[0001] The present invention relates to an electrical analog of a piping network having
a compressor therein and has particular reference to an electrical analog for simulating
the low frequency pulsations and surge characteristics of centrifugal compressors
and pumps and their interaction with their piping systems.
[0002] Centrifugal compressors have been widely used in pumping gaseous fluids through piping
systems, especially in the transportation of natural gas through pipelines.
[0003] Experimental work both in the laboratory and with field centrifugal compressors have
evidenced heretofore unexplained transient phenomena in at least two areas, namely:
1. the response of a compressor to pulsations from an external source which might
be introduced into either the compressor suction or discharge piping, and
2. the effects of compressor piping on machine surge.
[0004] Some of the more specific observed phenomena are:
a) A centrifugal compressor can either amplify or attenuate external pulsations.
b) Even with no positive source of pulsations in the piping system, low frequency
pulsations can be experienced at levels sufficiently high to fatigue compressor internals
or severely shake the piping.
c) These pulsation problems can often be mitigated by changing the pulsation response
of the compressor piping (lengths, diameters, etc.). High level pulsations have been
observed at frequencies ranging from less than one Hz and approaching zero, to several
hundred hertz. Frequencies are not harmonically related to and do not vary with centrifugal
compressor speed.
d) The severe pulsation frequencies normally relate to one of the major piqe resonances
of the piping systems, and measurements along the piping show a strong standing wave
pattern, often existing across or through the compressor.
e) The onset, frequency, and severity of machine surge can also vary as the piping
system is changed.
f) Pulsation levels are most severe when the compressor is situated at or near a velocity
maximum (pressure minimum) in the pulsation standing wave field.
g) External pulsations can induce surge in a centrifugal compressor.
[0005] It is the principal object of this invention to provide an analog of a centrifugal
compressor and its associated piping system in order that the above phenomena, as
well as others, can be studied and various variables optimized to minimize the effect
of pulsations and machine surge.
[0006] An electrical analog model of a piping network having a cylinder compressor is already
known from the US-A-3 581 077.
[0007] The known analog model has a capacitor pump for simulating the pumping action of
a compressor and has circuits connected to its output and input simulating the piping
upstream and downstream of the compressor. In use voltages are applied to the input
and output of the capacitor pump which are proportional to the suction and discharge
pressures of the compressor. The analog model includes electrical means for generating
a driving voltage for driving the capacitor pump at a driving input to cause it to
simulate the action of the cylinder compressor in that piping network. The electrical
means comprises a voltage generator having a sinusoidal output voltage and means for.
scaling a constant voltage by a factor to produce a reference voltage related to the
desired voltage at the outlet of the capacitor pump. In this known arrangement the
difference between the reference voltage and the desired voltage is measured and used
to modify the amplitude of the sinusoidal output voltage which in turn modifies the
output of the capacitor pump so that the output voltage equals the reference voltage.
Various electrical circuits are connected in series with the capacitor pump output
to simulate pipework, regulator stations, etc. downstream of the compressor station.
[0008] Varying compressor output pressures can be simulated by varying the constant voltage
source. Although the effects of certain changes downstream of the compressor can be
investigated in the known model no provision is made for producing a simulation of
low frequency pulsation and surge characteristics of a pump and pipelines functioning
together, in particular no provision is made for investigating the effects of pulsations
at the inlet to the compressor.
[0009] In orderto satisfy the principal object mentioned above there is provided, in accordance
with the present invention and starting from the known prior art arrangement of US-A-3
581 077, an electrical analog of a piping network having a compressor or pump therein
comprising:
a) a capacitor pump for simulating the pumping action of a compressor and having circuits
connected to its input and output simulating the piping upstream and downstream of
said compressor,the capacitor pump comprising two series connected diodes and a capacitor
connected to form a T-section, the driving input being the electrode of the capacitor
opposed to the diodes and the input and output of the capacitor pump being the anode
and cathode respectively of the series connected diodes;
b) means for applying voltages to the input and output of said capacitor pump which
are proportional to the suction and discharge pressures of said compressor; and
c) electrical means for generating a driving voltage for driving said capacitor pump
at a driving input, to cause it to simulate the action of the compressor in said piping
network, said electrical means comprising:
I) a voltage generator having a sinusoidal output voltage, and
II) means for scaling a constant voltage by a factor A,
said electrical analog being characterised in a centrifugal compressor by said electrical
means further comprising:
III) first means for sensing the suction voltage,
IV) means for scaling the output of said first means by a factor (B-1),
V) means for measuring the current I through the first said diode of said capacitor
pump and means for scaling it by a factor
where C is a numerical coefficient, Co is the value of said capacitor and f the frequency of said sinusoidal voltage in
(I),
VI) means for squaring and scaling said current flow respectively by a factor D,
VII) means for multiplying the suction voltage by the current and means for scaling
the result by a factor E;
VIII) means for adding the outputs of items II, III, IV, V, VI and VII to provide
a sum voltage; and
IX) means for making the amplitude of said sinusoidal output voltage proportional
to said sum voltage.
[0010] In effect the invention provides a nonlinear analog which effectively superimposes
the dynamic flow impedance characteristics of a piping system upon the compressor
curves so that the combined characteristics can be used to predict pulsation gain
or loss and system stability and the effect of various variables upon them.
[0011] The present invention will now be explained in more detail by way of example only
and with reference to the accompanying drawings wherein:
Figs. 1 to 6 are provided to facilitate an explanation of the theoretical background,
and
Fig. 7 shows an embodiment of the invention.
[0012] Referring firstly to Fig. 1 the curve 10 illustrates the basic nonlinear (square
law) nature of pipe flow resistance. Thus as its supply pressure is lowered, pipe
flow will decrease, stop or perhaps even backflow. If a centrifugal compressor is
the supply source, its performance curves can then be superimposed on the same plot
by plotting compressor discharge pressure versus discharge flow velocity as shown
by the curve 11 in Fig. 1, curve 11 being plotted for particular suction pressure
P
si. The operating point is the intersection of the two curves at point 0. Also shown
in Fig. 1 is a second performance curve of the compressor (a dashed line) which can
result from lowering suction pressure to P
S2 or compressor speed. In all cases, the operating point must fall on the pipe impedance
curve so long as steady flow conditions are assumed and the pipe steady flow impedance
is not changed. If, however, flow is modulated at higher frequencies where inertial
effects and line pack effects are significant, then the steady state impedance curve
sets the operating point but no longer controls the relations between pulsation pressures
and flows. This results in a different impedance line drawn to the operating point
and the slope of this dynamic impedance line is quite frequency sensitivefor typical
piping systems. The dynamic impedance frequency line is shown in Fig. 2 as line 12.
In Fig. 2, the operating curves 13, 14 and 15 are shown for a centrifugal compressor
operating at an average suction pressure P
so but pressure modulations cause this to vary from P
S1 to P
S2. Under these conditions, both the compressor curves and the pulsation impedance of
the discharge line will influence flow and discharge pressure modulations. The slope
of the dynamic impedance line 12 in Fig. 2 can be any positive value, theoretically,
from near zero to a very high value, depending on pulsation frequency and transient
response characteristics of the discharge piping.
[0013] Referring again to Fig. 2, it can be seen that when the discharge pressure modulation
(P
2-P
1) is larger than the suction pressure modulation (P
S2-P
S1) the compressor appears to amplify suction pressure pulsations, at least under those
particular operating conditions, with that particular piping system and at that particular
frequency. If the dynamic impedance line is sufficiently flat, then P
2-P
l can approach zero and the compressor will effectively attenuate suction pressure
pulsations.
[0014] Fig. 3 illustrates a plot of impedance versus length for the resonance mode of a
fundamental half wave in a pipe or vessel closed at both ends. Thus the slope of the
dynamic impedance line will vary from a relatively high value at the ends of the vessel
to essentially zero at the center of the vessel. Thus if a compressor feeds such a
vessel at its center point, a very low impedance would be evidenced at the frequency
depicted. On the other hand, a very high impedance would be seen at
' feed points near the closed ends. Therefore, the mangitude of the dynamic impedance
would vary markedly depending upon where the compressor feeds into the vessel and
upon the perturbation frequency.
[0015] Compressor surge has at times been a problem. To illustrate this, consider a set
of compressor curves as shown in Fig. 4 with the operating point B and a dynamic load
line as shown at Z
i. If the suction pressure is modulated from P
1 to P
2, the system is stable since in all cases the compressor head is sufficient to supply
the discharge pressure required by the dynamic load line. However, if suction pressure
drops below P
3, then the compressor cannot supply the piping pressure required to supply the necessary
flow and flow therefore diminishes. As flow diminishes, the compressor head inadequacy
becomes more pronounced and the entire flow regime collapses and surge results. The
piping may begin to backflow locally into the compressor discharge to make up for
the compressor inadequacy. As the suction pressure rises, then the compressor rebuilds
up the load line into a temporary stable condition, but with a rather violent flow
surge. The cycle then repeats.
[0016] As will be seen from Fig. 4, the steeper the slope of the dynamic load line, the
more stable the system insofar as surge is concerned and a very high impedance system
(Z
3) would never go into surge at all but would probable experience rotating stall instead.
[0017] The complexity of the pulsation pattern increases as the piping complexity increases
for example, the illustration in Fig. 4 implies that discharge pressure and flow are
in phase, a condition which can be achieved only in idealized piping systems. For
a real system with branches and/or area discontinuities, phase shifts occur, and in
fact approach 90 degrees near acoustic resonance. Such a condition is illustrated
in Fig. 5 where the orbit of flow versus pressure into a reactive piping system is
shown. The orbit of Fig. 5 for a reactive system is comparable to the line Z
3 in Fig. 4 for a non-reactive system, i.e. a state of stability. Fig. 6 illustrates
a surge orbit pattern for the reactive system of Fig. 5. The complexity of. Figs.
5 and 6 illustrate the need for simulating the various interactions of parameters
of the compressor and piping system.
[0018] In accordance with this invention, an analog is provided to simulate the operation
of a centrifugal compressor utilizing an actual (non-linear) head curve in order to,
among other things, simulate surge instability frequencies and amplitudes. Thus, it
has been found that a conventional capacitor pump when driven by a sinusoidal voltage
proportional to the sum of at-least 3, and preferably 5 values, will simulate the
dynamic characteristics of a centrifugal compressor. When the input and output of
the analog are connected to suitable delay lines and the liketo simulate various piping
configurations, the interaction of the compressor with the piping system can be simulated.
[0019] Referring to Fig. 7, there is shown a conventional capacitor pump comprising the
diodes D
1 and D
2 and the capacitor C
o, one form of which is described in the US―A―2,951,638 along with the attendant delay
lines for simulating a piping system. Thus there is provided a capacitor pump for
simulating the pumping action of a centrifugal compressor and having circuits (not
shown) connected to the input and output analogizing the piping upstream and downstream
of the compressor.
[0020] Means are also supplied for applying a voltage E
s to the input of the capacitor pump which is proportional to the suction pressure
of the compressor, this means being indicated by "Suction Es". Similarly, means are
provided for applying a voltage to the output of the capacitor pump proportional to
the discharge pressure and indicated by the term "Discharge E
o".
[0021] F
s and F
d are low pass filters which are inserted to filter out any stray alternating currents
which may have an adverse effect on the capacitor pump.
[0022] Electrical means are provided for driving the capacitor pump to cause it to simulate
the action of the centrifugal compressor in the piping network. The driving means
has a sinusoidal voltage output which is proportional to the sum
[0023] The driving means includes a first means for sensing the suction voltage here shown
as amplifier A2. Means are also provided for scaling the output of the first means
(A2) by a first factor (B-1), here illustrated as the potentiometer B, to. yield the
value (B-1) E
s in equation (1). (B-1) is derived by appropriate feed back around amplifier A2 as
shown from the resistor network 9R and R.
[0024] Means are also provided for sensing and scaling the current flow through the capacitor
pump by a second factor:
to yield the value
Where C is a numerical coefficient and C
o is the value of capacitance C
o in the circuit. This means is illustrated as including the amplifier A8 and potentiometer
alpha. The latter is set in accordance with the calculated value of equation (2) above.
In this connection, the components within the dashed block labeled "Meter" is a Hall
effect metering circuit. In any event, the current flowing to amplifier A8 is directly
proportional to the current flowing through the capacitor pump.
[0025] As a part of the driving means, means are also provided for squaring and scaling
the current flow through the capacitor pump to obtain the value:
This means includes a potentiometer D for scaling the current being fed to amplifier
A1 and a wide band precision analog multiplier M1 which squares the current value
multiplied by the factor D.
[0026] Means are also provided for scaling a constant voltage by a fourth factor which includes
a constant voltage source V
cc, and a scaling potentiometer A to obtain value A.
[0027] Means are also provided for multiplying the suction voltage E
s by the current flowing through the capacitor pump and scaling the result by a fifth
factor E to obtain the value:
shown and the output is scaled in potentiometer E and then passed to amplifier A6.
[0028] Means are also provided for adding the foregoing values in accordance with equation
(1) to provide a sum voltage E
B. This means of addition includes resistors R
A, R
B, R
c, R
D and R
E hooked into an adding circuit as shown and amplifier A7. The various factors involved
in these means are selected to define the coefficient of the terms of the above equation
which equation in turn defines the sum voltage required for the electrical driving
means to cause the capacitor pump to simulate the behavior of the centrifugal compressor.
As shown in the drawing, this sum voltage is applied to a broad band precision analog
multiplier M3 where the sum voltage is multiplied by a sinusoidal voltage EG of constant
magnitude and frequency. As a result, the sinusoidal voltage fed to amplifier A5 has
an amplitude proportional to the sum voltage.
[0029] It is preferred that the amplifiers A1 through A9 all be wide band precision analog
amplifiers.
[0030] To simulate a given compressor head curve and therefore to arrive at an E
B which will drive the capacitor pump to cause such simulation of such a given head
curve, a current modulator CM can be provided as shown in Fig. 7 and an oscilloscope
connected as shown to display the output of the capacitor pump. The current modulator
causes a periodic variation in current flow and provides an analog voltage output
which is proportioned to such current, which voltage is used to drive the X-axis of
the oscilloscope. The Y-axis is driven directly by E
D. Then using the given head curve, the various coefficients of equation 1 can be adjusted
in the circuit of Fig. 7 to force conformance of the capacitor pump output curve,
which is E
D, to the desired head or performance curve.
An electrical analog of a piping network having a compressor or pump therein comprising:
a) a capacitor pump (D1, D2 Co) for simulating the pumping action of a compressor and having circuits connected
to its input and output simulating the piping upstream and downstream of said compressor,
the capacitor pump comprising two series connected diodes (D1, DZ) and a capacitor (Co) connected to form a T-section, the driving input being the electrode of the capacitor
opposed to the diodes and the input and output of the capacitor pump being the anode
and cathode respectively of the series connected diodes;
b) means for applying voltages (Es and ED respectively) to the input and output of said capacitor pump which are proportional
to the suction and discharge pressures of said compressor and
c) electrical means for generating a driving voltage for driving said capacitor pump
at a driving input, to cause it to simulate the action of the compressor in said piping
network, said electrical means comprising
I) a voltage generator having a sinusoidal output voltage (EG) of frequency (f), and
II) means (A4, A) for scaling a constant voltage (Vcc) by a factor A,
said electrical analog being characterised in a centrifugal compressor by said electrical
means further comprising:
III) first means (A2) for sensing the suction voltage (Es),
IV) means (B, A3) for scaling the output of said first means (A2) by a factor (B-1),
V) means for measuring the current I through the first said diode (D1) of said capacitor pump (D1, D2, Co) and means (A8, Alpha, A9) for scaling it by a factor
where C is a numerical coefficient, Co is the value of said capacitor and f the frequency of said sinusoidal voltage in
(I)
VI) means (D, A1, M1) for squaring and scaling said current flow respectively by a
factor D
VII) means (M2) for multiplying the suction voltage by the current and means (E, A6)
for scaling the result by a factor E;
VIII) means (RA, RB, Rc, RD and RE, A7) for adding the outputs of items (II), (III), (IV), (V), (VI) and (VII) to provide
a sum voltage EB; and
IX) means (M3) for making the amplitude of said sinusoidal output voltage (EG) proportional
to said sum voltage.
1. Elektrische Simulationseinrichtung eines Röhrennetzwerkes, das einen Kompressor
oder eine Pumpe enthält, mit:
a) einer Kondensatorpumpe (D1, D2, Co) zum Simulieren der Pumpwirkung eines Kompressors mit an ihrem Eingang und ihrem
Ausgang angeschlossenen Kreisen, die die zustrom- un abstromseitige Verrohrung des
Kompressors simulieren, wobei die Kondensatorpumpe zwei in Reihe verbundene Dioden
(D1, D2) und einen Kondensator (Co) umfaßt, die zur Bildung eines T-Gliedes miteinander verbunden sind, wobei der Antriebseingang
die den Dioden gegenüberliegende Elektrode des Kondensators und der Eingang und der
Ausgang der Kondensatorpumpe die Anode bzw. die Katode der in Reihe geschalteten Dioden
sind;
b) Mitteln zum Anlegen von Spannungen (Es bzw. Eo), die den Ansaug- und Ausstoß-Druckwerten des Kompressors proportional sind, an den
Eingang bzw. Ausgang der Kondensatorpumpe, und
c) elektrischen Einrichtungen zur Erzeugung einer Antriebsspannung zum Antreiben der
Kondensatorpumpe an einem Antriebseingang, um sie die Wirkung des Kompressors in dem
Röhrennetzwerk simulieren zu lassen, wobei die elektrischen Einrichtungen enthalten
I) einen Spannungsgenerator mit einer sinusförmigen Ausgangsspannung (EG) der Frequenz (f) und
11) Einrichtungen (A4, A) zum maßstäblichen Verändern einer konstanten Spannung (Vcc) um einen Faktor A,
wobei die elektrische Simulationseinrichtung bei einem Zentrifugalkompressor dadurch
gekennzeichnet ist, daß die elektrische Einrichtung weiter enthält:
III) erste Einrichtungen (A2) zum Erfassen der Saugspannung (Es),
IV) Einrichtungen (B, A3) zum maßstäblichen Verändern des Ausgangssignales der ersten
Einrichtung (A2) mit einem Faktor (B-1),
V) Einrichtungen zum Messen des Stromes I durch die erste Diode (D1) der Kondensatorpumpe (D1, D2, Co) und Einrichtungen (A8, ALPHA, A9) zum maßstäblichen Verändern desselben mit einem
Faktor
wobei C ein numerischer Koeffizient,
Co der Wert des Kondensators und f die Frequenz der Sinusspannung in (I) ist,
VI) Einrichtungen (D, A1, M1) zum Quadratieren und maßstäblichen Verändern des Stromflusses
mit einem Faktor D,
VII) Einrichtungen (M2) zum Multiplizieren der Saugspannung mit dem Strom und Einrichtungen
(E, A6) zum maßstäblichen Verändern des Resultates mit einem Faktor E;
VIII) Einrichtungen (RA, Re, RD, RC und RE, A7) zum Addieren der Ausgangssignale der Gegenstände (11), (111), (IV), (V), (VI)
und (VII) zur Schaffung einer Summenspannung (EB); und
IX) Einrichtungen (M3), um die Amplitude der sinusförmigen Ausgangsspannung (EG) proportional der Summenspannung zu machen.
Simulateur électrique d'un réseau de canalisations comportant un compresseur ou une
pompe, comprenant:
a) une pompe à condensateur (D1, D2, Co) destinée à simuler l'action de pompage d'un compresseur et possédant des circuits
connectés à ses entrées et sorties, simulant la canalisation an amont et en aval dudit
compresseur, la pompe à condensateur comprenant deux diodes (D1, D2) montées en série et un condensateur (Co) monté de façon à former une section en T, l'entrée d'attaque étant l'électrode du
condensateur opposée aux diodes et l'entrée et la sortie de la pompe à condensateur
étant l'anode et la cathode, respectivément, des diodes montées en série;
b) des moyens destinés à appliquer des tensions (Es et ED, respectivement) à l'entrée et à la sortie de ladite pompe à condensateur, qui sont
proportionnelles aux pressions d'aspiration et de refoulement dudit compresseur, et
c) des moyens électriques destinés à générer une tension de commande pour la commande
de ladite pompe à condensateur à une entrée de commande, afine de l'amener à simuler
l'action du compresseur dans ledit réseau de canalisations, lesdits moyens électriques
comprenant
(I) un générateur de tension ayant une tension de sortie sinusoîdale (EG) de fréquence
(f), et
II) des moyens (A4, A) destines à démultiplier une tension constante (Vcc) par un facteur (A),
ledit simulateur électrique étant caractérisé, dans un compresseur centrifuge, par
lesdites moyens électriques comprenant en outre:
III) des premiers moyens (A2) destinés à détecter la tension d'aspiration (Es),
IV) des moyens (B, A3) destinés à démultiplier le signal de sortie desdits premiers
moyens (A2) par un facteur (B-1),
V) des moyens destinés à mesurer le courant traversant la première (D1) desdites diodes de ladite pompe à condensateur (D1, D2, Co) et des moyens (A8, ALPHA, A9) destinés à le démultiplier par un facteur
où C est un coefficient numérique, Co est la valeur dudit condensateur et f la fréquence de ladite tension sinusoîdale
dans (I)
VI) des moyens (D, A1, M1) destinés à conformer et démultiplier ledit écoulement de
courant, respectivement, par un facteur D,
VII) des moyens (M2) destinés à multiplier la tension d'aspiration par le courant
et des moyens (E, A6) destinés à démultiplier le résultat par un facteur E;
VIII) des moyens (RA, RB, RC, RD et RE, A7) destinés à additionner les sorties des points (II), (III), (IV), (V), (VI) et
(VII) pour produire une tension de somme EB; et
IX) des moyens (M3) destinés à rendre l'amplitude de ladite tension de sortie sinusoîdale
(EG) proportionnelle à ladite tension de somme.