Simulation-based design of an energy-efficient vacuum control of a milking machine.
Voicu, Mariana-Claudia ; Schmidt, Ralf-Gunther ; Lammen, Benno 等
1. INTRODUCTION
In milking plants the milk removal from the cow's udder is
stimulated by the pulsating flow of ambient air and vacuum in teat-cups
between the flexible rubber liners and the shells. The vacuum level is
crucial for animal welfare and health. The effects of the vacuum on milk
yield, teat condition, and udder health are described in (Rasmussen et
al., 2000). In (Reinemann et al., 2003) an overview of research
activities in milking machine research is given.
During the milking process the vacuum level has to follow a given
profile within well-defined tolerances (ISO 5707, 1996). Disturbances
e.g. by animals kicking off milking liners or due to leakage during
applying the teat cup liners must be compensated. In general, the vacuum
pump is running at a nominal rotation speed. The vacuum level is
adjusted by means of a servo-valve in the vacuum system which can be
opened to ambient air. The pump and the engine are operated with an
unnecessary high power in an energy-inefficient way. Furthermore the
possibilities for improving the disturbance reaction of the control loop
are restricted.
The research work (Voicu et al., 2009) presented in this paper aims
to improve the vacuum quality in an interdisciplinary mechatronic
approach. The control of the vacuum by the servovalve is replaced by a
new cascade control including an inner control loop of the rotational
pump speed. The development of the control strategies was carried out
based on a simulation model of the plant. The model was validated at a
test bed. The control structure is shown in fig. 1. It includes the
frequency converter, asynchronous motor (ASM), the pump and the vacuum
system consisting of the various pipes and volumes such as vacuum tank,
milk receiver jar, pulsator, milk hose, claw and teat-cup.
[FIGURE 1 OMITTED]
2. MODELLING AND SIMULATION
The mathematical model of the vacuum system can be derived from the
conservation principles of fluid mechanics for mass, impulse, and energy
(Rist, 1996). A set of partial differential equations for the pressure
p, temperature T and flow velocity w depending on time and position is
obtained for each pipe of the vacuum system. Measurements at the test
bed (Voicu et al., 2009) have shown that the temperature in the vacuum
system is almost constant. Thus the energy conservation equation can be
neglected to simplify the mathematical model. This leads to a set of
differential equations (1) and (2) for each pipe of the vacuum system.
The pressure p and the flow velocity w are given as a function of time t
and position x in one dimension taking into account losses due to
friction and shape:
[MATHEMATICAL EXPRESSION NOT REPRODUCIBLE IN ASCII] (1)
[MATHEMATICAL EXPRESSION NOT REPRODUCIBLE IN ASCII] (2)
The constants k, [R.sub.i], [lambda] and D denote the adiabatic
exponent, specific gas constant, pipe friction coefficient and diameter.
The local dependency is discretised by introducing difference quotients
instead of local derivatives. This yields ordinary non-linear
differential equations. Special attention has to be paid to the boundary
conditions at bifurcations (Voicu et al., 2009).
For the overall model the vacuum pump, engine and frequency
converter have to be described, too. The pump is modelled by the static
characteristic diagrams of volume flow and performance. The model is
implemented under Matlab/Simulink as a modular library that can easily
be adapted to
different configurations of milking machines. The simulation results
were successfully verified based on the milking machine in the test bed
and on two other milking machines operating under practical conditions
on farms.
[FIGURE 2 OMITTED]
Fig. 2 shows a good correlation between the measurement of the
pressure in the supply air pipe with constant rotational pump speed and
simulation results of the test bed. The step response of the vacuum
system was simulated by opening a teat-cup and the pressure in the
pipelines is increasing 8 kPa in 22 seconds.
3. TEST BED
In cooperation with an industrial partner a test bed with 16 milk
units was built consisting of exchangeable combinations of different
asynchronous motors and pumps, a frequency converter, and the vacuum
system of the milking machine as shown in fig. 3. The milking process
consists of repeatedly opening (milk phase) and closing (massage phase)
the teat-cup liner. As the pulsator operates, it causes the chamber
between the shell and the liner to alternate regularly from vacuum to
air source.The end of the cow's teat is exposed to the vacuum and
the internal milk pressure within the cow's udder causes the milk
to be drawn out through the teat opening. From the pipelines, milk flows
by gravity into a receiver jar. A milk pump removes the milk from the
receiver jar and it transfers it to the bulk tank. A vacuum regulator is
located in the vacuum supply pipe between the vacuum reserve tank and
the sanitary trap which supplies the receiver jar with vacuum.
To analyse the functionality of the test bed, sensors for measuring
pressure, mass flow rate and temperature at various points were
installed in the pipelines.
[FIGURE 3 OMITTED]
4. CONTROL DESIGN
The simulation model was used to develop a new multi-loop vacuum
control of the milking machine (Popic, 2009). In a first step, the inner
feedback loops have been designed with classical methods in frequency
domain. Due to the nonlienarities of the plant the outer vacuum control
loop was developed in an empirical approach by means of simulations. The
vacuum control loop was optimized towards the reaction to disturbances
such as sudden leakages in the vacuum system. The control algorithms
were evaluated both in simulation and in experiments in the test bed. In
fig. 4 the reaction of the control loop to droping off and reapplying a
set of milking liners is depicted. The simulation results show a good
analogy to the measured test result.
As an important outcome of simulation and experiments the
performance of the vacuum control is mainly restricted by the limits of
the actuating variable of the frequency converter.
[FIGURE 4 OMITTED]
6. SUMMARY AND CONCLUSIONS
The simulation-based development of a new cascaded vacuum control
for milking machines via the rotational speed of the vacuum pump has
been described. It avoids energy-inefficient control interventions of
the servo valve in the vacuum pipe. The simulation model includes the
vacuum pump, the engine and the frequency converter as well as the fluid
dynamics of the vacuum system. The local dependency in the partial
differential equations of the pressure and flow velocity could be
discretized to obtain ordinary differential equations. The simulation
model was validated by measurements at an experimental milking machine.
The control algorithms were evaluated both in simulation and in
experiments. As a result it could be shown, that the performance of the
vacuum control is restricted by the limits of the actuating variable of
the frequency converter.
7. ACKNOWLEDGEMENTS
The authors wish to thank the work group innovative projects AGIP
with the Ministry for Science and Culture of the land Lower Saxony for
the granted sponsorship (grant apply number 2006.748).
8. REFERENCES
ISO 5707 (1996). Milking Machine Installations--Construction and
Performance', International Standards Organisation, Geneva,
Switzerland
Popic, N. (2009). Reglerentwurf und Simulation einer Melkanlage,
Master Thesis, Fachhochschule Osnabruck
Rasmussen, M.D., Madsen, N. P. (2000). Effects of Milking Vacuum,
Pulator Airline Vacuum, and Cluster Weight on Milk Yield, Teat
condition, and Udder Health, Journal of Dairy Science Vol. 83, No.1, pp.
77- 84
Reinemann, D. J., Graeme, A., Mein, G. A., Davis-Johnson, M.
(2003). Milking Machine Research: Past, Present and Future, 42nd annual
meeting of the National Mastitis Council, Fort Worth Texas, USA
Rist, D. (1996). Dynamik realer Gase, Springer Verlag, ISBN 978-3540586388
Voicu, M.-C., Popic, N., Schmidt, R.-G., Janecke, M., Lammen, B.
(2009). Energieeffiziente Regelung fur den tiergerechten Betrieb von
Melkanlagen mit neuartigen Pumpentypen, AGIP-Project 2006.748, Final
report, Osnabruck