CN108138760A - For controlling the system of compressibility - Google Patents
For controlling the system of compressibility Download PDFInfo
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- CN108138760A CN108138760A CN201680051524.0A CN201680051524A CN108138760A CN 108138760 A CN108138760 A CN 108138760A CN 201680051524 A CN201680051524 A CN 201680051524A CN 108138760 A CN108138760 A CN 108138760A
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- 238000000034 method Methods 0.000 claims abstract description 30
- 239000012530 fluid Substances 0.000 claims abstract description 23
- 238000012545 processing Methods 0.000 claims abstract description 14
- 230000006835 compression Effects 0.000 claims abstract description 13
- 238000007906 compression Methods 0.000 claims abstract description 13
- 238000005259 measurement Methods 0.000 claims description 12
- 230000000694 effects Effects 0.000 claims description 7
- 241000208340 Araliaceae Species 0.000 claims 1
- 235000005035 Panax pseudoginseng ssp. pseudoginseng Nutrition 0.000 claims 1
- 235000003140 Panax quinquefolius Nutrition 0.000 claims 1
- 235000008434 ginseng Nutrition 0.000 claims 1
- 238000005086 pumping Methods 0.000 claims 1
- 230000008859 change Effects 0.000 description 25
- 238000007493 shaping process Methods 0.000 description 15
- 238000004891 communication Methods 0.000 description 8
- 238000007689 inspection Methods 0.000 description 8
- 230000008901 benefit Effects 0.000 description 5
- 230000009467 reduction Effects 0.000 description 5
- 238000004519 manufacturing process Methods 0.000 description 4
- 238000012986 modification Methods 0.000 description 4
- 230000004048 modification Effects 0.000 description 4
- 238000003860 storage Methods 0.000 description 3
- 238000012795 verification Methods 0.000 description 3
- 238000012544 monitoring process Methods 0.000 description 2
- 239000002699 waste material Substances 0.000 description 2
- 238000004458 analytical method Methods 0.000 description 1
- 238000013459 approach Methods 0.000 description 1
- 230000004888 barrier function Effects 0.000 description 1
- 230000005540 biological transmission Effects 0.000 description 1
- 238000004364 calculation method Methods 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 239000010725 compressor oil Substances 0.000 description 1
- 239000013256 coordination polymer Substances 0.000 description 1
- 238000013461 design Methods 0.000 description 1
- 238000001514 detection method Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000011156 evaluation Methods 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 238000007726 management method Methods 0.000 description 1
- 230000000737 periodic effect Effects 0.000 description 1
- 238000003825 pressing Methods 0.000 description 1
- 230000008569 process Effects 0.000 description 1
- 230000008672 reprogramming Effects 0.000 description 1
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- 238000012360 testing method Methods 0.000 description 1
- 238000012549 training Methods 0.000 description 1
- 238000012546 transfer Methods 0.000 description 1
Classifications
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F04—POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
- F04B—POSITIVE-DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS
- F04B41/00—Pumping installations or systems specially adapted for elastic fluids
- F04B41/06—Combinations of two or more pumps
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F04—POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
- F04B—POSITIVE-DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS
- F04B49/00—Control, e.g. of pump delivery, or pump pressure of, or safety measures for, machines, pumps, or pumping installations, not otherwise provided for, or of interest apart from, groups F04B1/00 - F04B47/00
- F04B49/06—Control using electricity
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F04—POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
- F04B—POSITIVE-DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS
- F04B49/00—Control, e.g. of pump delivery, or pump pressure of, or safety measures for, machines, pumps, or pumping installations, not otherwise provided for, or of interest apart from, groups F04B1/00 - F04B47/00
- F04B49/06—Control using electricity
- F04B49/065—Control using electricity and making use of computers
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F04—POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
- F04B—POSITIVE-DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS
- F04B49/00—Control, e.g. of pump delivery, or pump pressure of, or safety measures for, machines, pumps, or pumping installations, not otherwise provided for, or of interest apart from, groups F04B1/00 - F04B47/00
- F04B49/08—Regulating by delivery pressure
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F04—POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
- F04D—NON-POSITIVE-DISPLACEMENT PUMPS
- F04D25/00—Pumping installations or systems
- F04D25/16—Combinations of two or more pumps ; Producing two or more separate gas flows
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F04—POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
- F04D—NON-POSITIVE-DISPLACEMENT PUMPS
- F04D27/00—Control, e.g. regulation, of pumps, pumping installations or pumping systems specially adapted for elastic fluids
- F04D27/02—Surge control
Abstract
Method for the system for controlling compressibility and for controlling compressibility, the compressibility include：Compressor (C1 C7) and its controller (A1 A7), the compressor and its controller are used for compression fluid medium；Two stage treatment device, the medium that the two stage treatment device conveys for processing from compressor；And pipe-line system (17 19,23), the pipe-line system are used for fluid media (medium) conduction to consumption place (16,22), the control system includes control unit (3), which includes：Data processing system (34), the data processing system are used to control compressibility；User interface (35), the user interface include display associated there；And transmitting device, the transmitting device are used for the transmitting control data between control unit, controller and pressure sensor.Compressibility can have multiple adjusted values, these adjusted values determine the requirement of fluid medium, the variation in direction of fluid media (medium) and the rate of variation, wherein, compressor specific adjusted value is based on the parameter provided from user interface, wherein, adjusted value is converted into network delivery request or network pressure setting or the setting of compressor specified pressure, wherein, control system is suitable for network delivery request or network pressure setting or the setting of compressor specified pressure are converted into the specific control data of compressor via directly control data, pressure setting or the pressure data item of compressor.
Description
Technical field
Side the purpose of the present invention is being used to control the system of the compressibility of fluid media (medium) and for controlling compressibility
Method.
Background technology
In industrialized country, what industry was consumed about the 10% of electric energy spends in the production of compressed air.In addition,
Compressed air is the crucial factor of production, therefore appears in the economically meaning in many cases of the quality problems in compressed air
It is great.It has been found that the inefficient use of compressed air is the significant problem in many countries.
In the compressibility of compressed air network, compressed air is generated using compressor, the compressed air is via cold
But device and forbay are transmitted in the two stage treatment unit and second pressure case for being provided with filter and drier, compressed air from
Second pressure case is fed into consumption place.Compressor is controlled by means of controller, these controllers communicate total via data
Line is connected to the control computer for controlling the system.The other also such as pressure sensor of control computer is connected to, and
And the data obtained from these sensors are used for the control of system.
WO specifications 91/06762 disclose a kind of such compressor control device, which can
To be connected to computer.Via data communication bus, several compressors can be connected to computer.Single controller can be controlled
The operation mode of single compressor is made, the pattern is on-line/off-line, modulation operations and off-load operate.In WO specifications 91/
In 06762, each controller of compressor can individually be controlled by means of the signal obtained from computer.In addition, the equipment packet
The graphic alphanumeric display (such as light-emitting diode display) of such as controller parameter can be presented above by including, and the operator of equipment can be with
By pressing different switches the equipment is operated via user interface.
In order to save energy when producing compressed air, various methods have been developed.Wherein most typical solution
It is the standard controller for providing and having the control program of oneself by compressor Manufacturing business, the control program can not be customized to
It is suitble to the compressor of other manufacturers, and does not include the verification of control efficiency.In addition, it develops for several compressors
Type may customize and allow to connect the portions modular method of several pressure sensors.
Also there is the measuring method that may be used to determine and control realized energy-saving benefit.However, these measuring methods have
There is single operation property, and if purpose is to ensure that the execution of continuous high quality, these measuring methods must be repeated at periodic or other desired.
The price of customizable solution is higher due to required a large amount of programing works inter alia.In these cases, if
It is standby series to be produced with small lot to build, therefore they are costly.
Major part (up to 80%) maintenance visit associated with control system is attributable to the event caused by misuse
Barrier.This is because current control system is independent system, except in the case of fragmentary, they will not be tieed up after introduction
Shield.When replacing user, the training that they once received is no longer useful.The actual compression air system to be controlled through opening for many years
Hair, and control system is not necessarily suitble to situation about having changed.This leads to situations below：Over time, even if operation
Good control system also not necessarily reaches its purpose.
US Patent specification 4502842 disclose it is a kind of by multiple compressor sets into system, which can be pre-
Be set as example by a few thing in only compressor or by the power of reduction work it is this in a manner of act as in different situations
With.US Patent specification 4526513 proposes another system for controlling compressor assembly.
System well known in the prior art can not realize energy efficiency as best as possible, on the contrary the compressor warp in them
Often by the efficiency in compressor and/or whole system than being driven in bad range.
Invention content
The purpose of the present invention is realizing a kind of novel control system and a kind of novel control method, so that pneumatically
The operation of system and equivalent can become more effective on a large scale with rational cost and limited human resources.Following power
The details of the feature of the system of the present invention is given in profit requirement.
In a system in accordance with the invention, it controls and monitors and be connected to one or more compressed air networks or equivalent
One or more compressors and associated two stage treatment device.The system of the present invention is for controlling fluid media (medium)
The system of at least one compressibility.Compressibility includes：Compressor and its associated controller are situated between for compression fluid
Matter；Two stage treatment device, for handling the medium conveyed from compressor；And pipe-line system, for fluid media (medium) conduction to be arrived
Consume place.Control system includes control unit, which includes：Data processing system, the data processing system are used for
Control compressibility；User interface, the user interface include display associated there；And transmitting device, transmission dress
It puts for the transmitting control data between control unit, controller and pressure sensor.Spy can be selected in compressibility
Due to the control model of type of compressor, which determines adjusted value to be used.Adjusted value determines fluid medium
It is required that, the variation in direction of fluid media (medium) and the rate of variation.The parameter provided from user interface can act on the adjustment
Value.Control system is suitable for adjusted value being converted into based on shaping modes, compressor the transportation request selected for compressor
And control data.The control of compressor and the selection of shaping modes are carried out from the user interface of control system.
The system according to the present invention is specified in more detail in the characterizing part of claim 1.
By means of the system according to the present invention, variable conveying compression can be run in the range of good compression machine specific efficiency
Machine, so as to fulfill energy efficiency as best as possible.By means of the system according to the present invention, the range for running compressor can be by
It defines to particular compressor.In addition to this, measurement data can be used for controlling the transfer rate of compressor.
Description of the drawings
Hereinafter, the present invention is more fully described by means of some embodiments with reference to the accompanying drawings, in the accompanying drawings：
Fig. 1 presents compressibility according to the embodiment of the present invention；
Fig. 2 presents the operation of system according to the embodiment of the present invention；
Fig. 3 A to Fig. 3 D present the control model of compressor according to certain embodiments of the present invention as flow chart
With the operation of shaping modes；
Fig. 4 A to Fig. 4 C present the definition of network delivery request according to the embodiment of the present invention；
Fig. 5 presents the definition of compressor transportation request according to the embodiment of the present invention；
Fig. 6 presents showing for the control model of compressor according to the embodiment of the present invention and the operation of shaping modes
Example.
Specific embodiment
Hereinafter, 1 the present invention is more fully described by means of the example of embodiments of the present invention with reference to the accompanying drawings, it is attached
Fig. 1 presents the block diagram of pneumatic system according to the present invention, including control unit 3.
The pneumatic system according to the embodiment of the present invention presented in Fig. 1 includes two compressed air networks 1,2, this
Two compressed air networks, which are connected to, controls their control system.First network 1 includes：Six compressor C1-C6, this six
Compressor has their controller A1-A6；Forbay 11, the forbay are connected to three compressor C2-C4；At four two levels
Manage unit 12-15；Consume place 16；And the pipe-line system 17-19 for their interconnection.Second network 2 accordingly includes
The pipe of a compressor C7, two stage treatment unit 21 with its controller A7, consumption place 22 and the interconnection for them
Road system 23.
In addition, two networks are both provided with：Pressure sensor PI1-PI5, wherein, PI1 is connected to compressor C1 and two level
Pipeline 17 between processing unit 12, PI2 are connected to forbay 11, and PI3 is connected to compressor C5, C6 and two stage treatment unit
14th, the pipeline 19 between 15, PI3 and PI4 are connected to consumption place 16, and PI5 is connected to compressor C7 and two stage treatment list
Pipeline 23 and consumption place 22 between member 21；And pneumatic station control AS1-AS3, wherein, AS1 is connected to sensor
PI2, PI4, PI1 and two stage treatment unit 13, AS2 is connected to controller A5, A6 and sensor PI3, and AS3 is connected to biography
Sensor PI5.
Three serial communication bus that controller described above and sensor can be shared for example via two devices
30-32 is connected to the serial port 33 of control unit 3, and is also connected to the control including display and user interface 35 and calculates
Machine 34.Controller, sensor and the other components of system can also utilize a certain other wirelessly or non-wirelessly data communication bus
Or data communications method connects.UI Preferences has user interface program, and control computer is provided with a group control journey
Sequence and controller unit.
Via user interface 35, user can observe the operation of pneumatic system, configuration control and monitoring system, and export
The report related with system operation.Control program is given based on the information by means of data communication equipment and program acquisition and by user
The instruction gone out adjusts and controls pneumatic system via pneumatic station control and compressor controller.
Pneumatic station control AS1-AS3 reads the data specific to pneumatic station, such as pressure and alarm number from pneumatic system
According to.Compressor controller A1-A7 read with via data communication bus 30-32 by control program send compressor and control
Related data are ordered, and perform order, such as starts, stop and loads.
The quantity of compressor can be supplied to a group control program as parameter.Add or remove compressor when do not need to
Any mode changes control program.As long as this is because it is related to compressor, just so that each compressor C1-C7 is its classification
The mode of embodiment constructs the program according to modularized design, and the classification depends on given parameter to use or stop
With.
Each compressor C1-C7 can be configured to arbitrary type of compressor by means of parameter via user interface 35.Therefore, exist
For the first time during configuration control system or when changing independent type of compressor later, modification control system is not needed at all.This
It is due to the fact that：By means of parameter, the above embodiment of compressor classification can be configured as arbitrary basic compressor
Type.These are, for example, constant speed control, frequency converter drive control or turbo-compressor control.
Required amount of pressure sensor PI1-PI5 can be connected to control system, to read the conveying of each compressor
Pressure and desired network pressure.This makes it easier to control compressor and provides the general view of the state of pneumatic network.Pressure
Any one in force snesor may be configured to indicate the discharge pressure of any one in compressor, and pressure sensing
Any one in device may be configured to the control pressure as whole system.The addition or removal of pressure sensor are not related to
Control any variation of program.
Each pressure data item can also include and the volume that it belongs to is much and the rate of change of pressure is what is related
Information.Based on these data, the volume considered can be directed to and calculate air supply shear really.It is each by being directed to
Volume calculate the variation of air capacity and by the information with and the related data of state of all compressors combine, acquisition compressed air
Live actual consumption.This method significantly improves accuracy and the respond of control.
Equally, other measurements or controllable device may be coupled to control system.These for example can be dew point, heat consumption rate or
The measurement of flow velocity, the control of valve, drier, fan, air deflector or pump.It is additional measure and the attribute of attachment device with parameter come
Definition.Addition or the additional measurement of removal and attachment device are not related to any variation of application software.
Control system can control and monitor multiple individual pneumatic systems 1,2.This allows to be alternatively coupled to system
Pressure sensor PI1-PI5 in any one as each compressor C1-C7 control pressure sensor, in addition, pressure
Any one in contracting machine can be controlled via UI Preferences into according to pressure sensor value, the pressure sensor value
It sets to select according to individual pressure.
Therefore, it can utilize and be used to control the system of compressibility according to the present invention to control the operation of compressor.
In compressibility according to the present invention, control can be selected from user interface and adjust the pattern of compressor particular delivery.It is based on
The selection carried out from user interface, the control of the conveying of compressor can be joined based on the conveying calculated according to network delivery request
Examine value or as what is presented in figure 3 a is directly based upon network pressure setting or the setting of compressor specified pressure.
Particular compressor selection is directed to from user interface for adjusting the pattern of compressor.How the adjusting of compressor operates
Depending on being directed to which control model compressor selects.The Adjust and use of compressor directly adjusts (for example, by changing rotating speed)
Or by changing pressure setting or being realized by changing the discharge pressure reading of compressor.
Identical with the figure in Fig. 3 B if transportation request is selected as the control model of compressor, network delivery please
Seeking Truth adjusted value, the adjusted value determine the direction of api request (or being more briefly directed to the requirement of fluid media (medium)), fluid media (medium)
Variation and variation rate.Network delivery request according to embodiment of the present invention is described in Fig. 4 A to Fig. 4 C
(0-100%'s) determines.As Fig. 3 B are presented, from user interface selection for the shaping modes of compressor.If directly join
It examines (such as speed) and is selected as the method for adjusting compressor, then the transportation request of compressor is zoomed to the lattice needed for compressor
Formula.If pressure setting is selected as shaping modes, network delivery request is converted into compressor transportation request, and into one
Step is converted into the pressure for taking into account the limitation provided from user interface and sets.In this case, tune can be checked first
Whole rate, can according to the value of the discharge pressure sensor of the size of compressor transportation request, its derivative and compressor and
Derivative calculations go out new pressure setting.It, can be by two level in addition, if the pressure sensor of compressor oneself is on network side
Pressure difference on processing unit is taken into account.If pressure data item is selected as shaping modes, rate inspection can be performed first
It looks into, and the value identical with the pressure setting of compressor can be supplied to compressor for pressure transmitter signal.According to defeated
Request is sent, if necessary to smaller conveying, then the value that can will be greater than above-mentioned value is set as described value, and if necessary to bigger
Conveying, then smaller value can be set.Compressor according to one embodiment is presented in Fig. 5 and Fig. 6 in more detail
Transportation request determines.
If compressor control pattern is network pressure setting, identical with the figure of Fig. 3 C, network pressure setting is adjustment
Value, by comparing the reading of the adjusted value and control pressure sensor determine the requirement of fluid medium, fluid media (medium) side
To variation and variation rate.Compressor shaping modes are selected from user interface, the shaping modes are currently considered
In the case of can be directly reference, pressure setting or pressure data item.Network pressure setting can be for example converted into will be due to pressure
The compressor pressure setting value that the pressure loss caused by the two stage treatment of contracting air is taken into account.If directly with reference in network
Pressure is used as compressor shaping modes in the case of setting, then can perform the inspection of adjustment rate, can calculate network pressure
How many force data item sets different from network pressure, and can be based on the information and change directly reference.Utilize slow adjustment
Rate, variation is distributed to the desired period, and directly reference is also updated between the inspection of adjustment.If pressure is set
The pattern for being used as adjusting compressor is put, then can perform the inspection of adjustment rate, and network pressure setting can be provided
To compressor.If the sensor of compressor oneself not on network side, can be repaiied by the pressure difference on two stage treatment unit
Positive setting.If pressure data item is used as adjusting the pattern of compressor, the inspection of adjustment rate can be performed, and can be with
Calculate how many network pressure data item sets different from network pressure.Pressure transmitter to be used as can be corrected if necessary
Signal is supplied to the pressure data item of compressor.
If compressor control pattern is the setting of compressor specified pressure, identical with the figure of Fig. 3 D, compressor is specific
Pressure setting is adjusted value, and fluid media (medium) requirement, stream are determined by comparing the reading of the adjusted value and control pressure sensor
The variation in the direction of body medium and the rate of variation.Compressor shaping modes are selected from user interface, which is working as
It is preceding consider in the case of can be directly reference, pressure setting or pressure data item.If it is set in compressor specified pressure
In the case of, directly with reference to shaping modes are used as, then the inspection of adjustment rate can be performed, compressor pressure can be calculated
How many data item sets different from compressor specified pressure, and can be based on the information and change directly reference.Using slow
Rate is adjusted, variation is distributed to the desired period, and directly reference is also updated between the inspection of adjustment.If pressure
Power setting is used as adjusting the pattern of compressor, then compressor specified pressure setting is provided to compressor.If pressure data
Item is used as adjusting the pattern of compressor, then can perform the inspection of adjustment rate, and can calculate compressor pressure number
From compressor specified pressure how many sets different according to item.Pressure transmitter signal to be used as can be corrected if necessary to be supplied to
The pressure data item of compressor.
Fig. 4 B describe network delivery request determine how progress.If network pressure is close to setting (that is, closer
In the limiting value of setting), then check the rate of change of network pressure.It is defeated by quickly changing network if rate of change is big
Request is sent to slow down variation, and if rate of change is small, slowly changes network delivery request.The mean change of network pressure
It can be used for evaluating the rate of change of network pressure, and can be used as the setting of rate of change when checking rate of change
Parameter, the setting are intended for network pressure close to the situation of setting (that is, in limiting value closer to setting).If net
Network pressure then checks net further from setting (that is, outside limiting value closer to setting but in the limiting value further from setting)
The rate of change of network pressure.If rate of change is big, slow down variation, and if become by quickly changing network delivery request
It is small to change rate, then slowly changes network delivery request.The mean change of network pressure can be used for evaluating the variation of network pressure
Rate, and can be used as parameter when checking rate of change for the setting of rate of change, the setting is intended for network
Pressure is arranged distant from the situation of (that is, outside limiting value closer to setting but in the limiting value further from setting).If net
Network pressure is arranged distant from (that is, outside limiting value further from setting), then quickly changes network delivery request.Rate of change is set
It can be used as parameter when checking rate of change, the setting is intended for network pressure and is arranged distant from (that is, further from setting
Limiting value outside) situation.
Fig. 4 C describe how the determining of network delivery request can further be in progress.It, can after the above process is performed
To check for the variation of the quantity of the compressor needed for conveying air.If the quantity of required compressor changes, can
With the compressor capacity by changing network delivery request compensation increase/reduction.If quantity does not change, other steps are not needed to
Suddenly.The quantity and its conveying (quantity known to system and the conveying) for conveying the compressor of air can be used for needed for evaluation
The quantity of compressor.
The figure of Fig. 5 presents determining for the compressor transportation request in the case of an embodiment of the invention.It is first
First, the transportation request of determining compressor is asked according to network delivery.The limit of compressor adjustable range can for example influence this really
It is fixed.After this, it checks the efficiency ratio of compressor, and changes the transportation request of compressor, so as to from the efficiency of compressor ratio
Angle for as far as possible effectively.When evaluating compressor efficiency ratio, the efficiency ratio of currently considered compressor can be used
Such as the efficiency curve of the compressor.
Fig. 6 presents example according to the embodiment of the present invention, wherein, compressor control pattern is transportation request, and
And compressor shaping modes are pressure settings.Set-point can be selected, and can select via the user interface of control system
Transportation request, network pressure setting or the setting of compressor specified pressure are selected, as the control model for compressor.In these
Rong Zhong, for the example selection transportation request.Reference, pressure setting or discharge pressure reading can be selected to directly transport as use
In the shaping modes of compressor.In this example, pressure setting is selected for use in adjusting the pattern of compressor.
In the embodiment of fig. 6, it is first determined network delivery asks (0-100%).The variation in the direction of network pressure
The calculating can be all influenced with rate of change, with the difference of set pressure and the rate of change selected from user interface.After this,
Determine the transportation request (0-100%) for compressor.It will be adjusted simultaneously via user interface when determining compressor transportation request
Adjustable range available for compressor is taken into account.Finally, the pressure setting for compressor is determined, and here, such as can
By by compressor always by efficiency as best as possible than use it is this in a manner of the efficiency curve of compressor taken into account.
In the pressure setting for determining compressor, by the variation size of the adjustable range of compressor, transportation request value and described value and
The value of the discharge pressure sensor of compressor is taken into account, and if in addition, the discharge pressure sensor of compressor oneself not
On network side, then the pressure difference on two stage treatment unit is taken into account.
User can by select compressor control model and shaping modes and using selected adjusted value parameter come
Optimize the operation of entire pneumatic system.Control system is suitable for control and the feed adjustment of all known type of compressor.In basis
In the system of the present invention, to that can control and adjust together how many variable conveying compressors, there is no limit.This makes it possible to reality
Now energy-saving benefit as best as possible.
In controller known in the art, the adjustable range of compressor remains fixed.However, in fact, compressor
Adjustable range there is different sizes, and therefore without using the entire tune of the compressor in solution known in the art
Adjusting range cannot select desired machine to come always with best efficiency than operation.This leads to the unnecessary consumption of energy.
In the inventive solution, network adjusted value is being converted into the transportation request for variable conveying compressor
When, direction and its variable quantity of network api request can be calculated.The variation is distributed to each variable conveying compressor.Herein
Later, about whether can for example by means of the efficiency curve of compressor along more energy efficient adjustment in direction require examined
It looks into.
If one or more conveyings with bigger in compressor are in more preferably efficiency ratio and compressor
Some have more preferably efficiency ratio with smaller conveying, then can take into account the effect of efficiency curve.If some are compressed
Machine has more preferably efficiency ratio with smaller conveying, and even if the efficiency ratio of all machines will be conveyed more preferably with smaller,
Capacity is also significantly greater than other compressors, then can also take into account the effect of efficiency curve.If a certain compressor is with more
Big conveying has a more preferably efficiency ratio, and even if all machines efficiency than by with the conveying of bigger more preferably, capacity
Noticeably greater than other compressors can also then take into account the effect of efficiency curve.
In a solution in accordance with the invention, with off-load and compressor can be stopped.In this case, it calculates variable
The capacity that is wasted of compressor is conveyed, and if it is necessary, closing small compressor so that variable conveying compressor is with the defeated of bigger
Send operation.
Controller known in the art can have for the off-load limit of compressor and the loading limit.In normal condition
Under, in solutions known in the art, multiple variable conveying compressors are run with minimum conveying, in such case
Under, pressure is very slowly promoted or is not promoted.Next compressor off-load only when reaching the off-load limit.This existing
In technical solution, with poor efficiency than variable conveying compressor is driven to reach long time section.
In solution according to embodiment of the present invention, next the compressor of off-load is wanted in identification successively.
In addition to this, the capacity that is wasted of variable conveying compressor is calculated.Do not include to obtain the compressor of off-load in this computation
Capacity.According to the factor of safety that the deduction of the capacity of waste is provided from user interface or calculated automatically, thus to obtain being calculated
The capacity that is wasted.The capacity deduction that is wasted according to being calculated will obtain the compressor of off-load at the time of current consideration
Conveying.If the result calculated is just, off-load compressor.
The advantages of solution is significantly to perform the off-load of next compressor earlier, and with it is known in the art
Solution compare the driving for reducing variable conveying compressor in inefficient range.Nargin safe to use can be to avoid
The continuous loading of machine and off-load.If consumption fluctuation, lag can be used, this reduces " unnecessary " on/off switch.
Fig. 2 presents the example of the compressor off-load situation of the operation of system according to the embodiment of the present invention.
The region marked in Fig. 2 is defined as：
The compressor that 1=is currently running
The compressor that 2=has stopped
Next 3=wants the compressor of off-load
The variable conveying compressor that 4=is currently running
In the embodiment presented in Fig. 2, next identification wants the compressor of off-load (that is, in this case successively
For compressor 2, because it has lowest priority (=4)).Next the conveying for wanting the compressor of off-load is 50%* at this moment
80m3/min=40m3/min.
After this, the capacity that is wasted of variable conveying compressor (region 4) being currently running is calculated：(100%-
75%) * 100m3/min+ (100%-75%) * 80m3/min=45m3/min.
Factor of safety is inferred according to the capacity being wasted, thus to obtain the capacity that is wasted calculated.If for example, safety
The factor is 4m3/min, then the capacity that is wasted calculated is 45m3/min -4m3/min=41m3/min.
The conveying of the compressor of off-load is wanted in the capacity deduction that is wasted according to being calculated, and if final result is just,
Then off-load compressor.As a result, for example, if factor of safety is 4m3/min, the final result realized is：45m3/min–
4m3/min -40m3/min=1m3/min.In other words, in the case of the factor of safety currently considered, off-load compressor.By
This, if for example, factor of safety is 6m3/min, the final result realized is：45m3/min–6m3/min–40m3/min
=-1m3/min.In the case of the factor of safety, not off-load compressor.
The compressor for wanting off-load may be fixed conveying or some other type of compressor.It can be transported with sub-load
Capable all compressors (for example, frequency converter driving or turbo-compressor, more reciprocating piston compressors etc.) are considered as
Variable conveying compressor.
It in a solution in accordance with the invention, can be from the adjustable range of the variable conveying compressor of UI Preferences.
In this way, can be with best efficiency than operation compressor, and can discharge to avoid turbo-compressor.
The off-load and the loading limit of pressure are configured in some central controllers known in the art.It is also possible to
It is that there is central controller pressure to set and load the limit or setting and the off-load limit.If controller can also drive variable
Compressor is conveyed, then system also often has and set for the pressure of compressor.However, in combination known in the art,
How variable conveying compressor and off-load-loading compressor will not be set as running together and taken into account.Problem especially occurs
In the situation：Base load is run, and deposit at the following time together with variable conveying compressor：If the appearance of compressor
Amount midway is terminated, then off-load-loading compressor enters use, is conveyed with support pressure.In this case, it is general happens is that
Variable conveying compressor there are during enough capacity it is high or in running under pressure level.At the end of capacity, allow pressure
It reduces, and when pressure reduces enough, starts and support compressor.
It in the inventive solution, can be by so that in a manner of the very close loading limit of the setting limit of loading machine
For central controller setting off-load, the limit and the loading setting limit are set.Off-load is set between the limit and the loading setting limit
Range can also automatically be calculated by studying pressure and fluctuation range by single variable conveying driven compressor.The solution party
One advantage of case is in variable conveying compressor isolated operation, and pressure stage is lower, and can save energy.
In solutions known in the art, usually there are three set for tool in the central controller for compressor：Off-load
Pressure, on-load pressure and setting pressure.In some compressors, with it is minimum may feed drive they when, start to dump
Excess air.Significantly more work(when dumping excess air waste than being opened with minimum delivery operation and no outlet valve
Rate.In some compressed air networks significantly fluctuated in consumption, there are very more, feelings of the operation in the minimum delivery limit
Condition.
In a solution in accordance with the invention, positive normal pressure can be allowed more than (for example, in these types of cases)
Power is set.In this case, for example, allowing turbo-compressor than being run under setting the higher pressure specified by pressure.
In this case, turbine does not dump, and opposite drain valve remains turned-off.This realizes more preferably energy efficiency.
In a solution in accordance with the invention, off-load-loading compressor can be directed to and compressed for variable conveying
Machine adds the different off-load limit.The limit of variable conveying compressor can be set to the pole higher than off-load-loading compressor
Limit.Therefore, in this case, pressure is allowed slightly to be promoted in a network before compressor is allowed to dump.The limit for example may be used
To be set via user interface.By using above-mentioned solution, reduction compressor dumps under minimum delivery, so as to reduce
To the needs of power attenuation.
For compressor transportation request to control data further conversion (that is, the conveying of variable conveying compressor
Adjustment) it in the inventive solution can be in many ways (for example, using derived from resolution ratio per minute, conveying percentage
Than or pump blades posture direct reference) carry out.The adjustment of the conveying of variable conveying compressor can utilize pressure to set
Change, be automatic or by simulation being set to carry out together with pressure network pressure data item.These methods are suitable for institute
Have type of compressor, without tube model and make how.
In the system of the present invention, can be directed to compressor calculate adjusted value, the value specify can be supplied to compressor,
The expectation conveying of compressor or pressure stage and the sensor for it is expected driven compressor.By means of this point, rotating speed or IVG are calculated
Put alternative one, pressure setting or institute's analog network pressure data item alternative one, the value as compressor to be supplied to.Herein
Later, compressor horsepower or cell pressure are measured.Based on the measurement data, so that the mode for reaching set-point is corrected and to be carried
Supply the value of compressor.In this way, the compressor controlled with different control models can be controlled together with unified approach.Equally, may be used
Easily to parameterize compressor from user interface.
By means of the system of the present invention, can be controlled with same controller has multiple and different compressed air networks or air
Multiple and different factories of network.In this case, the controller of system of the invention can have for very more points
Set-point, user interface and control logic.Can retain centered on can handle data and can be according to institute fast enough
State the computer that data form control.System can also by it is following it is this in a manner of be configured：So that the interruption in computer network
The generation of compressed air is not prevented.In this way, the platform for the server of enterprise group may be coupled to control device, and not
Need individual system.This generates the saving of cost, and newer management is easier to by group.Equally, work can then be carried out
Factory is specific or the specific comparison of pneumatic network.
In an embodiment of the system of the present invention, a compressed air network can be controlled in multiple portions
System.In this case, a compressed air network is divided into multiple " virtual networks " in its control aspect.Compressed air network
These parts controlled as individual entity.In such a case, it is possible to the pressure drop by the faster part of network
It is low to take into account, and can be made a response in a manner of most preferably possibility to the pressure reduction.
If any one in selected compressor cannot operate, the system of the present invention can have emergent sequence.
In this case, as the larger compressor of base load operation compressor it is a certain it is unforeseen due to and stop or
It is placed in when not conveying air in the list for the selection for generating emergent sequence.Larger replacement compressor is arranged in emergent sequence
In so that they enter earlier uses.When the system that detects returns to normal condition, emergent sequence can be interrupted automatically
It uses.Operator can since user interface and interrupt emergent sequence use or can be automatic.
By means of the emergent sequence of the system according to the present invention, usually compressed not as the compressor of base load operation
The compressor as base load operation is also used as in the case of machine failure, to replace usually as base load operation
It is out of order or the compressor of stall.In this case, it is out of order in larger compressor and real in operation after the failure
Now pressure evenly.In this case it is also possible to minimum operating pressure is calculated, and continuous section in the normal operation period
Save energy.
In an embodiment of the invention, according to the setting provided in the user interface or by straight from user interface
Selecting is selected, and compressor can be run in a manner of timing and have become hotter.After this, compressor is back to normal automatic drive
It is dynamic.Special operating status can be constructed in the central controller (in addition to normal condition, also for the purpose of hotter operation
Part, automatic, manual mode).Each compressor can be for example individually switched with timing mode or via user interface to current institute
The state of consideration.Compressor is moved in terms of priority before other compressors, becomes the compressor for being very easy to driving.
Compressor can be according to the compressor oil temperature (or other measurements) run through all phases/states or with timing mode from current
The state considered be back to it is automatic or it is a certain it is other before state.Finally, compressor is no longer on priority list at it
Stop during top and close.
Using above-mentioned solution, automatically hotter in a controlled manner it can be run and may insure to compress in stand-by compressor
The clear and definite hotter operation of machine and can realize for being appropriately carried out required all phases/states when reduces manual work.It is however, standby
The period of unnecessary length is not used in compressor.
In an embodiment of the invention, there may be particular point in network, and system can be by the particular point
It takes into account.Therefore, if there are a certain vital points in network, the pressure in the place can be monitored, and can be in system
It is middle that place is set as particular point.If pressure reduction, the setting for delivery end can be improved.Therefore, for major part
Time, the pressure of delivery end can be relatively low, and when higher is needed to convey end pressure, which can be promoted to expectation etc.
Grade.In this way, generate unnecessary high pressure without compressor.It is also possible to detection more quickly and the pressure stage of particular point have
The spike effect of the consumption of pass, and when consumption spike is not present in network, network pressure can be kept relatively low.
In this embodiment, additional sensors can be added to consumption place and/or can be used and can be used in a network
Measurement.There may also be the settings of the expectation minimum pressure for particular point.Furthermore it is also possible to exist for how many network pressures
Power can be declined according to the parameter of particular point and controller or raised setting.Setting can be selected by operator.It can be with
Compressor is controlled according to given setting and promotes network pressure grade.
In an embodiment of the invention, lower pressure network support higher pressure can be passed through in the case that desired
Power network.In this embodiment, system can identify the pressure drop in elevated pressures network.Can also for Another reason and
Start the support of the second network.In solution preferably, the second sequence is selected in lower pressure network, at this
In sequence, the pressure stage higher of lower pressure network.After this, verification pressure is promoted in lower pressure network becomes high
In the pressure of elevated pressures network.After this, valve is opened, to support elevated pressures network.It can be held when based on measurement verification
During row, normal sequence can be back to.The return can also be realized from user interface.
In a system in accordance with the invention, each compressor can be directed to and set for pneumatic system minimum and maximum
Pressure limit.When more than these values, the control of compressor is switched to the control system of themselves.Start and loading is compressed
The sequence of machine is determined by sequence of operation table.
Compressor can be arranged to multiple sequence of operation table work as needed.This is possible, because each
Independent operation sequence is the embodiment of its classification, can be made by the program parameter of the quantity of the determining embodiment of change
With or deactivate.Therefore, reprogramming is not needed at all when adding or removing the sequence of operation.
By way of selecting to change the sequence of operation changing a control parameter.The sequence of operation can for example be based on week
It goes through, the stopping of compressor or automatic setting change.The automatic required unloaded work(changed based on possible all compressor combinations
The Continuous plus of rate, the Continuous plus and the unrestricted choice group that the observation of effective required compressor and observation to be kept to be spaced
It closes ground and generates automatically selecting for the possible most effective sequence of operation.
It in an embodiment of the invention, then can be by limiting compressor if there is enough compressors
Start to rotate compressor.For example, when being related to large-scale motor, startup can for example be limited to 2 times per hour.If it is required that it is
Three 10 minute periods per hour, then preceding 2 periods are by a compressor operating, and the last one period is by another compression
Machine is run.This can reduce excessive zero load.Rule can be that compressor is specific, and they can for example utilize center control
Device is set.
The method for starting and stopping compressor being selected via user interface.These methods be using continuous signal or
The startup and stopping that pulse carries out, and the startup based on allowed quantity and operate stopping or stopping.
Startup, loading and the off-load delay of each compressor can be individually adjusted.This allows method under any circumstance
Correct operation, but regardless of pneumatic system oneself dynamics how.
Compressor controller reads information from compressor, and will send information to control program, from a group control program read (CP read)
Take control command, and while the condition for also monitoring the validity of order and data communication bus and program according to it from
Oneself control program execution command.In existing solution, even to be incorporated in the single non-standard pressure under control system
Contracting machine model is also required to carry out relatively wide modification to control program.This problem is only limitted to simple compression machine controller now
The modification of program.When the solution is successful, even this modification can be also reduced, because this will be easy to
Form the library of compressor controller program.
Control program can continuously calculate total output and the power input of pneumatic system.These data can be stored in greatly
On capacity storage medium.In the user interface, these data can be present in same figure so that can at every moment be schemed
Shape form watches these data.In addition, mean consumption and power during the period selected by user interface calculating.Moreover, figure
Point can be Printed to File with desired time interval.Resulting report allows to verify the practical effect generated by control system
Benefit even can continuously measure execution with long duration.
Information received via data communication equipment by control program, related with compressor state and pressure value is continuously deposited
Storage is in the large-capacity storage media in may be at control computer.The mode of operation and pressure stage of compressor can be presented on
In same figure so that at every moment can graphically watch them.This makes it possible to real-time or its post analysis pneumatic system
Operation.
The basic framework of method allows the device of arbitrary manufacturer in compressor controller.This allows to this
Invention is in impossible many situations before it.
When (for example, connecting fault) is interfered to appear in the arbitrary portion of system, compressor controller, which will control, to be switched
To the control system of compressor oneself.The noiseless production of compressed air in the case of this guarantee is nearly all.
By means of group controller or it can will run any device test compression that controller is write with loading command
The operation of machine controller.This is realized by the structure of director demon, in this configuration, no matter type of compressor and model
How, external interface can be made to keep as simple as possible and standard.It only runs/ceases and desist order and lead to required load factor
Cross interface write-in.
It is apparent to those skilled in the art that the present invention different embodiments be not limited solely to it is described above
Example, but them can be changed in the range of claims presented below.
Claims (24)
1. a kind of system for controlling compressibility, the compressibility includes：Compressor (C1-C7) and its controller (A1-
A7), the compressor (C1-C7) and its controller (A1-A7) are for compression fluid medium；Two stage treatment device, the two level
The medium that processing unit conveys for processing from the compressor；And pipe-line system (17-19,23), the pipeline system
(17-19,23) are united for by fluid media (medium) conduction to consumption place (16,22), the control system to include control unit
(3), described control unit (3) includes：Data processing system (34), the data processing system (34) is for controlling the compression
System；User interface (35), the user interface (35) include display associated there；And transmitting device, the biography
Defeated device is used for the transmitting control data between described control unit, the controller and pressure sensor,
It is characterized in that,
The compressibility has at least one adjusted value, and at least one adjusted value determines the requirement of fluid medium, institute
The variation in the direction of fluid media (medium) and the rate of variation are stated,
Wherein, compressor specific adjusted value is based on the parameter provided from the user interface,
Wherein, the control system is suitable for adjusted value being converted into network delivery request or network pressure setting or compressor is specific
Pressure is set, and
Wherein, the control system is suitable for inciting somebody to action via directly control data, pressure setting or the pressure data item of the compressor
The network delivery request or network pressure setting or compressor specified pressure setting are converted into the specific control of compressor
System request.
2. control system according to claim 1, which is characterized in that compressor has the limitation to adjustable range, described
Limitation is suitable for determining from user interface.
3. control system according to claim 1 or 2, which is characterized in that the control system is suitable for based on compressor
Allow adjustable range and/or will be converted into based on the efficiency curve of compressor for the adjusted value of the network to variable defeated
Send the transportation request of compressor.
4. control system according to claim 3, which is characterized in that if in the compressor it is one or more with
Substantially larger conveying have some in better efficiency ratio and the compressor with substantially it is smaller convey with
Better efficiency ratio, then the control system be suitable for taking into account the effect of the efficiency curve.
5. control system according to any one of the preceding claims, which is characterized in that the control system is suitable for utilizing
Derived from the direct reference of rotating speed, the reference derived from conveying percentage or the posture derived from pump blades reference by transportation request into
One step is converted into the control data to the compressor.
6. control system according to any one of the preceding claims, which is characterized in that the control system is suitable for being directed to
Compressor, which calculates, it is expected that adjusted value the compressor convey or suitable for providing the pressure for it is expected compressor operating
Grade and sensor,
The control system is further adapted for calculating the rotating speed or the pumping for being sent to the compressor as control data
The posture, pressure setting or the analog network pressure data item of phyllidium piece.
7. control system according to any one of the preceding claims, which is characterized in that the control system is further adapted for surveying
The power of capacity compressor or the pressure of sensor, and based on the measurement data so that reaching the mode of set-point to correct
It is supplied to the value of the compressor.
8. control system according to any one of the preceding claims, which is characterized in that the control system has off-load
The limit and the loading limit, and the limit is suitable for based on the pressure and fluctuation model by single variable conveying driven compressor
It encloses to set.
9. control system according to any one of the preceding claims, which is characterized in that the system is directed to off-load-loading
Compressor and variable conveying compression machine have the different off-load limit.
10. control system according to any one of the preceding claims, which is characterized in that variable to convey the described of compressor
The off-load limit is suitable for the off-load limit higher than off-load-loading compressor.
11. control system according to any one of the preceding claims, which is characterized in that the control system is suitable for：
The unused capacity of variable conveying compressor is calculated,
Further calculate according to sequence want off-load next compressor it is currently considered at the time of the conveying,
The conveying of next compressor of off-load is wanted from unused capacity deduction,
The safety margin for providing from user interface or calculating automatically from unused capacity deduction,
And if the result calculated is just, compressor described in off-load.
12. control system according to any one of the preceding claims, which is characterized in that the compressibility includes being located at
It consumes the sensor in place or the compressibility is suitable for using available measurement in the network,
The system also includes the setting of the expectation minimum pressure for particular point and for the network pressure according to
Particular point can down or up how many setting,
Wherein, the system is suitable for the grade for controlling the compressor and the network pressure being adjusted according to given setting.
13. a kind of method for controlling compressibility, the compressibility includes：Compressor (C1-C7) and its controller
(A1-A7), the compressor (C1-C7) and its controller (A1-A7) are for compression fluid medium；Two stage treatment device, it is described
The medium that two stage treatment device conveys for processing from the compressor；And pipe-line system (17-19,23), the pipe
Road system (17-19,23) is for by fluid media (medium) conduction to consumption place (16,22), the control system to include control
Unit (3), described control unit (3) include：Data processing system (34), the data processing system (34) are described for controlling
Compressibility；User interface (35), the user interface (35) include display associated there；And transmitting device, institute
It states transmitting device and is used for the transmitting control data between described control unit, the controller and pressure sensor,
It is characterized in that,
The compressibility has at least one adjusted value, and at least one adjusted value determines the requirement of fluid medium, institute
The variation in the direction of fluid media (medium) and the rate of variation are stated,
Wherein, compressor specific adjusted value is based on the parameter provided from the user interface,
Wherein, adjusted value is converted into network delivery request or network pressure setting or the setting of compressor specified pressure, and
Wherein, the network delivery request or network pressure setting or compressor specified pressure setting are via the pressure
Directly control data, pressure setting or the pressure data item of contracting machine are converted into the specific control data of compressor.
14. according to the method for claim 13, which is characterized in that compressor has the limitation to adjustable range, the limit
System is determined from user interface.
15. the method according to claim 13 or 14, which is characterized in that be based on compressor for the adjusted value of the network
Permission adjustable range and/or efficiency curve based on compressor be converted into transportation request to variable conveying compressor.
16. according to the method for claim 15, which is characterized in that if one or more with this in the compressor
Larger conveying is conveyed with substantially smaller with more with some in better efficiency ratio and the compressor in matter
Good efficiency ratio, then take into account the effect of the efficiency curve.
17. the method according to any one of claim 13 to 16, which is characterized in that utilize the direct ginseng derived from rotating speed
It examines, derived from the reference of conveying percentage or the reference of posture derived from pump blades, transportation request is further converted into institute
State the control data of compressor.
18. the method according to any one of claim 13 to 17, which is characterized in that calculated for compressor described in it is expected
What adjusted value compressor convey or provide the pressure stage and sensor for it is expected the compressor operating,
It further calculates to be sent to the compressor as described in the rotating speed of control data or the pump blades
Posture, pressure setting or analog network pressure data item.
19. the method according to any one of claim 13 to 18, which is characterized in that measure compressor horsepower or sensor
Pressure, and based on the measurement data so that reaching the mode of set-point to correct the value that be supplied to the compressor.
20. the method according to any one of claim 13 to 19, which is characterized in that the control system has off-load pole
Limit and the loading limit, and the limit by the pressure and fluctuation range of single variable conveying driven compressor based on being set
It puts.
21. the method according to any one of claim 13 to 20, which is characterized in that the system is directed to off-load-loading
Compressor and variable conveying compression machine have the different off-load limit.
22. the method according to any one of claim 13 to 21, which is characterized in that variable the described of conveying compressor subtracts
Carry the off-load limit that the limit is higher than off-load-loading compressor.
23. the method according to any one of claim 13 to 22, which is characterized in that in the method：
Calculate the unused capacity of variable conveying compressor；
Further calculate according to sequence want off-load next compressor it is currently considered at the time of the conveying；
The conveying of next compressor of off-load is wanted from unused capacity deduction；
The safety margin for providing from user interface or calculating automatically from unused capacity deduction；
And if the result calculated is just, compressor described in off-load.
24. the method according to any one of claim 13 to 23, which is characterized in that the compressibility, which includes being located at, to disappear
The sensor or the compressibility for consuming place use available measurement in the network,
The system also includes the setting of the expectation minimum pressure for particular point and for the network pressure according to
Particular point can down or up how many setting,
Wherein, the system controls the compressor and the grade of the network pressure is adjusted according to given setting.
Applications Claiming Priority (3)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| FI20155586 | 2015-08-14 | ||
| FI20155586 | 2015-08-14 | ||
| PCT/FI2016/050484 WO2017029427A1 (en) | 2015-08-14 | 2016-06-30 | System for the control of a compression system |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN108138760A true CN108138760A (en) | 2018-06-08 |
| CN108138760B CN108138760B (en) | 2020-09-25 |
Family
ID=58050723
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201680051524.0A Active CN108138760B (en) | 2015-08-14 | 2016-06-30 | Control system and method for controlling a compression system |
Country Status (5)
| Country | Link |
|---|---|
| EP (1) | EP3334934B1 (en) |
| CN (1) | CN108138760B (en) |
| ES (1) | ES2900024T3 (en) |
| PL (1) | PL3334934T3 (en) |
| WO (1) | WO2017029427A1 (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112639644A (en) * | 2018-09-03 | 2021-04-09 | 恩尔赛思有限公司 | Method for analyzing the energy (specific energy consumption) for producing a unit mass or volume of compressed gas |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE102019104760A1 (en) * | 2019-02-25 | 2020-08-27 | Knorr-Bremse Systeme für Schienenfahrzeuge GmbH | Air supply system and method for controlling and / or monitoring an air supply system |
Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4526513A (en) * | 1980-07-18 | 1985-07-02 | Acco Industries Inc. | Method and apparatus for control of pipeline compressors |
| US6419454B1 (en) * | 2000-06-14 | 2002-07-16 | Leo P. Christiansen | Air compressor control sequencer |
| US20030065423A1 (en) * | 2001-09-14 | 2003-04-03 | David Vanderbeek | Compressed gas system |
| US20040151593A1 (en) * | 2001-02-02 | 2004-08-05 | Vesa Saarinen | Modular system for the control of compression systems |
| CN101142406A (en) * | 2004-04-30 | 2008-03-12 | 计算机程序控制公司 | Fixed and variable compressor system capacity control |
| JP2012067626A (en) * | 2010-09-21 | 2012-04-05 | Denso Corp | Compressor operation control system |
Family Cites Families (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4502842A (en) | 1983-02-02 | 1985-03-05 | Colt Industries Operating Corp. | Multiple compressor controller and method |
| US5054995A (en) | 1989-11-06 | 1991-10-08 | Ingersoll-Rand Company | Apparatus for controlling a fluid compression system |
| FI104205B1 (en) * | 1994-11-24 | 1999-11-30 | Sarlin Hydor Oy | Method and apparatus for controlling a compression system for a liquid medium |
-
2016
- 2016-06-30 WO PCT/FI2016/050484 patent/WO2017029427A1/en active Application Filing
- 2016-06-30 EP EP16836699.5A patent/EP3334934B1/en active Active
- 2016-06-30 ES ES16836699T patent/ES2900024T3/en active Active
- 2016-06-30 PL PL16836699T patent/PL3334934T3/en unknown
- 2016-06-30 CN CN201680051524.0A patent/CN108138760B/en active Active
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4526513A (en) * | 1980-07-18 | 1985-07-02 | Acco Industries Inc. | Method and apparatus for control of pipeline compressors |
| US6419454B1 (en) * | 2000-06-14 | 2002-07-16 | Leo P. Christiansen | Air compressor control sequencer |
| US20040151593A1 (en) * | 2001-02-02 | 2004-08-05 | Vesa Saarinen | Modular system for the control of compression systems |
| US20030065423A1 (en) * | 2001-09-14 | 2003-04-03 | David Vanderbeek | Compressed gas system |
| CN101142406A (en) * | 2004-04-30 | 2008-03-12 | 计算机程序控制公司 | Fixed and variable compressor system capacity control |
| JP2012067626A (en) * | 2010-09-21 | 2012-04-05 | Denso Corp | Compressor operation control system |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112639644A (en) * | 2018-09-03 | 2021-04-09 | 恩尔赛思有限公司 | Method for analyzing the energy (specific energy consumption) for producing a unit mass or volume of compressed gas |
Also Published As
| Publication number | Publication date |
|---|---|
| ES2900024T3 (en) | 2022-03-15 |
| WO2017029427A1 (en) | 2017-02-23 |
| EP3334934B1 (en) | 2021-08-04 |
| EP3334934A1 (en) | 2018-06-20 |
| EP3334934A4 (en) | 2019-02-20 |
| CN108138760B (en) | 2020-09-25 |
| PL3334934T3 (en) | 2022-05-09 |
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