Leak Test of Sensors with the Test Medium compressed Air

Similar documents
Pressure Drop in Air Piping Systems Series of Technical White Papers from Ohio Medical Corporation

GAS TURBINE PERFORMANCE WHAT MAKES THE MAP?

be the mass flow rate of the system input stream, and m be the mass flow rates of the system output stream, then Vout V in in out out

- The value of a state function is independent of the history of the system. - Temperature is an example of a state function.

One-Chip Linear Control IPS, F5106H

CRITICAL AVIATION INFRASTRUCTURES VULNERABILITY ASSESSMENT TO TERRORIST THREATS

TOWARDS REAL-TIME METADATA FOR SENSOR-BASED NETWORKS AND GEOGRAPHIC DATABASES

Pinhole Optics. OBJECTIVES To study the formation of an image without use of a lens.

Fluent Software Training TRN Solver Settings. Fluent Inc. 2/23/01

MODEL OF THE PNEUMATIC DOUBLE ACTING CYLINDER COMPILED BY RHD RESISTANCES

1.3 Saturation vapor pressure Vapor pressure

Failure Behavior Analysis for Reliable Distributed Embedded Systems

STABILITY OF PNEUMATIC and HYDRAULIC VALVES

First Law, Heat Capacity, Latent Heat and Enthalpy

Monitoring Frequency of Change By Li Qin

A MOST PROBABLE POINT-BASED METHOD FOR RELIABILITY ANALYSIS, SENSITIVITY ANALYSIS AND DESIGN OPTIMIZATION

Numerical Simulation of Sand Erosion Phenomena in Rotor/Stator Interaction of Compressor

OUTCOME 1. TUTORIAL No. 2 THERMODYNAMIC SYSTEMS

4. Influence of Temperature and Pressure on Chemical Changes

Load Balancing Mechanism in Agent-based Grid

A Simple Model of Pricing, Markups and Market. Power Under Demand Fluctuations

Storage Basics Architecting the Storage Supplemental Handout

CABRS CELLULAR AUTOMATON BASED MRI BRAIN SEGMENTATION

COST CALCULATION IN COMPLEX TRANSPORT SYSTEMS

Vertically Integrated Systems in Stand-Alone Multistory Buildings

Thermodynamics worked examples

Concurrent Program Synthesis Based on Supervisory Control

Synopsys RURAL ELECTRICATION PLANNING SOFTWARE (LAPER) Rainer Fronius Marc Gratton Electricité de France Research and Development FRANCE

An inventory control system for spare parts at a refinery: An empirical comparison of different reorder point methods

The International Standard Atmosphere (ISA)

Rummage Web Server Tuning Evaluation through Benchmark

Corporate Compliance Policy

Compensating Fund Managers for Risk-Adjusted Performance

NOISE ANALYSIS OF NIKON D40 DIGITAL STILL CAMERA

Migration to Object Oriented Platforms: A State Transformation Approach

Project Management and. Scheduling CHAPTER CONTENTS

Local Connectivity Tests to Identify Wormholes in Wireless Networks

Two-resource stochastic capacity planning employing a Bayesian methodology

The number of revolutions is proportional to the passed volume. The rotation is transferred to a mechanical index, which indicates this volume.

C-Bus Voltage Calculation

IEEM 101: Inventory control

Static and Dynamic Properties of Small-world Connection Topologies Based on Transit-stub Networks

Free Software Development. 2. Chemical Database Management

VESTAKEEP PEEK PEEK Polyether Ether Ketone Powders

Fugacity, Activity, and Standard States

ENFORCING SAFETY PROPERTIES IN WEB APPLICATIONS USING PETRI NETS

Risk in Revenue Management and Dynamic Pricing

Chapter 2 - Porosity PIA NMR BET

X How to Schedule a Cascade in an Arbitrary Graph

Sage Timberline Office

Index Numbers OPTIONAL - II Mathematics for Commerce, Economics and Business INDEX NUMBERS

THE BAROMETRIC FALLACY

A Virtual Machine Dynamic Migration Scheduling Model Based on MBFD Algorithm

1 Exercise 4.1b pg 153

A Modified Measure of Covert Network Performance

Drinking water systems are vulnerable to

Detectors in Nuclear and Particle Physics

Memory management. Chapter 4: Memory Management. Memory hierarchy. In an ideal world. Basic memory management. Fixed partitions: multiple programs

The Economics of the Cloud: Price Competition and Congestion

Parallel Multi-Zone Methods for Large-Scale Multidisciplinary Computational Physics Simulations

Risk and Return. Sample chapter. e r t u i o p a s d f CHAPTER CONTENTS LEARNING OBJECTIVES. Chapter 7

The impact of metadata implementation on webpage visibility in search engine results (Part II) q

MODELLING AND SIMULATION OF A DISH STIRLING SOLAR ENGINE. Sergio Bittanti Antonio De Marco Marcello Farina Silvano Spelta

physical therapy Faculty Ed Barakatt, Bryan Coleman-Salgado, Rafael Escamilla, Clare Lewis, Susan McGinty, Brad Stockert

Sage HRMS I Planning Guide. The HR Software Buyer s Guide and Checklist

2D Modeling of the consolidation of soft soils. Introduction

Sage Document Management. User's Guide Version 12.1

Design of A Knowledge Based Trouble Call System with Colored Petri Net Models

The Online Freeze-tag Problem

Sage Document Management. User's Guide Version 13.1

Comparing Dissimilarity Measures for Symbolic Data Analysis

An Introduction to Risk Parity Hossein Kazemi

HEAT UNIT 1.1 KINETIC THEORY OF GASES Introduction Postulates of Kinetic Theory of Gases

Service Network Design with Asset Management: Formulations and Comparative Analyzes

IGBT (Insulated Gate Bipolar Transistor) 1 Differences Between MOSFET and IGBT

Price Elasticity of Demand MATH 104 and MATH 184 Mark Mac Lean (with assistance from Patrick Chan) 2011W

Safety evaluation of digital post-release environment sensor data interface for distributed fuzing systems

Title: Stochastic models of resource allocation for services

DAY-AHEAD ELECTRICITY PRICE FORECASTING BASED ON TIME SERIES MODELS: A COMPARISON

Automatic Search for Correlated Alarms

Evaluating a Web-Based Information System for Managing Master of Science Summer Projects

On the predictive content of the PPI on CPI inflation: the case of Mexico

Re-Dispatch Approach for Congestion Relief in Deregulated Power Systems

This document is downloaded from DR-NTU, Nanyang Technological University Library, Singapore.

STERIVAPHP IL. Disinfections, sterilisation and decontamination in the science, research and industry area. protecting human health

Large firms and heterogeneity: the structure of trade and industry under oligopoly

(1) VIDEO CD Player. Operating Instructions MCE-S78K by Sony Corporation

Machine Learning with Operational Costs

STERIVAP HP IL Large Steam Sterilizer for Disinfections, Sterilisation and Decontamination in the Science, Research and Industry Area

Managing specific risk in property portfolios

TRANSMISSION Control Protocol (TCP) has been widely. On Parameter Tuning of Data Transfer Protocol GridFTP for Wide-Area Networks

Transcription:

DOI 10.516/sensor013/B7.3 Leak Test of Sensors with the Test Medium comressed Air Dr. Joachim Lasien CETA Testsysteme GmbH, Marie-Curie-Str. 35-37, 4071 Hilden, GERMANY, E-Mail: joachim.lasien@cetatest.com Abstract As sensors are used in the diverse industrial alications this comonent has to fulfill a variety of requirements. This includes leak tightness against dirt and moisture, whose requirements are secified in the IP rotection classes. Penetration of liquids can cause serious malfunction of the sensor and the associated electronics. Thus, the sensors have to be leak tight. The leak testing of the sensors as an end-of-line test integrated in the roduction line is of articular imortance. The basics of leak testing and imortant ractical asects of the leak test rocess are treated. Key words: leak tightness, IP rotection classes, leak test, end-of-line test, hood test. Test Medium comressed Air The definition of the IP rotection classes describes how a laboratory test has to be erformed. But of course, such a test cannot be integrated as 100%-inline rocess in the roduction line. Based on the results of the laboratory exeriments the requirements for a corresonding leak test in the roduction line have to be worked out. Ideally the test ressure and the ermissible leak rate can be defined. Deending on the leak rate a suitable test medium and test rocess have to be chosen to fulfill the technical requirement. Table 1 shows some of the most common used test media and their secific features. Widesread is the use of the test medium comressed air for the 100 % in-line leak testing in industrial roduction lines. The test medium comressed air can be used down to an air leak rate of 10-3 mbar*l/s (deending on the test art). If a sensor has to be waterroof an air leak rate of 10 - mbar*l/s (= 0,6 cm³/min) is commonly assumed. Tyical examles of automotive sensors, which are tested with comressed air are oil ressure sensors, ABS sensors, level sensors. Tab. 1. Overview about leak test media (1 mbar*l/s = 60 cm³/min). Test Medium Air Leak Rate Method Remarks Water > 10 - mbar*l/s Detection of bubbles Qualitative method Localisation of leaks Comressed Air > 10-3 mbar*l/s Measurement of ressure decay res. ressure rise (relative ressure sensor, differential ressure sensor) Quantitative method Easy to handle Deending on the volume Temerature sensitivity Integral method Localisation of leaks => Use of leak sray Hydrogen (Forming Gas) > 10-6 mbar*l/s Measurement of H -concentration Quantitative method No volume deendency No temerature sensitivity Sniffing: Localisation of leaks Helium > 10-9 mbar*l/s Measurement of He-concentration Quantitative method No volume deendency No temerature sensitivity Evacuation for small leak rates Sniffing: Localisation of leaks AMA Conferences 013 - SENSOR 013, OPTO 013, IRS 013 313

DOI 10.516/sensor013/B7.3 Test Method Pressure Decay Test for direct fillable Test Parts Test arts with small volumes, which can be filled directly, have often to be tested in a very short total test time by the use of comressed air. The overall test consists of the consecutive hases: filling, stabilizing, testing and duming. In the filling hase, the test art has to be filled to reach the test ressure. The stabilizing hase is necessary so that air disturbances (caused by the filling rocess and generated by the switching of the internal valves of the test device) can subside. In case of a ositive relative test ressure the air is comressed adiabatically during the filling rocess, which heats u the air. So, the temerature of the comressed air has to adjust to the temerature of the test art. In the testing hase, the rate of ressure loss is measured and comared with the ermitted tolerances. The testing hase must be long enough to generate a significant measurement value. In the testing hase mostly a very sensitive differential ressure sensor is activated to measure the ressure decay with high resolution. A stable measurement hase is characterized by the effect, that the leakageinduced ressure loss is roortional to time. Finally follows the duming hase (see Fig. 1). Fig. 1. Princile of the ressure decay test of direct fillable test arts. Leak Rate Formula The exected ressure decay in time in the test hase can be calculated by the use of the socalled leak rate formula. This is an aroximation for the leakage induced ressure decay in a stable test regime (eq. (1)): Pa QL [cm³ /min] t s V [cm³] eff 100.000 Pa 60 s/min (1) where /t = Pressure decay in time V eff = Effective test volume This is the sum of the volumes of the test art, the adation, the measuring line and the measuring circuit inside the test device Q L = Leak rate (1 mbar *l/s = 60 cm³/min). The air escaes into the ambient atmoshere with an atmosheric ressure of arox. 100.000 Pa (absolute ressure) AMA Conferences 013 - SENSOR 013, OPTO 013, IRS 013 314

DOI 10.516/sensor013/B7.3 Test Method "Closed Comonents" for encasulated Test Parts Encasulated test arts, like most of the sensor tyes, cannot be filled inside with ressurized air. A tyical examle to demonstrate this test method is an encasulated hotoelectric sensor (see Fig. ). These tyes of test arts are laced in a hood which encloses the test art as closely as ossible. The hood is ressurized. The temoral ressure decay of the ressure in the test art is measured. This tye of test is called "closed comonent test" or "hood test". Fig.. Photoelectric sensor as an examle for a encasulated test art. Hereby occurs the following roblem: If the test art has a major leak (so-called gross leak), it is already filled with comressed air during the filling hase of the hood. In this case, only the tightness of the hood surrounding the test art would be measured. Therefore it has to be controlled in the first ste that the test art has no gross leak (gross leak test). After this the fine leak test is erformed by means of a ressure decay measurement (see above). The gross leak test is done in the following way (see Fig. 3): A reservoir volume, which is integrated in the test device, is filled to a ressure 1 and searated from the ressure regulator. Then the check valve of the internal reservoir volume is oened and the air is flooded through the measuring line into the hood. Hereby the ressure decreases to a lower ressure. The ratio / 1 is a measure for the volume which is filled. The ressure values are measured with a relative ressure sensor. Fig. 3. Princile of the leak test of encasulated test arts. The total test consists of two stes: After the gross leak test follows the fine leak test. If the test art has no gross leak, the following alies (eq. ()): V R () 1 VR VM VL VH VPe In case of a gross leak the internal volume of the test art is filled additionally and the following alies (eq. (3)) V R (3) 1 VR VM VL VH VPe VPi AMA Conferences 013 - SENSOR 013, OPTO 013, IRS 013 315

DOI 10.516/sensor013/B7.3 where V R = Reservoir volume V M = Volume of the measuring circuit V L = Volume of the measuring line V H = Volume of the emty hood V Pe = External volume of the test art V Pi = Internal volume of the test art (filled in case of a gross leak) These relationshis are a result of the ideal gas equation, assuming constant temerature (isothermal change of state). In the initial state, the volumes are at atmosheric ressure level, so that in these formulas, the ressures are to be used as ositive and negative relative ressures. Examle The outer volume of a sensor is 5 cm 3. The sensor is encasulated and has an internal volume of cm 3, which is filled in case of a gross leak. The hood, surrounding the sensor, has a volume of 10 cm 3. The test device has an internal reservoir volume of 45 cm 3, the internal measuring circuit has a volume of 5 cm 3. The measuring line has a length of 0.5 m and an inner diameter of 4 mm. This corresonds to a line volume of 6.3 cm 3. In this case, the ressure ratio is 0.734 in case of a sensor without gross leak. If the sensor has a major leak, there is a ressure ratio of 0.711. In case of a non gross leak sensor the fine leak follows. To erform the fine leak test at a test ressure of = 500 mbar, a ositive ressure of 1 = 681 mbar has to be set as the start value. Technical Features of the Leak Tester Fundamental hysical effects (temerature adjustment of the comressed air, disturbances in the comressed air) can hardly be influenced, but the test device can be otimized regarding the comonents which have a sensitive influence uon the test rocess. The distinction between a test art with gross leak and a test art without gross leak is more difficult if the fillable internal volume of the test art is quite small comared to the sum of the other volumes (see eq. (1) and ()). By the use of a relative ressure sensor for the measurement of the ressures 1 and a difference of at least about 0.0 between the gross leak ressure ratio and the non-gross leak ressure ratio is needed for a stable leak test rocess integrated in the roduction line. This can be imroved by the use of more sensitive ressure sensors (see below). The resolution and the total test time in the leak test of small-volume test arts can be otimized by the following rocedures: Use of a measuring line with a small inner diameter, rovided this does not hinder the filling rocess too much. If the measuring line has an inner diameter of 3 mm, the line volume can be reduced by 44% as an equal length measuring line with 4 mm inner diameter. Use of secial internal electrical valves that have an extremely low switching kick. This reduces the time for the relaxation of the air disturbances caused by the switching rocess. Reduction of the internal volumes of the test device (esecially measuring circuit volume). Use of a hood that encloses the test art as closely as ossible. Hereby the test art tolerances have to be taken into account. In ractice it is ossible, that the hood has just a surrounding distance of only 0. mm to the outer contour of the test art. Use of a much more sensitive ressure sensor (differential ressure sensor instead of relative ressure) to detect even finer differences in the ressure ratio / 1. Practical Alications High Seed Pressure Decay Test and Detection of Assembly Defects With such an otimized instrument like the leak tester, tye CETATEST 515 in the variant "closed comonents, high resolution" (see Fig. 4), the assembly of microarts can be tested, too. The volume which can be filled with air can be taken as a measure to detect assembly defects like a missing o-ring. In a test art, which has a fillable volume of 0 cm 3 and which can be filled directly, a volume difference of only 0.03 cm 3 can be detected by using a ositive relative ressure of 900 mbar This corresonds to the volume of an o-ring of 1 mm diameter and 1 mm cross section. Fig. 4. Leak tester tye CETATEST 515 for the leak test of encasulated test arts with small volume. AMA Conferences 013 - SENSOR 013, OPTO 013, IRS 013 316

DOI 10.516/sensor013/B7.3 The leak test of encasulated small volume test arts (external volume arox. 0,5 cm³) have been realized in the roduction line with a total test times in the range of 1 to s. This can result in several million cycles in one year in a roduction line working to full caacity. The internal comonents in the test device must be designed accordingly for a long service life. In the leak test of low-volume secial valves by the ressure decay leak test using the CETATEST 515 (in the variant "ressure decay high seed ) a total test time of just 750 ms has been realized. In this very short time a comlete leak test cycle consisting of filling, stabilizing, testing and duming is erformed. AMA Conferences 013 - SENSOR 013, OPTO 013, IRS 013 317