[0001] The present invention relates to a rotary screw compressor and more particularly
to a system and a method to control the discharge capacity of the screw compressor
by using a combination bypassing the compressed medium and by varying the speed of
the motor of the compressor.
Background and related art
[0002] Screw compressors are widely used for various industrial applications due its simplicity
of operation, reliable & consistent performance over its life span. A screw compressor
generally includes a male screw rotor and a female screw rotor in engagement with
each other. These rotors are rotated by a prime mover like an electric motor, engine
etc. to compress an intake air/gas to be supplied to an equipment, appliance or a
process requiring compressed air or any other gas for its operation or functioning.
[0003] A screw compressor is normally designed for operating at a particular speed for optimum
performance but most of the time it does not operate at the designed speed due to
lack of demand of compressed air or any other gas from the dependent equipment or
appliance or process, which requires supply of compressed air or any other gas for
its operation or functioning. The part load operation of the screw compressor results
into degradation of the performance and energy efficiency of the same. In ideal condition
a compression system should operate in such a way that the compressor flow delivery
is always in line with the demand without causing any additional energy & efficiency
losses.
[0004] In order to ensure that the flow delivery of the compressed air/gas from a screw
compressor is always in line of the demand several methods for capacity controls are
in use and reported in various research literatures.
[0005] In a known way, capacity control in a screw compressor is performed by means of sliding
valve mechanism, in which a sliding valve operated through suitable control mechanism
is used to control the opening area of the bleeding port. This method offers unlimited
capacity control over its capacity control range. But involvement of various sliding
parts makes unsuitable due to problems related to maintenance.
[0006] In another known method, the capacity control operation is performed by a suction
throttle, wherein controlling the valve at the compressor suction controls air mass
entering into the compressor. The throttling of air through this valve causes pressure
losses and corresponding increase in total pressure ratio and there by power input
which offsets the gains of capacity control.
[0007] In yet another known method of capacity control by blow off by letting out of the
pressurized air and also small quantity of oil mixed with pressurized air. This method
doesn't offer any advantages on power consumption side and at the same time it can
not be used for oil flooded compressors.
[0008] The capacity control of a rotary compressor motor is also performed by using multi-pole
electric motor (Two Pole/Four Pole/Six Pole motors), which is not a dynamic type ,as
disclosed in
DE 4 221 494 A1, considered to represent the closest prior art document. In another known method,
the capacity Control of Compressor is performed by varying the speed of the motor,
by variable speed frequency drives. This method is efficient as it has a control over
the capacity control process. The major drawbacks of this method are high cost and
power reduction is not in proportional to capacity reduction with decrease in rotational
speed of the equipment.
[0009] In the US patent application
US 2003/0007879, a screw compressor for accommodating low compression ratio and pressure variation
is described, which is intended to be achieved by varying the internal volume ratio
by means of positioning of an internal volume ratio control valve at a pre-determined
position. Further a bypass valve is arranged which operates between discharge and
suction zones of the compressor.
[0010] As outlined above, many capacity control methods are available and are in use for
dynamic capacity control of the screw compressors. The main drawback of these methods
is that these systems operate most efficiently only for small capacity reduction ranges
e.g. up to 20 to 30 % from 100 % capacity. These systems are also able to reduce the
capacity further downwards but in such cases the reduction in screw compressor input
power is same as that of reduction in capacity.
[0011] Due to problem of smaller range of capacity reduction ability of various dynamic
capacity control methods, the market trend is shifting towards using the screw compression
systems that are equipped with Variable Frequency Drives (VFD). These screw compressor
systems equipped with VFD system offers a very fine control over the screw compressor
capacity from 30 to 100 % range. While these systems with VFD matches well the delivery
of the compressed air or any other gas to as required by the dependent equipment,
appliance or process. The VFD as an additional component of a screw compressor system,
itself generates energy losses in the form of heat generation during the process of
supply frequency modulation. In addition to this energy loss it also creates distortions
in the input supply grid & increase sound level. By modulating the supply frequency,
the VFD runs the dependent screw compressor system at lower or higher revolutions.
The dependent systems like screw compressors operates most efficiently at an optimum
speed and running a screw compressor at lower speeds than the optimum or designed
speed, degrades its performance due to various losses generated because of operating
at lower speeds like reduced volumetric efficiency at lower speeds etc. So apparently
even if the system's supply and demand matches well, the energy efficiency of the
complete system is very poor.
Objects of the present invention
[0012] The primary object of the present invention is to provide a system and a method for
a screw compressor with in-built bypass flow arrangement and driven by a multi-speed
or multi-capacity (speed and power) electric motor to generate, regulate the flow
or delivery of the compressed air or gas.
[0013] An object of the present invention is to provide a system and method where no variable
frequency drive (VFD) is used.
Summary of the invention
[0014] The present invention provides a system and a method for implementing capacity control
in a screw compressor, said system comprising; a screw compressor, said compressor
driven by a multi-capacity (speed and power)motor to compress air or gas medium, a
bypass inlet member with a bypass valve, extending from the high pressure zone to
the low pressure zone of the screw compressor to recirculate the gaseous medium, a
bypass valve controller functionally connected to said bypass valve, a motor controller
functionally connected to the motor to effect multi-capacity (speed and power) operations,
a main processing control unit disposed to control the bypass valve and multi-capacity
(speed and power) operations, measuring means disposed on the compressed medium passage
for measuring the changes in the pressure and/or temperature changes in the form of
signals, a signal converter functionally connected to the main processing unit and
the measuring means to receive the signals, and said motor controller and bypass valve
controller are functionally connected to the main processing unit to perform the capacity
control of the screw compressor.
Brief description of the accompanied diagrams
[0015]
Fig 1 is a schematic expression of the system of the present invention.
Fig 2 is partial sectional view of the of the screw compressor of the present invention
equipped with a bypass line connected to main controller.
Fig 3 is a side view of a motor drive depicting the functional connectivity of the drive
elements with the main controller.
Fig 4 is a flow chart depicting the method of capacity control of the rotary screw compressor
of the present invention.
Fig 5 is a graphical depiction of comparative account of the efficiency loss of the between
the screw compressor of the present invention and a screw compressor driven by a variable
frequency drive.
Fig 6 is a graphical representation of the sequence of operations/method of capacity control
of the rotary screw compressor of the present invention for a 50Hz frequency power
supply condition.
Detailed description of the invention
[0016] Accordingly, the present invention provides a rotary screw compressor system and
a method to control the discharge capacity of the screw compressor by using a combination
of bypassing the compressed air or gas and by varying the speed of the motor of the
compressor. The constructional features of the system of the present invention are
described by referring to
Fig 1-3.
[0017] Initially, referring to
Fig 1, which is a schematic diagram of the compression system of the present invention,
wherein a rotary screw compressor
1 is driven by a multi-capacity (speed and power) motor
2 to compress a gas or air medium and to discharge the compressed medium.
[0018] The screw compressor
1 comprises rotor housing in which male rotor
11 and female rotor
12 rotates in continuous engagement. The gaseous medium air or gas enters into the rotor
housing through the upstream pipe or intake pipe
13 and thereafter compressed to the desired pressure level during its transportation
from suction end to discharge end of the rotor housing. This compressed air or gas
is then transported to the end applications
6 through the network of various sub-components of a compression system hereinafter
described.
Constructional features of the bypass arrangement of the present invention
[0019] A bypass line
14 extending from a bypass port
18 is provided with a bypass valve
10, said bypass line 14 extending from the high-pressure zone to the low-pressure zone
of the screw compressor to recirculate the gas or air medium. The bypass valve of
the present invention either a vertically operated or a rotary valve, which is known
in the art to provide a controlled flow of the medium. A by pass valve controller
7, which is a device adapted to control the bypass valve
10. The valve controller
7 is a stepper motor or any suitable mechanical device that can drive or transmit the
driving functions to the bypass valve
10. The bypass arrangement of the present can also be implemented by adapting a sliding
valve mechanism.
Constructional features of the motor drive arrangement of the present invention
[0020] A multi-capacity (speed and power) electric motor
2 with a shaft used as a prime mover for the screw compressor
1 through suitable transmission assembly
19. The suitable power transmission mechanism
19 includes a direct coupling of the shaft of motor
2 with male rotor
11 or a gear drive or a belt pulley arrangement. The multi-capacity (speed and power)
2 is generally equipped with an in-built electrical winding network suitable to operate
the multi-capacity (speed and power) motor
2 at different pole configurations e.g. 2-pole, 4-pole, 6-pole etc. Considering the
working requirements of the compressor 1 the pole configuration of the motor
2 is configured to run at a particular speed by activation of the particular pole configuration.
[0021] A motor controller device
9 is connected the motor
2 to provide activation of the required winding configuration. The motor controller
9 is a stepper motor or any suitable mechanical device or electrical contactors that
can drive or transmit the driving functions to the motor
2.
[0022] An oil separator tank
3 is disposed to collect the compressed discharge from the compressor
1 to filter the residual oil that is carried by the discharge gas or air during the
compression operations. However, it is understood here that this requirement of having
an oil separator tank may not be necessary if an oil-free screw compressor is used
in place of oil-flooded screw compressors.
[0023] A storage container
5 is generally used as a temporary storage device, for storing the compressed gas or
air and to further supply to end applications
6, wherever there is requirement of compressed air or gas supply
[0024] A non-return valve
4 is disposed between the oil separator tank 3 and the storage container
5, to facilitate unidirectional flow of the compressed air or gas.
[0025] A plurality of sensing means (not shown in figures), is disposed on the storage container
5. The sensing means can also be disposed on any location of the discharge passage between
compressor outlet
13a and end applications
6. The sensing means are pressure transducers, the can sense a change in the pressure
levels and transmit the same as analog signals
15. In the present invention, as an exemplary embodiment sensing is performed by using
pressure transducers. However, alternatively either a temperature transducer or a
combination of pressure and temperature transducers can also be used. It is also within
purview of this invention to use a flow transducer to measure the flow rate of the
discharged compressed gas or air to generate corresponding signals
15.
[0026] A signal converter interface unit
20 is disposed to convert the analog signals
15 generated from the sensing means to convert the same in to digital signals. The digital
signals thus converted are further transmitted to main processing unit
8, which is hereinafter described.
Main processing control unit
[0027] Main processing control unit
8 of the present invention is a micro-controller based device having an instruction
set to control the various connected devices including motor control unit
9, bypass control unit
7. The micro controller used in the present invention is a device, which is generally
used to perform the control operations of this nature.
Integration of the main control-processing unit with bypass and motor controllers
[0028] Main processing control unit
8 is connected by means of an electrically conductive material to bypass controller
7 and motor controller
9.
Method of implementation of capacity control of the screw compressor by using the
system of the present invention
[0029] The method of implementation of the capacity control of the screw compressor of the
present invention is now described.
[0030] The process steps of the present invention is described by referring to various phases
of operation that the compressor of the present invention undergoes to control the
bypass flow of the compressed air or gas and the multi-capacity (speed and power)
of the motor
2 to generate and regulate the flow or delivery of the compressed air or gas.
Initialisation process
[0031] A method to control the discharge capacity of the screw compressor
1 by using the system of the present invention is now described. The screw compressor
1 along with the controlling elements and other devices as explained above is energized
to carry out the process of compression of air or gas. At the outset, the main processing
control unit
8, which is a micro-controller based is loaded with an instruction set to control the
operational aspects of the system.
[0032] In order to describe the working principle of the proposed step-less capacity control
system, as an exemplary embodiment, a three-speed electric motor
2 with required number of poles and electrical windings/configurations for achieving
these three speeds
(N1, N2 & N3) is used to perform the capacity control of the screw compressor
1 of the present invention.
Assignment of speed step values to the main processing control unit
[0033] After considering the speed configuration of the motor
2, corresponding speed steps are allocated to each of the designated
N1, N2 &
N3 as
1500, 1000 &
750 rpm respectively. It is also to be noted here that the value of
N1 is always maximum, which is generally the maximum value of the speed provided to
the motor during fabrication. Once the maximum speed value
N1 of the motor
2 is established, a corresponding decreasing speed values are
N2 & N3. These values
N1, N2 & N3 are used as input data for the main processing control unit
8 to enable the control unit
8 in regulating the desired rpm of the motor
2 at various stages of operation of the screw compressor
1. It is to be understood here the values of
N correspond to the motor speed configuration of any selected motor. Therefore
N values can vary from
N1 to
Nn.
Assignment of pressure values to the main processing control unit
[0034] In any given compressor-based system, the variation in the discharge pressure is
a function of demand of the compressed air or gas of the dependant applications
6. Therefore, it is necessary control the desired pressure at various stages of the
working of the compressor. In the present invention, considering the speed values
N1, N2 & N3, corresponding pressure values are assigned in the form of
SP1, SP2 & SP3 to the main processing control unit
8 as input data.
[0035] Since, the discharge pressure of the compressor of the present invention is constantly
monitored during the operation, it is necessary to measure these values in order to
provide a continuous input to the main control unit
8. As described above, these values are measured by the sensing means. The value of
discharge pressure at a given point of time is designated as
MP.
[0036] After the screw compressor
1 starts functioning, the constantly monitored
MP pressure value is compared with the pressure values
SP1, SP2 and SP3 for finding the matching values. In the event of the matching of the value of MP
with any one of the values
of SP1, SP2 or SP3, the motor control unit
9, effect the change in the motor speed, by selecting the rpm from any one of the
N1, N2 or N3 values, which correspond to
SP1 or SP2 or
SP3. Based on the above described initialization phase the working principle of the screw
compressor
1 system of the present invention is now described. During operation the screw compressor
system of the present invention is implemented in the following operational phases
viz., Start-up phase, Working pressure built-up phase and Capacity control phase.
Start-up phase:
[0037] During start-up phase of the screw compressor
1, active pole configuration of the motor
2 is suitable to run the motor
2 at a maximum speed available i.e. the motor
2 runs at speed value
N1. At this stage, the bypass valve
10 is completely closed, since the normal pressure conditions are experienced in the
initial stages of the operation.
Working pressure built-up phase:
[0038] It is understood that the pressure value
SP1 is designates as a normal working pressure of the screw compressor
1. During working pressure built-up phase, the main processing control unit
8 will run the motor
2 at speed
N1 with bypass control valve
10 in completely closed condition until the continuously monitored discharge pressure
value
MP is equal to
SP1.
Capacity Control phase:
[0039] The capacity control phase starts after completion of the working pressure built-up
phase. The screw compressor
1 is required to be operated in capacity control phase whenever there is a reduction
in the demand of the compressed air or gas from the end applications
6. In the capacity control phase, the pressure sensing elements sense the pressure of
the compressed air or gas and generates the signal
15, in the form of an analog signal as an input to the analog-to-digital converter (ADC)
20 and thereafter supplied to the main processing control unit
8 for further processing.
[0040] Now by referring to the
Fig. 4, the logical operations or instruction set of the main processing control unit
8 are explained.
[0041] In the event where the continuously monitored pressure value
MP is less than or equal to
SP1, the main processing control unit
8 will not generate any signal for motor control unit
9 and for bypass control unit
7 so the motor keeps on running at
N1 with bypass valve
10 in completely closed state.
[0042] In the event where the continuously monitored pressure value
MP is less than pressure value
SP2 and greater than the pressure value
SP1, the main processing control unit
8 will generate signal
17 for the bypass control unit
7 and no signal will be generated for motor control unit
9 to enable the motor to run at the maximum speed
N1. On receiving the signal
17, the bypass control unit 7, opens up the bypass valve
10 till the value of
MP is equal to the value of
SP1.
[0043] In the event where the continuously monitored pressure value of
MP is equal to
SP2, the main processing control unit
8 generates signals
16 and
17. In response to the signal
17, the bypass control unit 7, closes the bypass valve
10 completely. After this closure of the valve
10 in response to signal
17, the motor control unit
9 changes motor
2 speed value to
N2 i.e. motor 2 starts running at
N2.
[0044] In the event where the continuously monitored pressure value
MP is less than
SP3 and greater than
SP2, the main processing control unit
8 does not generate the signal
16 and generates only the signal
17. In response to signal
17, the bypass control unit
7 opens-up the bypass valve
10 till the value
of MP is equal to
SP1.
[0045] In the event where the continuously monitored pressure value of
MP is equal to
SP3, the main processing control unit
8 generates the signals
16 and
17. In response to signal
17 the bypass control unit
7, closes the bypass valve
10 completely and there after in response to signal
17, the motor control unit
9 changes the motor speed to speed value
N3 i.e. motor
2 starts running at
N3.
[0046] In the event where the continuously monitored pressure value
MP is greater than
SP3, the main processing control unit
8 generates only the signal
17 and no signal
16 is generated. In response to signal
17, the bypass control unit
7, opens up the bypass valve
10 till the
MP is equal to
SP1. By executing the above set of operations, continuous capacity control of the screw
compressor of the present invention is ensured.
[0047] It is to be noted here that the above set of operations are described considering
3-speed motor. It is appreciated by a person skilled in the art that the above operations
are iterated 'n' number of times depending on the pressure and motor speed factors.
[0048] The system of the present invention can also be implemented by dispensing with the
bypass inlet member, which is used to bypass the intermediately compressed air or
gas. In such case, the multi-capacity (speed and power) of the motor is achieved by
step-control arrangement. In such an arrangement the capacity control will be in stages.
[0049] The performance of the screw compressor of the present invention, where VFD is not
used is described. The factors that contribute to the overall efficiency of the compressor
system are compressor speed and motor efficiency. Accordingly, the system of the present
invention is implemented to optimize these two factors resulting in the improved capacity
control and efficiency of the compressor. In order to determine the enhanced efficiency
of the compressor of the present invention, a comparative account with compressors
run with VFD is made and results are tabulated in
Table 1. However, it is to be noted here that the comparative values are indicative in nature,
since these values are subject to change depending on the various capacities of the
compressors.
TABLE 1
| Compressor Capacity Range (%) |
Screw compressor without bypass flow arrangement and driven a standard single speed
motor with a VFD |
Screw compressor with in-built bypass flow arrangement and driven by a multi-capacity
(speed and power) motor |
| Efficiency Loss (%) |
Efficiency Loss (%) |
| |
Speed (%) |
VFD |
Motor |
Compresor |
Total |
Speed (%) |
Motor |
Compresor |
Total |
| 100 |
100 |
0 |
0 |
0 |
0 |
100 |
0 |
0 |
0 |
| 67 |
67 |
4 |
5 |
8 |
17 |
100 |
0 |
0 |
0 |
| 66.5 |
67 |
4 |
5 |
8 |
17 |
67 |
0 |
8 |
8 |
| 50.5 |
51 |
4 |
10 |
12 |
26 |
67 |
0 |
12 |
12 |
| 50 |
50 |
4 |
10 |
12 |
26 |
50 |
0 |
12 |
12 |
| 20 |
20 |
4 |
15 |
20 |
39 |
50 |
0 |
12 |
12 |
[0050] It can be seen from the above
Table 1 that the compressor of the present invention where VFD is not used is much more efficient
than the compressors run with VFD. For instance if the capacity reduction required
is 80 %, in case of compressors with VFD, the same need to be run at 20 % of the desired
speed. However, in the compressor of the present invention for the same capacity reduction
of 80%, the compressor is run at the 50% of the designed speed.
[0051] The results of
Table 1 are plotted on
Fig 5, by considering compressor capacity (%) and overall efficiency loss (%), which clearly
shows the enhanced performance of the compressor of the present invention.
[0052] Now by referring to
Fig 6, which is a graphical representation of the sequence of operations/method of capacity
control of the rotary screw compressor of the present invention for a 50Hz frequency
power supply condition. The same method can be made applicable for other frequency
conditions such as 60Hz frequency condition. The sequence of operations or the method
of capacity control is explained in
Fig.6. The point "A" in this figure corresponds to the 100% capacity of the compressor.
At this point, the multi-capacity motor 2 operates at its maximum design speed and
the by pass valve 10 is fully closed. Between A-B, bypass valve gradually opens based
on the capacity control requirement. The capacity at "B" with full opening of bypass
valve 10 will be corresponding to the capacity of the compressor at next designed
speed of motor at Point "C" with by-pass valve fully closed. Hence between B-C motor
speed changes to next design speed of motor and at closes the bypass valve completely.
The above sequence follows between C-D and D-E and so on.
Assumptions made for preparing performance comparison Table 1: -
[0053]
- 1. 100 % means the screw compressor 1 performance at optimum rotational speed for a given compressor.
- 2. The efficiency losses of the VFD have been taken as 4 % for any reduction in supply
frequency.
- 3. Incase of a screw compressor 1 driven by a with multi-capacity (speed and power) motor 2, no motor efficiency losses
have been considered as these motors are designed specially to operate at same efficiency
for various active pole configurations or different speed steps.
- 4. Incase of a screw compressor 1 without bypass flow arrangement and driven by a standard single speed motor 1 equipped with a VFD, there will be marginal drop in motor 2 efficiency when it runs
at lower speed as this motor 1 is standard one designed to operate most efficiently only for a particular active
or designed pole configuration.
- 5. Screw Compressor 1 overall efficiency reduction has been assumed as 10 % for a reduction of 40 % in
screw compressor 1 speed from its optimum or designed speed magnitude.
- 6. Various magnitudes given in performance comparison Table 1 for a given range of 20 to 100 % have been calculated proportionately.
[0054] Various magnitudes given in performance comparison
Table 1 is only indicative nature and can defer from system to system.
[0055] Therefore, the present invention provides a system for implementing capacity control
in a screw compressor, said system comprising; a screw compressor, said compressor
driven by a multi-capacity (speed and power) motor to compress a medium, a bypass
inlet member with a bypass valve, extending from the high pressure zone to the low
pressure zone of the screw compressor to recirculate the gaseous medium, a bypass
valve controller functionally connected to said bypass valve, a motor controller functionally
connected to the motor to effect multi-capacity (speed and power) operations, a main
processing control unit disposed to control the bypass valve and multi-capacity (speed
and power) operations, measuring means disposed on the compressed medium passage for
measuring the changes in the pressure and/or temperature changes in the form of signals,
a signal converter functionally connected to the main processing unit and the measuring
means to receive the signals, and said motor controller and bypass valve controller
are functionally connected to the main processing unit to perform the capacity control
of the screw compressor.
[0056] In an embodiment of the present invention, the system wherein the measuring means
is pressure or temperature transducers.
[0057] In another embodiment of the present invention, the system wherein the bypass inlet
member on the compressor where pressure of the air or gas moving through the screw
compressor has a positive pressure.
[0058] The present invention also provides a method for method for capacity control in a
screw compressor as claimed in claim 1, said method comprising the steps of; setting
a plurality of pressure values along with corresponding motor capacity (speed and
power) values for the compressor, measuring discharge pressure of the compressor,
comparing the discharge pressure value with the pre-set pressure value, running initially
the multi-capacity (speed and power) motor at a maximum speed with bypass valve closed,
to deliver the compressed medium, when the discharge pressure value is equal to pre-set
pressure value, and controlling the compressor capacity by relative regulation of
the bypass valve and the speed of multi-capacity (speed and power) motor, through
the main processing unit, to achieve the desired capacity of the compressor.
[0059] In another embodiment of the present invention, the method wherein the controlling
of the compressor capacity is performed by; measuring the discharge pressure, comparing
the discharged pressure with pre-set pressure value, running the motor at the motor
speed value corresponding to the pre-set pressure value, and controlling the bypass
valve to achieve the desired capacity of the compressor.
[0060] In yet another embodiment of the present invention, the method wherein the initial
motor speed value is varied to the corresponding pre-set pressure value whenever the
discharge pressure value is equal to pre-set pressure value.
[0061] Further embodiment of the present invention, the method wherein the opening of the
bypass valve is regulated when the discharge pressure value is not equal to pre-set
pressure value.
Advantages of the present invention
[0062]
- 1. Less noise generation as compared to systems with VFD.
- 2. No distortion in the supply grid as there will not be any kind of grid frequency
modulation as in case of VFD.
- 3. System costs are lower by about 25-30 % compared to costs of the system with VFD.
- 4. Very compact in size as all control systems can be mounted on the compressor &
motor body itself.
- 5. Overall operating efficiency of the compression system is far better by about 30
to 40 % as compared to that with compression system with VFD.
- 6. Control systems for bleeding port flow area opening control & motor active pole
control are simple and independent in operation.
- 7. Technology involved is not as complicated as VFD technology.
1. Ein System zur Durchführung einer Leistungssteuerung in einem Schneckenverdichter
mit:
(a) einem von einem Mehrfachleistungsmotor angetriebenen Schneckenverdichter mit einer
gleich bleibenden Leistung entsprechend der jeweils gewählten Drehzahl, zum Verdichten
eines gasförmigen Mediums, wobei der Verdichter eine Verdichtungszone zwischen einem
Ansaugrohr und einem Auslasskanal aufweist,
(b) einer zwischen dem Ansaugrohr und einem Bereich in der Verdichtungszone angeordneten
Bypass-Zone, in der ein etwas höherer Druck als am Ansaugrohr herrscht,
(c) einer Bypass-Leitung mit einem Bypass-Ventil, die zur Rückführung des gasförmigen
Mediums von der Bypass-Zone zu dem Ansaugrohr verläuft,
(d) einer Hauptprozesssteuerungseinheit,
(e) einer in einem verdichtetes Medium führenden Kanal des Verdichters angeordneten
Messeinrichtung zum Messen der Druckänderungen und/oder Temperaturschwankungen in
Form von Signalen,
(f) einem funktional mit der Hauptprozesseinheit und der Messeinrichtung verbundenen
Signalumwandler zum Empfangen von Signalen,
(g) einem funktional mit dem Bypass-Ventil verbundenen Bypass-Ventilregler,
(h) einem funktional mit dem Motor verbundenen Motorregler zur Durchführung von Mehrfachleistungsvorgängen,
wobei der Bypass-Ventilregler und der Motorregler funktional mit der Hauptprozesseinheit
verbunden ist,
(i) der Hauptprozesssteuerungseinheit, die derart angeordnet ist, dass das Bypass-Ventil
bei Empfang der Signale zur Steuerung der Verdichterleistung mittels des Bypass-Ventilreglers
schrittweise geöffnet wird, sowie
(j) der Hauptprozesseinheit, die weiterhin derart angeordnet ist, dass die Motordrehzahl
durch die Motorsteuerung bei Empfang der Signale zur Steuerung der Verdichterleistung
auf die nächste eingestellte Drehzahl umgeschaltet wird, indem das Bypass-Ventil geschlossen
wird, wenn die Verdichterleistung der Leistung in der nächsten eingestellten Motordrehzahl
entspricht.
2. System gemäß Anspruch 1, wobei die Messeinrichtung aus Druck- und Temperaturwandlern
besteht.
3. Verfahren zur Leistungssteuerung in einem Schneckenverdichter gemäß Anspruch 1, wobei
das Verfahren folgende Schritte umfasst:
(a) Einstellen einer Vielzahl von Druckwerten zusammen mit entsprechenden Motordrehzahlwerten
für den Verdichter,
(b) Messen des Förderdrucks des Verdichters,
(c) Vergleichen des Förderdruckwertes mit dem voreingestellten Druckwert,
(d) anfängliches Regeln des Mehrfachleistungsmotors bei maximaler Drehzahl mit dem
Bypass-Ventil in geschlossenem Zustand, um das verdichtete Medium zuzuführen, wenn
der Förderdruckwert dem voreingestellten Druckwert entspricht, und
(e) Steuern der Verdichterleistung durch relative Regulierung des Bypass-Ventils und
der Drehzahl des Motors mit mehreren Geschwindigkeiten über die Hauptprozesseinheit,
um die gewünschte Leistung des Verdichters zu erreichen.
4. Verfahren gemäß Anspruch 3, wobei die Steuerung der Verdichterleistung durchgeführt
wird durch
(a) Messen des Förderdrucks,
(b) Vergleichen des Förderdrucks mit dem voreingestellten Druckwert,
(c) Betreiben des Motors mit einem Motordrehzahlwert entsprechend dem voreingestellten
Druckwert und
(d) Steuern des Bypass-Ventils, um die gewünschte Leistung des Verdichters zu erreichen.
5. Verfahren gemäß Anspruch 4, wobei der Ausgangswert der Motordrehzahl auf den entsprechenden
voreingestellten Druckwert geändert wird, wenn der Förderdruckwert dem voreingestellten
Druckwert entspricht.
6. Verfahren gemäß Anspruch 4, wobei die Öffnung des Bypass-Ventils reguliert wird, wenn
der Förderdruckwert nicht dem voreingestellten Druckwert entspricht.