Effects of liner buckling pressure and teat length on pulsation chamber a- and c-phases

Similar documents
Determination of the physical properties of different types of milk claws and air leaks in the claw according to rotameter-milk bucket methods

Unraveling the mysteries of liner compression

Comparison of Liner Action with Pulsation Performance

What s new in milking: Systems, Components, Testing and Settings Ralph Ginsberg Nantes 2016

Test, service and up-grade milking machines

Discussion and guidance on the definition and qualification of porous loads

Components for air preparation and pressure adjustment. OUT port position ( ) connected Rear side. of IN port. Air tank. directly.

THE GOAT AND SHEEP RANGE

Flow in a shock tube

DESIGN AND PERFORMANCE OF THE NEW SARTORIUS 1 KG VACUUM MASS COMPARATOR AT PTB

Impact Fatigue on Suction Valve Reed: New Experimental Approach

Variability of milking frequency and intervals between milkings in milking robots

Pressure Reducing Valve DMV 755

DIAPHRAGM PUMPS WITH KNF STABILIZATION SYSTEM

WAVES. Pulses are disturbances or a single wave motion. A continuous production of pulses will give rise to a progressive wave (wave train).

Measuring range Δp (span = 100%) Pa

RIPPLE TANK - with rippler & kit

FPG8601 Force Balanced Piston Gauge

WIKA INSTRUMENT CORPORATION

Carrier Gases in Capillary GC

E. Agu, M. Kasperski Ruhr-University Bochum Department of Civil and Environmental Engineering Sciences

TYPE ECS SEAL METAL BELLOWS DRY-RUNNING SECONDARY CONTAINMENT Technical Specification

Pressure transmitters EMP 2

Tissue Congestion Relief

Hitachi Differential Pressure/Pressure Transmitter

A New Way to Handle Changing Fluid Viscosity and the Full-to-empty Effect

Best Practices for Installation of Gaseous Sample Pumps

Tank Blanketing Pressure Regulators RHPS Series

RESEARCH IN TIME BETWEEN MILKING INTERVAL AND VARIABILITY OF MILKING FREQUENCY USING MILKING ROBOTS

Self-operated Pressure Regulators for special applications

no peaks missing peaks too small peaks increasing retention decreasing retention

Making Life Easier Easypump II

Caution for using. ! General cautions common to all the instruments

Variation of Nordic Classic Ski Characteristics from Norwegian national team athletes

Old documentation - Only for your information! Product is not available anymore!

Wave phenomena in a ripple tank

SPECIFICATION FOR REPEATED LOAD TRIAXIAL (RLT) TESTING FOR PAVEMENT MATERIALS

VACUUM REGULATORS CONTENTS

Specific Accreditation Criteria Calibration ISO IEC Annex. Mass and related quantities

Chs. 16 and 17 Mechanical Waves

SURFACE CASING SELECTION FOR COLLAPSE, BURST AND AXIAL DESIGN FACTOR LOADS EXERCISE

Comparative Tests on Differential Pressure Control Valves

P-04 Stainless Steel Corrugated Hoses and Metal Bellows Expansion Joints

CSO/STORMWATER MANAGEMENT. HYDROVEX HHV-E Vortex Driven Regulator

VPPL VARIABLE DISPLACEMENT AXIAL-PISTON PUMPS FOR INTERMEDIATE PRESSURE SERIES 10

TURBINE SEAL: AXIAL TYPE DESIGN

VENTILATION OF PROTECTED AREAS IN ROAD TUNNELS

Pressure Relief Valve DHV 718

Prof AH Basson, Pr Eng March Departement Meganiese en Megatroniese Ingenieurswese. Department of Mechanical and Mechatronic Engineering

Sheep and Goat Milking Equipment. Easy to use components for reliable milking performance

Influence of HALO and drain-extension doping gradients on transistor performance

A New Test Setup for Testing Polyethylene Tubes under Constant and Cyclic Internal Pressures

THIS ARTICLE IS SPONSORED BY THE MINNESOTA DAIRY HEALTH CONFERENCE.

Dwell Time and Immersion Depth Optimization For Immediate Defect Reduction

Materials : Dichromate zinc plated steel flanges

CHAPTER 3 : AIR COMPRESSOR

Full-Vacuum Chlorinator C 2212 MB / 1

General page Straight unions page Angle unions page Tee and L-unions page Gauge connection unions page 42

Pressure Reducing Valve DMV 755 set range: 1,0-9,0 bar

DEVIL PHYSICS THE BADDEST CLASS ON CAMPUS AP PHYSICS

CONTENTS 1. INTRODUCTION DESCRIPTION OF TEST SAMPLE TEST RIG GENERAL ARRANGEMENT TEST SEQUENCE...7

From a recent Westfalia-Surge US Patent document submittal, December 2004:

State and national standardized lactation averages by breed for cows calving in 2013

Vibration and Pulsation Analysis and Solutions

DM01. Please visit our website: Battery Powered Precision Digital Gauge. Stainless Steel Sensor. class 0.05

S261 Remote seals with capillary tube

ETd 04. Battery Powered Precision Digital Gauge. Stainless Steel Sensor. Type: ETd 04. class 0.05

Drilling Efficiency Utilizing Coriolis Flow Technology

1 Exam Prep. Questions and Answers

Annex G (normative) Requirements for Nondestructive Examination

Ballorex Dynamic Description. Versions. Benefits. Balancing

Measurement of Representative Landfill Gas Migration Samples at Landfill Perimeters: A Case Study

Materials : Dichromate zinc plated steel flanges or AISI 316

INTERNATIONAL OIML R 32 RECOMMENDATION. Rotary piston gas meters and turbine gas meters ORGANISATION INTERNATIONALE INTERNATIONAL ORGANIZATION

5.1 Introduction. Learning Objectives

Milking center performance and cost

Controllers DR, DP, FR and DFR

WhirlWind Multifunctional gas control Fully integrated gas-air system with control and safety function GB-WND 055 D01

DISSOLUTION TEST FOR SOLID DOSAGE FORMS

Body Material: PVC, PP, PVDF Bonnet Material: Glass Filled PP Size: ½ - 2 Pressure Rating: 150 psi Set Pressure: 4 to 150psi Seals:

Technical Data Sheet TI-F50 Locking Units series KFH

Paper #: POWER

A Hare-Lynx Simulation Model

Pressure Reducing Valve DMV 750 set range: bar

CORESTA RECOMMENDED METHOD N 6

Differential pressure controller (PN 16) AHP - return mounting, adjustable setting

Differential pressure controller (PN 16) AVPL return mounting, adjustable setting

Pressure Relief Valve DHV 718

GUKO FDA. einfach. gut. beraten.

Sartorius CCL kg Prototype Mass Comparator

CHARACTERISTICS OF LEAK DETECTION BASED ON DIFERENTIAL PRESSURE MEASUREMENT

Special edition paper

Pressure relief valve DHV 712 DN 65-80: 0,5-10 bar, DN : 0,3-4 bar, DN 100: 0,5-6 bar

Aug 17, 2001 LAB MANUAL MAXIMUM SPECIFIC GRAVITY (RICE VOIDS TEST) OF PAVING MIXTURES AASHTO Designation T 209 (Mn/DOT Modified))

Pressure Reducing Valve DMV 750

DM01. Battery Powered Precision Digital Gauge. Stainless Steel Sensor. class 0.05

WATER PRESSURE REDUCER (SBD)

GasBloc Multifunctional gas control Combined regulator and safety shut-off valves Integrated gas-air system GB-GD 057 D01

INTERNATIONAL STANDARD

FRM. Medium Pressure Regulator. Medium pressure regulator Type FRM

Transcription:

Effects of liner buckling pressure and teat length on pulsation chamber a- and c-phases H. Worstorff 1 & E. Bilgery 2 1 Inst. of Physiology, FML, Techn. University Weihenstephan, Weihenstephaner Berg 3, D 85354 Freising, Germany e-mail: physio@weihenstephan.de 2 BITEC Engineering, Rütistraße 15, CH 8590 Romanshorn, Switzerland e-mail: bitec@tgnet.ch 6 x 4 silicone liners covered buckling pressures from 6.5 to 17.9 kpa. Hard PVC teats provided penetration depths from 50-110 mm. Teat length increased liner stiffness by 39-55% which decreased a- and c-phases by 34, 83, 58 ms and 45, 48, 60 ms at 40 kpa alternate pulsation, 40/32 kpa alternate (8 kpa vacuum drop) and 40 kpa simultaneous, respectively. A- phases were shortest with vacuum drop and stiff liners while c- phases were generally shortest with soft liners and vice versa. Summary Key words: Machine milking, liner, teat penetration, pulsator phases The milking machine pulsator controls the pulsation chamber wave form but liner wall movement is determined by differential pressure (1,4,9). Liners open and close, respectively, when the latter falls short of or exceeds liner buckling pressure (6,7). With fairly stable liner vacuum, differential pressure is a more or less inverted pulsation curve. Under milking conditions, however, high capacity clusters with alternate pulsation show more or less a parallel shift of liner vacuum in combination with an increasing dip between b- and c- phase. By contrast, simultaneous pulsation alters the shape of the cyclic fluctuation with increasing flow rate (5,8) requiring measurement under actual wet conditions. ISO testing is based on teatcup plugs of 59 mm length. Longer teats, however, exist and teatcups Introduction 55

Effects of liner buckling pressure and teat length are manufactured in different lengths. Pulsation failure will occur if teat penetration is too high (2,3). The present paper analyses interactions of liner buckling pressure and teat penetration. Material and Methods Liners and teatcup plugs For the laboratory trials, 6 x 4 silicone liners (SL M23, Siliconform, D 86842 Türkheim) with 42, 51, 58 Shore and 2.80 / 3.25 mm barrel wall, respectively, were mounted in transparent 147 mm shells (# 457800897, Impulsa, D 4910 Elsterwerda). To study teat penetration effects, a series of hard PVC teatcup plugs was tooled on a CNC lathe. The construction based on the ISO 6690 specification, but the cylindrical shaft was modified in steps of 10 mm resulting in total plug lengths of 49-109 mm. Nominal and effective buckling pressure For conditioning, all liners were stored at room temperature for more than 24 h and pulsated for 10 min (40 kpa, 60 c/min, 60%) before measurement. Nominal buckling pressure (BP n ) is defined as touch point of opposite walls of liners closed by a glass plate (6). Effective buckling pressure (BP eff ) was defined as measurement with a teatcup plug in place. The touch point was observed through the transparent shell and liner held against a lamp. For slow evacuation, a small hand pump (Mityavac II, Neward Ent. Inc., Cocamonga CA) was connected to the short milk tube with the pulsation nipple open. BP was measured by strain gauge equipment (Pulsotest II, Bitec Engineering, CH 8590 Romanshorn). Measurement frequency was 1 khz, pressure readings (better than class 0.6) were displayed in intervals of 0.5 s, time recording was better than 1 ms. Measurement of pulsator phases Electronic pulsators supplied alternate (Autopuls P, Westfalia Landtechnik, D 59302 Oelde) and simultaneous pulsation (Flow Processor, Lemmer Fullwood, D 53797 Lohmar). A dry laboratory milking plant provided constant vacuum conditions (40 kpa) and vacuum drop (40/32 kpa), respectively. The latter was restricted to alternate pulsation, because simultaneous pulsation would have required specific wet conditions, exceeding this basic study. Short pulse tubes (230 x 7 mm i.d.) and 2.40 m long pulse tubes were applied for alternate (2 x 7.5 mm i.d.) and simultaneous pulsation (1 x 9 mm i.d.), respectively. Pulsator phases were recorded by Pulsotest. Nominal pulsator phases (PP n ) were measured with ISO plugs in place while effective pulsator phases (PP eff ) were measured with 50 and 70-110 mm teat penetration depth (TPD). The difference of +1 mm to the teat length accounts for liner head deformation under vacuum. Each set of liners was run 3 min for conditioning to the actual plug length before measurement. 56 Conference on "Physiological and technical aspects of machine milking"

Table 1 summarises mean buckling pressure data of all tested liners without teat (zero TPD; BP n ) as well as for 7 teat lengths (BP eff ), measured twice. The BP n figures indicate a selection from very soft to fairly stiff liners. The standard deviation increased with Shore hardness and was dominated by differences between liners, while repeated measurements typically lay within 0.1 kpa. BP eff remained unchanged or was even lower than BP n for TPD 50 and 60 mm, respectively. The slight decrease is attributed to different liner deformation: When the mouthpiece is covered by a glass plate, the entire shaft deforms while a teat limits the buckling area to the space underneath. Starting from 70 mm TPD, liner stiffness increased progressively by max. 39-55%. As expected, Shore hardness and liner wall thickness acted together and partly interchangeable. Results and discussion Nominal and effective buckling pressure. Table 1. Buckling pressure (kpa) and teat penetration depth (TPD) of liners with different Shore hardness (4 x 48 x 2 measurements). Swingliner SL M23, 2.80 mm barrel wall TPD 42 ShA 51 ShA 58 ShA (mm) BP SD % BP SD % BP SD % 0 6.49 0.12-8.71 0.14-12.50 0.61-50 6.49 0.16 0 8.65 0.17-0.1 12.49 0.45 0 ISO 60 6.41 0.11-0.1 8.61 0.25-0.1 12.46 0.49 0 70 6.76 0.12 + 0.4 8.91 0.12 + 0.2 12.79 0.43 + 0.2 80 6.95 0.15 + 0.7 9.28 0.11 + 0.7 13.69 0.26 + 1.0 90 7.48 0.23 + 1.5 9.88 0.30 + 1.3 14.74 0.52 + 1.8 100 8.18 0.29 + 2.6 10.99 0.22 + 2.6 16.39 0.80 + 3.1 110 9.43 0.33 + 4.5 12.68 0.57 + 4.6 19.35 0.77 + 5.5 Swingliner SL M23, 3.25 mm barrel wall 0 9.18 0.11-13.81 0.20-17.88 0.45-50 9.01 0.15-02 13.55 0.35-0.2 17.36 0.31-03 ISO 60 9.09 0.27-01 13.88 0.33 0 17.39 0.49-03 70 9.35 0.15 + 0.2 14.24 0.30 + 0.3 18.38 0.33 + 0.3 80 9.74 0.17 + 0.6 15.11 0.46 + 0.9 19.26 0.48 + 0.8 90 10.41 0.20 + 1.3 16.38 0.43 + 1.9 20.64 0.43 + 1.5 100 11.11 0.37 + 2.1 18.18 0.47 + 3.2 22.99 0.50 + 2.9 110 12.75 0.26 + 3.9 21.31 0.50 + 5.4 27.64 0.96 + 5.5 Generally, BP eff increased with TPD causing less liner deformation and volume change during the pulsator a- and c- phases (PP eff ). For alternate pulsation at 40 kpa, an increase of BP eff from 6.5 to 27.6 kpa caused a pulsator a- phase reduction from 141 to 107 ms. This is a maximum difference of 3,4% and a relative change of -18 to -30% for soft and hard liners, respectively. For simultaneous pulsation at 40 kpa, the a- phase reduced from 199 to 141 ms (5,8%). For alternate pulsation with 8 kpa Effects of teat penetration depth on a- and c-phases. 57

Effects of liner buckling pressure and teat length vacuum drop, the a- phases reduced from 185 to 102 ms (Figure 1). The length of the a- phases decreased with increasing TPD and BP eff forming an undisturbed BP-sequence. Figure 2 illustrates the c- phase reduction with increasing TPD at 40 kpa for simultaneous and alternate pulsation, respectively. Data for 12.5 kpa BP eff was omitted for clearness because of overlapping with 13.6 kpa. The 200 a - Phase (ms) 175 150 125 100 BP sequence (kpa) 6,5 17,9 50 60 70 80 90 100 110 TPD (mm) Figure 1. A-phase reduction with increased liner Shore hardness and teat penetration depth (60 c/min, 60% alternate, 40 kpa, 8 kpa vacuum drop). 180 c- Phase (ms) 160 140 120 alternate simultaneous BP sequence (kpa) 17,9 6,5 100 80 50 60 70 80 90 100 110 TPD (mm) Figure 2. C-phase reduction with increased liner Shore hardness and teat penetration depth (60 c/min, 60%, 40 kpa). 58 Conference on "Physiological and technical aspects of machine milking"

series 40/32 kpa had profiles very similar to alternate pulsation without vacuum drop and is not shown either. All recordings yielded parallel lines ranked with BP n. C-phases were shortest for 6.5 kpa BP n and longest 17.9 kpa BP n. This sequence is opposite to its influence on the a- phase with vacuum drop (Figure 1). ISO tests are carried out with standard teatcup plugs of 59 mm length. While short teats are common in the field, longer teats exist and penetration increases during milking (3,9). In the present analysis, teat length increased liner stiffness and reduced a- and c- phases due to less volume change. Caution is commanded when shortening teat cups to increase cluster flexibility or milkability of low udders because pulsation failure must be excluded. Effects of a- and c- phase changes will be analysed with regard to liner-open phase and release (10). Implications Butler, M.C. & J.E. Hillerton, 1989; Methods of assessing teatcup liner performance. J. Agric. Eng. Res. 44, 77-86 References Mein, G.A., M.R. Brown & D.M. Williams, 1983; Pulsation failure as a consequence of milking with short teatcup liners. J. Dairy Res. 50, 249-258 Ronningen, O. & A.D. Reitan, 1990; Teat lenght and penetration into teatcup during milking in Norwegian Red Cattle. J. Dairy Res. 57, 165-170 Thiel, C.C., P.A. Clough & D.N. Akam, 1964; Mechanics of machine milking. J. Dairy Res. 31, 303-313 Thiel, C.C., P.A. Clough, D.R. Westgarth & D.N. Akam, 1968; Factors affecting vacuum within the teatcup liner during milking. J. Dairy Res. 35, 303-316 Thum, E., H.-J. Rudovsky & B. z. Linden, 1975; Zur Bestimmung der Grenznut-zungsdauer für Zitzengummis. Agrartechnik 25, 78-81 Worstorff, H. & H. Stanzel, H., 1977; Untersuchungen zur Bewegung des Zitzengummis in Abhängigkeit von Einfaltdruck, Pulszyklus und Vakuumhöhe in Melkanlagen. Grdl. Landtechnik 27, 8-12 Worstorff, H., 1978; Vakuumverhältnisse im Melkzeug in Abhängigkeit von der Pulsierung. Milchwissenschaft 33, 159-162 Worstorff, H. & D. Schätzl, D., 2000; Zur Bedeutung des Einfaltverhaltens von Silicon-Zitzengummis für deren Melkeigenschaften. Milchwissenschaft 55, 183-186 Worstorff, H., E. Bilgery & H.H.D. Meyer, 2001; Effects of buckling pressure and teat length on calculated liner-open phases. Milchwissenschaft, submitted. 59