle with the inlet and outlet straight pipe required, therefore some differences from the results of standardised flow measurement method can be noticed. The results is shown in the table 1. Table 1. Benchmark test results Shape Analytical [Pa] CFD [Pa] Empty pipe 194 219 Venturi orifice ϕ20mm 12201 11166 Venturi orifice ϕ15mm 41098 36825 Venturi nozzle ϕ20mm 11634 10631 Venturi nozzle ϕ15mm 41345 39848 To conduct the preliminary simulations the author considered that the results with a maximum error about 10% are satisfactory. 5. Results comparison The main assumption of this paper is to analyse the possibility to optimize the passive pressure pulsation damper using CFD. Therefore there is a need to assess the nozzle influence on the fluid flow. In the numerical calculations such a parameter can be a pressure drop on the element. In the experimental investigations the important parameter for the assessment of nozzle influence is the increase of power consumption due to flow restriction by the nozzle. To make this assessment the volumetric flow rate to compressor shaft power ratio was chosen. This parameter is increasing with lower energy consumption and decreasing with lower volume flow rate. Results of the experimental obtained V/N coefficient is shown in the fig. 4. for compressor revolution speed equal to 1615 rev/min and in the fig. 5. for 2100 rev/min. All the results are percentage increase or loss compared to an empty pipe V/N ratio value. Fig. 4. V/N power loss in [%] compared to empty pipe for 1615 rev/min

Fig. 5. V/N power loss in [%] compared to empty pipe for 2100 rev/min In terms of values V/N parameter increase indicates compressor s better overall performance. It has been assumed that V/N is related to the steady flow pressure loss on the element, therefore the steady flow through the element was simulated and the pressure loss was compared with an empty pipe pressure loss during steady flow. To have a better comparison to the simulation results the pressure drop on the element has been related to the average pressure in the discharge compressor manifold and the pressure loss on a straight empty pipe (pipe0) using the following formula: Coefficient β is shown in Fig. 6. This figure shall be compared with the experimental results shown in Figs 4 and 5. The exact match here with the figures cannot be expected since this is not the same parameter, but the relations between the results for each shape and dimension are similar to the experimental results. (5) Fig. 6. Relative pressure loss β on damping element in comparison with the pressure loss on an empty straight pipe in [%]

6. Conclusions In the paper comparison between parameters obtained in the experimental investigations and numerical simulations is analysed. The comparison shows that there is a possibility to exact some features from both, experimental and numerical results, which correspond to each other. It has been shown that the simulation of steady flow through the nozzle is a basis for compressor power increase determination. Obviously the CFD results are not directly the same as experimental determined parameters, because using CFD method only a short part of pipe with nozzle is simulated, while in the experimental investigation there is a lot of elements that have an influence on the number of parameters. In conclusion, a possibility of a good shape optimization using CFD is possible, but the interesting parameters have to be chosen reasonably and managed at a high level. Symbols Δp pressure drop (Pa) fd dimensionless Darcy s coefficient (1) L pipe length (m) D pipe internal diameter (m) V average flow velocity (m/s) r relative roughness of the wall (1) Re Reynolds number (1) e roughness height (m) mass flow rate (kg/s) v1 specific volume before the nozzle (m 3 /kg) flow number (1) ε expansion number (1) A area of the nozzle cross-section (m 2 ) power loss coefficient (kg/ws) References 1. He S., Jackson J., 2009. An experimental study of pulsating turbulent flow in a pipe. European Journal of Mechanics B/Fluids 28, pp.309-320. 2. Dowling, J. & Peat, K., 2003. An algoritm for the efficient acoustic analysis of silencers of any general geometry. Applied acoustics 65, pp. 211-227. 3. Lokitsangtong, M., Murakami, S. & Iijima, T., 2006. Acoustical characteristics of singleresonator-type silencers. Proceedings of the School of Engineering, Tokai University, Series E 31, pp. 39-44. 4. Hermann, J. et al., 2011. Frequency-dependent damping model for the hydroacoustic finite element analysis of fluid-filled pipes with diameter changes. Mechanical systems and signal processing 25, pp. 981-990. 5. Shademan, Y., Barron, M. & Balachandar, R., 2012. CFD Study of effects of geometry variations on flow in a nozzle. Engineering Applications of Computational Fluid Mechanics Vol.6, No. 3, pp. 412-425.. 6. Lee, S.-H. & Ih, J.-G., 2008. Effect of non-uniform perforation in the long concentric resonator on transmission loss and back pressure. Journal of sound and vibration, pp. 280-296. 7. EngineeringToolbox, 2014. EngineeringToolbox. [Online] Available at: http://www.engineeringtoolbox.com/darcy-weisbach-equation-d_646.html [Accessed 07 04 2015].