CN112304380A - Method for circularly accumulating natural gas flow in distributed control system - Google Patents
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- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 title claims abstract description 108
- 239000003345 natural gas Substances 0.000 title claims abstract description 54
- 238000000034 method Methods 0.000 title claims abstract description 15
- 238000005070 sampling Methods 0.000 claims abstract description 42
- 238000009825 accumulation Methods 0.000 claims abstract description 15
- 230000001105 regulatory effect Effects 0.000 claims abstract description 11
- 230000001186 cumulative effect Effects 0.000 claims description 33
- 125000004122 cyclic group Chemical group 0.000 claims description 10
- 230000010354 integration Effects 0.000 claims 2
- 238000010586 diagram Methods 0.000 description 5
- 230000006870 function Effects 0.000 description 3
- 238000012544 monitoring process Methods 0.000 description 3
- 230000001276 controlling effect Effects 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000005540 biological transmission Effects 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 239000003245 coal Substances 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 238000003384 imaging method Methods 0.000 description 1
- 238000009776 industrial production Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000011159 matrix material Substances 0.000 description 1
- 238000005272 metallurgy Methods 0.000 description 1
- 239000003208 petroleum Substances 0.000 description 1
- 238000004886 process control Methods 0.000 description 1
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- G—PHYSICS
- G01—MEASURING; TESTING
- G01F—MEASURING VOLUME, VOLUME FLOW, MASS FLOW OR LIQUID LEVEL; METERING BY VOLUME
- G01F15/00—Details of, or accessories for, apparatus of groups G01F1/00 - G01F13/00 insofar as such details or appliances are not adapted to particular types of such apparatus
- G01F15/07—Integration to give total flow, e.g. using mechanically-operated integrating mechanism
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- G—PHYSICS
- G05—CONTROLLING; REGULATING
- G05B—CONTROL OR REGULATING SYSTEMS IN GENERAL; FUNCTIONAL ELEMENTS OF SUCH SYSTEMS; MONITORING OR TESTING ARRANGEMENTS FOR SUCH SYSTEMS OR ELEMENTS
- G05B19/00—Programme-control systems
- G05B19/02—Programme-control systems electric
- G05B19/418—Total factory control, i.e. centrally controlling a plurality of machines, e.g. direct or distributed numerical control [DNC], flexible manufacturing systems [FMS], integrated manufacturing systems [IMS] or computer integrated manufacturing [CIM]
- G05B19/41845—Total factory control, i.e. centrally controlling a plurality of machines, e.g. direct or distributed numerical control [DNC], flexible manufacturing systems [FMS], integrated manufacturing systems [IMS] or computer integrated manufacturing [CIM] characterised by system universality, reconfigurability, modularity
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- G—PHYSICS
- G06—COMPUTING; CALCULATING OR COUNTING
- G06F—ELECTRIC DIGITAL DATA PROCESSING
- G06F17/00—Digital computing or data processing equipment or methods, specially adapted for specific functions
- G06F17/10—Complex mathematical operations
- G06F17/15—Correlation function computation including computation of convolution operations
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- G—PHYSICS
- G05—CONTROLLING; REGULATING
- G05B—CONTROL OR REGULATING SYSTEMS IN GENERAL; FUNCTIONAL ELEMENTS OF SUCH SYSTEMS; MONITORING OR TESTING ARRANGEMENTS FOR SUCH SYSTEMS OR ELEMENTS
- G05B2219/00—Program-control systems
- G05B2219/30—Nc systems
- G05B2219/33—Director till display
- G05B2219/33273—DCS distributed, decentralised controlsystem, multiprocessor
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- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P90/00—Enabling technologies with a potential contribution to greenhouse gas [GHG] emissions mitigation
- Y02P90/02—Total factory control, e.g. smart factories, flexible manufacturing systems [FMS] or integrated manufacturing systems [IMS]
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Abstract
The invention discloses a method for circularly accumulating natural gas flow in a decentralized control system, which comprises the following steps of: 1) natural gas instantaneous flow Q of pressure regulating station inlet measured by pressure regulating station inlet flowmeter0(ii) a 2) Calculating the natural gas instantaneous flow Q of a sampling periodi(ii) a 3) Setting the total accumulated flow of the kth sampling period as L0(ii) a 4) Dividing the total circulation accumulated flow time into a plurality of groups, wherein the total single circulation time of the t-th group is Mt(h) Dividing the total time of a single cycle into NtEach shift, wherein the time length of each shift is mt(h),Mt=mt×Nt(ii) a 5) The circulation accumulated flow of each shift in each group is obtained to complete the circulation accumulation of the natural gas flow in the distributed control system, and the method can realize the automatic circulation of the natural gas flowAnd (6) accumulating.
Description
Technical Field
The invention belongs to the technical field of industrial information control, and relates to a method for circularly accumulating natural gas flow in a decentralized control system.
Background
With the transformation adjustment of national energy structures, compared with the high emission of coal and petroleum, the instability of wind energy and solar energy and the safety risk of nuclear energy, the low-carbon clean natural gas is becoming the development direction of energy consumption. In the industrial production process, the accurate recording of the accumulated flow of the natural gas usage in the shift is an important index for measuring the enterprise operation management level.
A Distributed Control System (DCS) is a multi-level computer Control System consisting of a process Control level and a process monitoring level. The basic ideas of centralized management and decentralized control are adopted to complete the functions of monitoring and controlling production equipment in real time, and the method is widely applied to industries such as electric power, metallurgy, petrochemical industry and the like. For the convenience of actual programming of engineers, the programs of the distributed control system are compiled by imaging logic configuration languages, but the difficulty of realizing loop iteration is increased.
Disclosure of Invention
The present invention aims to overcome the disadvantages of the prior art and to provide a method for cyclically accumulating natural gas flow in a decentralized control system, which enables automatic cyclic accumulation of natural gas flow.
In order to achieve the above object, the method for cyclically accumulating the natural gas flow in the decentralized control system according to the present invention comprises the following steps:
1) natural gas instantaneous flow Q of pressure regulating station inlet measured by pressure regulating station inlet flowmeter0Then sending the data to a distributed control system;
2) the distributed control system calculates the natural gas instantaneous flow Q of a sampling periodi;
3) When the preset input time is reached, the cumulative natural gas flow is recorded, wherein the total cumulative flow of the kth sampling period is set to be L0;
4) Dividing the total circulation accumulated flow time into a plurality of groups, wherein the total single circulation time of the t-th group is Mt(h) Dividing the total time of a single cycle into NtEach shift, wherein the time length of each shift is mt(h),Mt=mt×Nt;
5) Calculating the cumulative time k of the current cycle divided by MtRemainder k of x 36000t;
6) When remainder ktIn the range of 1 to 36000 x mtCumulative flow L of the 1 st shift of the t group at the k sampling time within the sampling timet1Comprises the following steps:
7) repeating the step 6), and calculating the accumulated flow of each shift of the tth group, wherein the accumulated flow of the pth shift of the tth group is LtpWhen k istAt 36000X (p-1). times.mt+1~36000×p×mtWithin the sampling time, the cumulative flow L of the pth group and the pth shift of the kth sampling timetpComprises the following steps:
8) when remainder ktAt 36000 xMt-36000×mt+1~36000×MtWithin the sampling time of (c), then the nth group of the kth sampling timetCumulative flow L of shiftt,NtComprises the following steps:
9) and (6), 7) and 8) are repeated to obtain the circulating accumulated flow of each shift in each group, and the circulating accumulation of the natural gas flow in the distributed control system is completed.
Further comprising: the total accumulated flow L0Current cumulative flow (L) of each shift of group 111,L12,……,L1N1) … …, current cumulative flow (L) of each shift of the t-th groupt1,Lt2,……,LtNt) Stored in a history repository.
Instantaneous flow Q of natural gas for one sampling periodiComprises the following steps:
wherein the sampling period is 100 ms;
when Q is0≤20Nm3When the sampling time is/h, the natural gas instantaneous flow at the current sampling time is zero, and when the sampling time is Q0>20Nm3At the hour of/h, the instantaneous flow of the natural gas at the current sampling moment is Qi。
Total cumulative flow L for the kth sampling period0Comprises the following steps:
the invention has the following beneficial effects:
the method for circularly accumulating the natural gas flow in the distributed control system utilizes the distributed control system to calculate the accumulated flow L by grouping and classifying times during specific operationt1Therefore, the circulation accumulated flow of each shift in each group is obtained, the automatic circulation accumulation of the natural gas flow is realized, and the automation degree of monitoring, recording, predicting and controlling the natural gas flow by operators is improved. The flow of the natural gas is accurately and reliably monitored.
Drawings
FIG. 1 is a general diagram of the present invention;
FIG. 2 is a flow chart of the present invention;
FIG. 3 is a configuration diagram of the total cumulative natural gas flow in the decentralized control system according to the present invention;
FIG. 4 is a logic configuration diagram of the cumulative flow of three shifts of natural gas cycles per day in a decentralized control system according to the present invention.
FIG. 5 shows the t-th component N in the present inventiontTotal time of single cycle of shift MtTime length of m per shifttThe logic configuration diagram of the natural gas circulation accumulated flow in the distributed control system.
Detailed Description
The invention is described in further detail below with reference to the accompanying drawings:
referring to fig. 1 to 4, the method for cyclically accumulating the natural gas flow in the distributed control system according to the present invention includes the following steps:
1) natural gas instantaneous flow Q of pressure regulating station inlet measured by pressure regulating station inlet flowmeter0Then sending the data to a distributed control system;
2) natural gas flow Q measured by pressure regulating station inlet flowmeter0≤20Nm3When the natural gas flow in the inlet pipeline of the pressure regulating station is zero, the distributed control system judges that the natural gas flow in the inlet pipeline of the pressure regulating station is zero; when Q is0>20Nm3When the flow rate is/h, the instantaneous flow rate of the natural gas in the current sampling period is Qi;
Then the instantaneous flow Q of the natural gas for one sampling periodi=Q 036000, wherein one sampling period is 100 ms;
setting a natural gas circulation accumulation input button, an exit button and a preset input time button, and respectively finishing the functions of starting circulation accumulation, exiting circulation accumulation and clearing the accumulated flow of each section and the specific moment of starting circulation accumulation.
The initial value of the total natural gas accumulated flow is zero, and the circular accumulated exit button can initialize and clear the total natural gas accumulated flow and the accumulated flow of each section.
3) When the preset input time is reached, the cumulative natural gas flow is recorded, wherein the total cumulative flow of the kth sampling period is set to be L0Wherein, in the step (A),
4) dividing the total circulation accumulated flow time into a plurality of groups, wherein the total single circulation time of the t-th group is Mt(h) Dividing the total time of a single cycle into NtEach shift, wherein the time length of each shift is mt(h),Mt=mt×Nt;
For example, the flow is divided into groups according to year, quarter, month, day of the week, etc., and the cyclic cumulative flow calculation is performed on each shift for the t groups, for example, group 1 is the cyclic cumulative flow of three shifts per day, that is, the cyclic cumulative flow of 0 to 8 hours, the cyclic cumulative flow of 8 to 16 hours, and the cyclic cumulative flow of 16 to 24 hours.
5) Calculating the cumulative time k of the current cycle divided by MtRemainder k of x 36000t;
6) When remainder ktIn the range of 1 to 36000 x mtCumulative flow L of the 1 st shift of the t group at the k sampling time within the sampling timet1Comprises the following steps:
wherein z is11Initial value is 1, after one cycle period is finished, z11Automatically adding 1;
cumulative m of cyclestAfter the time length, the current value of the cumulative flow of the 1 st shift of the tth group is Mt-2mtKeeping the time length unchanged, resetting and keeping mtThe next cycle is entered after the time period.
7) Repeating the step 6), and calculating the accumulated flow of each shift of the tth group, wherein the accumulated flow of the pth shift of the tth group is LtpWhen k istAt 36000X (p-1). times.mt+1~36000×p×mtWithin the sampling time, the cumulative flow L of the pth group and the pth shift of the kth sampling timetpComprises the following steps:
cumulative m of cyclestAfter the time length, the current value of the cumulative flow of the pth shift of the tth group is Mt-2mtKeeping the time length unchanged, resetting and keeping mtAfter a certain period of time, enter the next cycle, i.e. ztp=ztp+1。
8) When remainder ktAt 36000 xMt-36000×mt+1~36000×MtWithin the sampling time of (c), then the nth group of the kth sampling timetCumulative flow L of shiftt,NtComprises the following steps:
cumulative m of cyclestAfter a certain period of time, the nth grouptThe current value of the cumulative flow of the shift is Mt-2mtKeeping the time length unchanged, resetting and keeping mtAfter a certain period of time, enter the next cycle, i.e. zt,Nt=zt,Nt+1。
9) And (6), 7) and 8) are repeated to obtain the circulating accumulated flow of each shift in each group, and the circulating accumulation of the natural gas flow in the distributed control system is completed.
The invention also includes: the total accumulated flow L0Current cumulative flow (L) of each shift of group 111,L12,……,L1N1) … …, current cumulative flow (L) of each shift of the t-th groupt1,Lt2,……,LtNt) And storing the current accumulated flow of each shift of the t groups in a history library, wherein the current accumulated flow of each shift of the t groups can be simplified into a matrix L:
referring to FIG. 5, the t-th component NtTotal time of single cycle of shift MtThe time length of each shift is mtThe configuration diagram of the natural gas circulation accumulated flow in the distributed control system, the broken line represents a switching value logic judgment loop, and the solid line represents a switching value logic judgment loopAnalog real-time data transmission loop. As can be seen from fig. 5, based on the graphical programming language of the distributed control system, the delay block TON, the and gate and, the not gate, and the switch block T are used comprehensively to implement the function of the natural gas flow cyclic accumulation, which corresponds to the T-th group of cyclic accumulation L in fig. 5tpThe specific operation is as follows:
1a) accumulating the input buttons by natural gas circulation and passing (p-1) m after the preset input time is reachedtAfter a time period of LtpBegin to accumulate from zero;
2a)Ltpto mtAfter the hours of the cycle are accumulated, M is maintainedt-mtConstant in hours, LtpZero clearing hold mtHour, accumulation resumes after the end of a cycle period.
3a) Repeating step 2a), accumulating L cyclicallytp。
4a) Start Natural gas circulation cumulative Exit button, LtpAnd stopping clearing.
The logic blocks used by the graphical program language include a delay TON, an AND gate AND, an NOT gate NOT, an OR gate OR, a pulse block, a constant block, an accumulation block SUM, AND a switching block T.
The invention overcomes the defect that the graphical program does not have compliable statements such as for, while, if and the like, which are not easy to realize circulation, and simultaneously does not bring extra cost to the system, which is also an advantage of the invention.
Claims (4)
1. A method for circularly accumulating natural gas flow in a decentralized control system is characterized by comprising the following steps:
1) natural gas instantaneous flow Q of pressure regulating station inlet measured by pressure regulating station inlet flowmeter0Then sending the data to a distributed control system;
2) the distributed control system calculates the natural gas instantaneous flow Q of a sampling periodi;
3) When the preset input time is reached, the cumulative natural gas flow is recorded, wherein the total cumulative flow of the kth sampling period is set to be L0;
4) Integrating the total circulationThe flow duration is divided into a plurality of groups, wherein the total duration of the single circulation of the tth group is Mt(h) Dividing the total time of a single cycle into NtEach shift, wherein the time length of each shift is mt(h),Mt=mt×Nt;
5) Calculating the cumulative time k of the current cycle divided by MtRemainder k of x 36000t;
6) When remainder ktIn the range of 1 to 36000 x mtCumulative flow L of the 1 st shift of the t group at the k sampling time within the sampling timet1Comprises the following steps:
7) repeating the step 6), and calculating the accumulated flow of each shift of the tth group, wherein the accumulated flow of the pth shift of the tth group is LtpWhen k istAt 36000X (p-1). times.mt+1~36000×p×mtWithin the sampling time, the cumulative flow L of the pth group and the pth shift of the kth sampling timetpComprises the following steps:
8) when remainder ktAt 36000 xMt-36000×mt+1~36000×MtWithin the sampling time of (c), then the nth group of the kth sampling timetCumulative flow L of shiftt,NtComprises the following steps:
9) and (6), 7) and 8) are repeated to obtain the circulating accumulated flow of each shift in each group, and the circulating accumulation of the natural gas flow in the distributed control system is completed.
2. Natural gas flow circulation in a decentralized control system according to claim 1The method of accumulation, characterized by, further comprising: the total accumulated flow L0Current cumulative flow (L) of each shift of group 111,L12,……,L1N1) … …, current cumulative flow (L) of each shift of the t-th groupt1,Lt2,……,LtNt) Stored in a history repository.
3. Method for cyclic integration of natural gas flows in decentralized control system according to claim 1, characterized in that the instantaneous flow Q of natural gas is measured for one sampling periodiComprises the following steps:
wherein the sampling period is 100 ms;
when Q is0≤20Nm3When the sampling time is/h, the natural gas instantaneous flow at the current sampling time is zero, and when the sampling time is Q0>20Nm3At the hour of/h, the instantaneous flow of the natural gas at the current sampling moment is Qi。
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Citations (5)
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JPH11281413A (en) * | 1998-03-31 | 1999-10-15 | Yazaki Corp | Flow rate measuring method and device, and electronic gas meter |
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JP2004354398A (en) * | 2004-09-17 | 2004-12-16 | Matsushita Electric Ind Co Ltd | Flowmeter |
CN104748810A (en) * | 2015-03-16 | 2015-07-01 | 江苏永钢集团有限公司 | Fluid flow accumulating system |
CN105973321A (en) * | 2015-07-07 | 2016-09-28 | 成都国光电子仪表有限责任公司 | Microcomputer metering system for natural gas |
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Patent Citations (5)
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JPH11281413A (en) * | 1998-03-31 | 1999-10-15 | Yazaki Corp | Flow rate measuring method and device, and electronic gas meter |
JP2003270009A (en) * | 2002-03-15 | 2003-09-25 | Matsushita Electric Ind Co Ltd | Method for measuring and displaying flow rate and flowmeter using the same |
JP2004354398A (en) * | 2004-09-17 | 2004-12-16 | Matsushita Electric Ind Co Ltd | Flowmeter |
CN104748810A (en) * | 2015-03-16 | 2015-07-01 | 江苏永钢集团有限公司 | Fluid flow accumulating system |
CN105973321A (en) * | 2015-07-07 | 2016-09-28 | 成都国光电子仪表有限责任公司 | Microcomputer metering system for natural gas |
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