CN111623239A - Method for monitoring characteristic flow of low-pressure gas pipeline - Google Patents
Method for monitoring characteristic flow of low-pressure gas pipeline Download PDFInfo
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
- F17D—PIPE-LINE SYSTEMS; PIPE-LINES
- F17D3/00—Arrangements for supervising or controlling working operations
- F17D3/01—Arrangements for supervising or controlling working operations for controlling, signalling, or supervising the conveyance of a product
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
- F17D—PIPE-LINE SYSTEMS; PIPE-LINES
- F17D1/00—Pipe-line systems
- F17D1/02—Pipe-line systems for gases or vapours
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
- F17D—PIPE-LINE SYSTEMS; PIPE-LINES
- F17D5/00—Protection or supervision of installations
- F17D5/005—Protection or supervision of installations of gas pipelines, e.g. alarm
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Abstract
The invention provides a method for monitoring characteristic flow of a low-pressure gas pipeline, which is provided with a pressure regulating device, wherein two sides of the pressure regulating device are respectively connected with the low-pressure gas pipeline and a medium-pressure gas pipeline, the pressure regulating device is connected with gas equipment through the low-pressure gas pipeline, a pressure transmitter is arranged on the low-pressure gas pipeline and is used for collecting real-time pressure in the low-pressure gas pipeline, a p-t curve of the pressure and time is established, the slope k of the p-t curve is obtained by continuously calculating the pressure change delta p in delta t time, and the state of the pressure regulating device and the change of the flow in the low-pressure gas pipeline are judged according to the. The low-pressure gas pipeline monitoring system solves the technical problems that a large amount of manpower and time are consumed, the cost is high, the inspection frequency is low, and the safety and reliability are poor due to the fact that the manual inspection mode is mainly adopted for monitoring the low-pressure gas pipeline. The invention can be widely applied to low-pressure gas pipeline monitoring.
Description
Technical Field
The invention relates to a flow monitoring method, in particular to a method for monitoring the characteristic flow of a low-pressure gas pipeline.
Background
Natural gas is one of the most important clean energy sources for human beings, and with the increase of the detected reserves and the progress of the exploitation technology, the use of natural gas is more and more popular. At present, the mode of manual inspection is mainly adopted in the downstream gas pipe network monitoring, and for the downstream low-pressure pipe network monitoring with a plurality of branch pipelines, a large amount of manpower and time need to be consumed, the cost is high, the inspection frequency is lower, and the safety and reliability are poor.
Disclosure of Invention
The invention provides a method for monitoring the characteristic flow of a low-pressure gas pipeline, which can monitor and early warn in real time, has high detection speed, high efficiency and good reliability and aims at solving the technical problems that the existing low-pressure gas pipeline network monitoring mainly adopts a manual inspection mode, needs to consume a large amount of manpower and time, has high cost, lower inspection frequency and poor safety and reliability.
Therefore, the technical scheme is that the method for monitoring the characteristic flow of the low-pressure gas pipeline is provided with a pressure regulating device, two sides of the pressure regulating device are respectively connected with the low-pressure gas pipeline and a medium-pressure gas pipeline, the pressure regulating device is connected with gas equipment through the low-pressure gas pipeline, a pressure transmitter is arranged on the low-pressure gas pipeline and used for collecting real-time pressure in the low-pressure gas pipeline, a p-t curve of the pressure and time is established, the slope k of the p-t curve is obtained by continuously calculating the pressure change amount delta p in delta t time, and the state of the pressure regulating device and the change of the flow in the low-pressure gas pipeline are judged according to the slope k.
Preferably, the specific method for judging the state of the pressure regulating device and the flow change in the low-pressure gas pipeline according to the change of the slope k comprises the following steps:
(1) when the pressure change amplitude | Δ p | exceeds the pressure change threshold value M, dividing the pressure change Δ p into n sections, and respectively setting the pressure difference of the n sections as Δ p1、Δp2…...ΔpnAnd | Δ p | ═ Δ p1|+|Δp2|+……+|ΔpnI, order slope Kn＝ΔpnA/Δ t, if the measured slopes before and after are respectively K1、K2、……KnSequentially calculating the difference value delta K between the front slope and the rear slope1＝K2-K1、ΔK2＝K3-K2、……..ΔKn-1＝Kn-Kn-1And judging the flow change according to the following conditions:
a. if the measured slope Kn<0，ΔKn-1>0, determining that the flow is unchanged, and judging that the pressure regulating device is in a stable state; if Δ Kn-1<0, the flow rate is determined to be changed,namely, the pressure regulating device starts to act, and the flow in the pipeline changes;
b. if the slope K is measuredn>0，ΔKn-1<0, determining that the flow is unchanged, and judging that the pressure regulating device is in a stable state; if Δ Kn-1>0, determining that the flow changes, namely the pressure regulating device starts to act and the flow in the low-pressure gas pipeline changes;
(2) and when the pressure change amplitude value | delta p | is within the pressure change threshold value M, determining that the pressure regulating device is in a stable state.
Preferably, when the pressure in the low-pressure gas pipeline suddenly changes, the pressure regulating device is adjusted to have hysteresis, and in a hysteresis time period, the change of the flow in the low-pressure gas pipeline can be calculated through an ideal gas state equation:
PV＝(P+ΔP)(V+ΔV)
wherein: p is a pressure value before the flow changes;
delta P is a pipe pressure change value after the flow is changed;
Δ t is the lag time;
delta V is the variable quantity of inlet and outlet gases in the low-pressure pipeline within delta t time;
v is the total volume of the pipeline and the appliance behind the valve.
Δ Q is the change in flow.
Preferably, when a large gas appliance is started on the low-pressure gas pipeline, the time spent by the pressure regulating device under the starting flow is delta t', and in order to prevent the large gas appliance from flameout due to delay of opening of a valve port of the pressure regulating device, the design capacity V of the low-pressure gas pipeline should meet the following conditions:
wherein: q: the flow rate of the device; phi: flameout protection pressure of the equipment; pQi (Qi): the pressure of the atmosphere in the environment; p': equipment in low-pressure gas pipelineAbsolute pressure after opening; p' -PQi (Qi): the lowest pressure in the pipeline.
Preferably, the lowest pipeline pressure P' -P for starting large equipment after the low-pressure gas pipelineQi (Qi)Should be greater than the flameout protection pressure Φ of the device.
Preferably, the metering deviation of the metering gauge can be calculated by monitoring the flow increment, and the specific method comprises the following steps:
(1) calibrating the characteristic flow:
firstly, recording flow increment delta q1, delta q2 and delta q3... delta qi... delta qn of each time of starting of the large equipment one by one, wherein i is more than or equal to 1 and less than or equal to n, and is an integer and is used as the characteristic flow of the large equipment; secondly, when the meter metering performance calibration is qualified, the flow increment value delta Q of the corresponding associated meter when the characteristic flow occurs is recorded1、ΔQ2、ΔQ3......ΔQi......ΔQnRealizing the one-to-one correspondence of the characteristic flow and the meter flow increment, and storing;
(2) and (3) calculating gauge measurement deviation:
in the daily use process, when any recorded characteristic flow is monitored, the flow increment delta Q of the current meter is readiiFlow increment Δ Q corresponding to characteristic flow calibrationiThe measurement deviation of the gauge can be obtained by the following calculation:
preferably, still be equipped with the bleed valve on the low pressure gas pipeline, when the bleed action that has intermittent cycle appears in the bleed valve, can judge that pressure regulating device breaks down in the low pressure gas pipeline, the calculation method of the single bleed flow of bleed valve is:
wherein:
p is a pressure value before the flow changes;
delta P is a pipe pressure change value after the flow is changed;
Δ t is the lag time;
delta V is the variable quantity of inlet and outlet gases in the low-pressure pipeline within delta t time;
v is the total volume of the pipeline and the appliance behind the valve;
and multiplying the single diffusion flow by the diffusion time to obtain the single diffusion amount, and accumulating the single diffusion amounts to obtain the total diffusion amount.
The invention has the following beneficial effects:
(1) the pressure transmitter is arranged on the low-pressure gas pipeline, so that the pressure state in the low-pressure gas pipeline is monitored in real time, and the flow variation in the low-pressure gas pipeline is calculated through the action of the pressure regulating device;
(2) the flow after the pressure regulating device is monitored in real time, so that the design of pipe capacity after the pressure regulating device can be assisted, and the metering precision of a metering gauge can be detected, so that the phenomenon of gas stealing can be found in time;
(3) whether the pressure regulating device normally operates can be monitored in real time by arranging the bleeding valve, and the bleeding amount is calculated.
Drawings
FIG. 1 is a system architecture diagram;
FIG. 2 is a flow chart illustrating the status of the rear valve port of the pressure regulating valve;
FIG. 3 is a schematic view of a response time curve of the pressure regulating valve after a new flow rate is added;
FIG. 4 is a schematic view of a periodicity of a diffusion curve.
Detailed Description
The present invention will be further described with reference to the following examples.
As shown in fig. 1, when the municipal gas pipeline supplies gas to a user, decompression treatment is required, and the decompression system mainly comprises a pressure regulating valve and a bleeding valve, and is used for regulating the stability of downstream pressure, so as to ensure that a stable fuel-air ratio (the matching ratio of gas and air) is obtained by the gas appliance.
And a pressure transmitter is arranged on a low-pressure pipeline between the pressure regulating valve and the gas using equipment, and is used for acquiring the pressure on the low-pressure gas pipeline in real time, judging the state of a downstream valve port, monitoring the flow behind the pressure regulating valve, monitoring the metering precision of a related meter and finding the behavior of stealing gas in time.
As shown in fig. 2, the valve port state of the pressure regulating valve can be determined by monitoring the characteristic flow rate after the valve port of the pressure regulating valve, thereby realizing the determination of the actual gas usage state and the pipeline state. The specific method for judging the state of the valve port of the pressure regulating valve comprises the following steps: the real-time pressure in the low-pressure pipeline is collected through the pressure transmitter, a p-t curve of the pressure and the time is established, the slope k of the p-t curve is obtained through continuously calculating the pressure variation delta p in delta t time, and the state of the pressure regulating device and the change of the flow in the low-pressure gas pipeline are judged according to the change of the slope k.
The specific method for judging the state of the pressure regulating device and the flow change in the low-pressure gas pipeline according to the change of the slope k comprises the following steps:
(1) when the pressure change amplitude | Δ p | exceeds a pressure change threshold value M (the M value is related to the specific pipe capacity and the characteristics of the pressure regulating valve, and the value range is normally 20-50 Pa), dividing the pressure change Δ p into n sections, and setting the pressure difference of the n sections as Δ p1、Δp2…...ΔpnAnd | Δ p | ═ Δ p1|+|Δp2|+……+|ΔpnI, order slope Kn＝ΔpnA/Δ t, if the measured slopes before and after are respectively K1、K2、……KnSequentially calculating the difference value delta K between the front slope and the rear slope1＝K2-K1、ΔK2＝K3-K2、……..ΔKn-1＝Kn-Kn-1And judging the flow change according to the following conditions:
a. if the measured slope Kn<0，ΔKn-1>0, determining that the flow is unchanged, and judging that the pressure regulating device is in a stable state; if Δ Kn-1<If 0, the flow is determined to be changed, namely the pressure regulating device starts to act, and the flow in the pipeline is changed;
b. if the slope K is measuredn>0，ΔKn-1<0, determining that the flow is unchanged, and judging that the pressure regulating device is in a stable state; if Δ Kn-1>0, the flow is determined to be changed, namely, the pressure regulating device starts to act and the pipeline flows inwardsThe amount is changed;
(2) and when the pressure change amplitude value | delta p | is within the pressure change threshold value M, determining that the pressure regulating device is in a stable state.
The pressure collected by the pressure transmitter in a certain period of time is set to be in a relatively steady state (a pressure threshold is set according to the actual load condition of the system in advance, and whether the pressure is in the steady state or not is judged according to the pressure threshold, for example, if the pressure threshold is set to be 15MPa, the pressure fluctuation range is within 15Pa, namely, the pressure fluctuation range belongs to the steady state). If a flow is suddenly increased or decreased, the pressure will drop or increase suddenly. The action of the valve port of the pressure regulating valve is automatically adjusted by a mechanical structure, the action response of the valve port can be delayed, and in the delay time period, for the change of the flow, in a shorter time range (assuming that the temperature change is ignored), the change of the flow is calculated by adopting an ideal gas state equation:
PV＝(P+ΔP)(V+ΔV)
wherein: p is a pressure value before the flow changes;
delta P is a pipe pressure change value after the flow is changed;
Δ t is the duration;
delta V is the variable quantity of inlet and outlet gases in the low-pressure pipeline within delta t time;
v is the total volume of the pipeline and the appliance behind the valve.
Δ Q is the change in flow.
As shown in fig. 3, in the state that the pressure in the low-pressure gas pipeline is stable, after the pressure reaches a point a, the pressure is reduced because of the use of a large flow rate after the valve port of the pressure regulating valve, and the time before the point B is reached is the response time Δ t' required for the device to start after the valve, and after the point B, the slope changes.
Assuming that a large gas appliance is started when a pressure regulating valve is closed, a flow rate is used after the valve, or a normal use condition, the response time delta t 'required for the pressure regulating valve to operate at the flow rate is used'For preventing flameout of large-scale gas equipment caused by action delay of pressure regulating valve when valve port is opened, the requirement of meeting P-PQi (Qi)-Φ>0, where P-P can start the deviceQi (Qi): the lowest pressure of the pipe network; phi: flameout protection pressure of the equipment;
on the premise that the equipment meets the starting condition, the pipeline capacity V behind the pressure regulating valve should meet the following conditions:
wherein: q: the flow rate of the device; phi: flameout protection pressure of the equipment; pQi (Qi): the pressure of the atmosphere in the environment; p': absolute pressure after opening of the equipment in the low-pressure pipeline; p' -PQi (Qi): the lowest pressure in the pipeline.
The metering deviation of the metering gauge can be calculated by monitoring the flow increment, and the specific method comprises the following steps:
(1) calibrating the characteristic flow:
firstly, recording flow increment of each large equipment start as delta q1, delta q2 and delta q3... delta qi... delta qn (i is more than or equal to 1 and less than or equal to n, and i is an integer) one by one, and taking the flow increment as the characteristic flow of the large equipment start; secondly, when the meter metering performance calibration is qualified, the increment value of the metering flow of the corresponding associated meter when the characteristic flow occurs is recorded as delta Q1、ΔQ2、ΔQ3......ΔQi......ΔQnRealizing the one-to-one correspondence of the characteristic flow and the meter metering flow increment, and storing;
(2) and (3) calculating gauge measurement deviation:
in the use process at a later date, when any characteristic flow, such as delta qi, which accords with the record in the step (1) is monitored, the actual metering flow increment delta Q of the current meter is readiiFlow increment Δ Q corresponding to characteristic flow calibrationiThe measurement deviation of the gauge can be obtained by the following calculation:
as shown in fig. 4, if the valve port of the pressure regulating valve is not closed tightly or the pressure regulating valve is damaged, when the pressure rises to the lower limit value of the bleeding valve after the valve, the bleeding valve is triggered to bleed, so that the pressure drops, the bleeding valve is closed, the pressure rises again, the bleeding valve bleeds again, the process has a certain intermittent period, and it can be determined that the bleeding valve has a bleeding behavior according to the formula:
wherein: p is a pressure value before the flow changes;
delta P is a pipe pressure change value after the flow is changed;
Δ t is the duration;
delta V is the variable quantity of inlet and outlet gases in the low-pressure pipeline within delta t time;
v is the total volume of the pipeline and the appliance behind the valve.
The single diffusing flow can be calculated, the single diffusing flow is obtained by multiplying the diffusing time, and the total diffusing flow can be obtained by accumulation.
By the technical scheme, the pressure state of the low-pressure gas pipeline can be monitored in real time, the valve port state of the pressure regulating valve can be judged, the flow variation in the low-pressure gas pipeline can be obtained through calculation, and the design of the pipe volume after the pressure regulating device is assisted; the monitoring of the pressure state can also be used for detecting the metering precision of the metering gauge, so that the phenomenon of gas stealing can be conveniently found in time; whether the pressure regulating valve normally operates can be monitored in real time through the arrangement of the bleeding valve, and the bleeding amount is calculated. The whole system realizes the judgment of the downstream valve port state, the monitoring of the flow behind the valve, the monitoring of the metering precision of the meter and the effective monitoring of the behavior of stealing gas by monitoring the pressure state, eliminates the defect of manual inspection, and has the advantages of time saving, labor saving, safety and reliability.
However, the above description is only exemplary of the present invention, and the scope of the present invention should not be limited thereby, and the replacement of the equivalent components or the equivalent changes and modifications made according to the protection scope of the present invention should be covered by the claims of the present invention.
Claims (7)
1. The utility model provides a method of monitoring low pressure gas pipeline characteristic flow, is equipped with the regulator, low pressure gas pipeline and middling pressure gas pipeline are connected respectively to the regulator both sides, the regulator warp low pressure gas pipeline is connected with gas appliances, its characterized in that, be equipped with pressure transmitter on the low pressure gas pipeline, pressure transmitter is used for gathering real-time pressure in the low pressure gas pipeline sets up the p-t curve of pressure and time to through constantly calculating delta t time internal pressure variation delta p, reacing the slope k of p-t curve, judge according to slope k regulator's state reaches the change of low pressure gas pipeline internal flow.
2. The method for monitoring the characteristic flow of the low-pressure gas pipeline according to claim 1, wherein the specific method for judging the state of the pressure regulating device and the flow change in the low-pressure gas pipeline according to the change of the slope k comprises the following steps:
(1) when the pressure change amplitude | Δ p | exceeds the pressure change threshold value M, dividing the pressure change Δ p into n sections, and respectively setting the pressure difference of the n sections as Δ p1、Δp2…...ΔpnAnd | Δ p | ═ Δ p1|+|Δp2|+……+|ΔpnI, order slope Kn＝ΔpnA/Δ t, if the measured slopes before and after are respectively K1、K2、……、KnSequentially calculating the difference value delta K between the front slope and the rear slope1＝K2-K1、ΔK2＝K3-K2、……..ΔKn-1＝Kn-Kn-1And judging the flow change according to the following conditions:
a. if the measured slope Kn<0，ΔKn-1>0, determining that the flow is unchanged, and judging that the pressure regulating device is in a stable state; if Δ Kn-1<If 0, the flow is determined to be changed, namely the pressure regulating device starts to act, and the flow in the pipeline is changed;
b. if the slope K is measuredn>0，ΔKn-1<0, determining the flow unchanged, and judging the pressure regulating deviceIn a stable state; if Δ Kn-1>If 0, the flow is determined to be changed, namely the pressure regulating device starts to act, and the flow in the pipeline is changed;
(2) and when the pressure change amplitude value | delta p | is within the pressure change threshold value M, determining that the flow is unchanged, and the pressure regulating device is in a stable state.
3. A method for calculating the flow change by applying the method of claim 1, wherein when the pressure in the low-pressure gas pipeline suddenly changes, the pressure regulating device is adjusted to have hysteresis, and the change of the flow in the low-pressure gas pipeline in the hysteresis time period can be calculated by an ideal gas state equation:
PV＝(P+ΔP)(V+ΔV)
wherein: p is a pressure value before the flow changes;
delta P is a pipe pressure change value after the flow is changed;
Δ t is the lag time;
delta V is the variable quantity of inlet and outlet gases in the low-pressure pipeline within delta t time;
v is the total volume of the pipeline and the appliance behind the valve;
Δ Q is the change in flow.
4. A method for designing pipe capacity by applying the method of claim 3, wherein when a large gas appliance is started on the low-pressure gas pipe, the time taken for the pressure regulating device to respond to the starting flow of the appliance is Δ t', and in order to prevent the large gas appliance from extinguishing due to the delay of the opening of the valve port of the pressure regulating device, the low-pressure gas pipe design capacity V should satisfy the following condition:
wherein: q: of devicesFlow rate; phi: flameout protection pressure of the equipment; pQi (Qi): the pressure of the atmosphere in the environment; p': absolute pressure after opening of the equipment in the low-pressure pipeline; p' -PQi (Qi): the lowest pressure in the pipeline.
5. The method for designing pipe capacity according to claim 4, wherein the lowest pipe pressure P' -P of the low-pressure gas pipeQi (Qi)Should be greater than the flameout protection pressure Φ of the device.
6. A method for calculating a metering deviation of a meter by applying the method of claim 3, wherein the metering deviation of the meter can be calculated by monitoring a flow increment, and the method comprises the following steps:
(1) calibrating the characteristic flow:
firstly, recording flow increment delta q1, delta q2 and delta q3... delta qi... delta qn of each time of starting of the large equipment one by one, wherein i is more than or equal to 1 and less than or equal to n, and is an integer and is used as the characteristic flow of the large equipment; secondly, when the meter metering performance calibration is qualified, the flow increment value delta Q of the corresponding associated meter when the characteristic flow occurs is recorded1、ΔQ2、ΔQ3......ΔQi......ΔQnRealizing the one-to-one correspondence of the characteristic flow and the meter flow increment, and storing;
(2) and (3) calculating gauge measurement deviation:
in the daily use process, when any recorded characteristic flow is monitored, the flow increment delta Q of the current meter is readiiFlow increment Δ Q corresponding to characteristic flow calibrationiThe measurement deviation of the gauge can be obtained by the following calculation:
7. the method for calculating the amount of the released gas by applying the method of claim 1, wherein a release valve is further arranged on the low-pressure gas pipeline, when the release valve has a gas release action with an intermittent period, it can be determined that the pressure regulating device does not normally operate, and the method for calculating the single-time released flow of the release valve comprises the following steps:
wherein: p is a pressure value before the flow changes;
delta P is a pipe pressure change value after the flow is changed;
Δ t is the lag time;
delta V is the variable quantity of inlet and outlet gases in the low-pressure pipeline within delta t time;
v is the total volume of the pipeline and the appliance behind the valve;
and multiplying the single diffusion flow by the diffusion time to obtain the single diffusion amount, and accumulating the single diffusion amounts to obtain the total diffusion amount.
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| CN112254007A (en) * | 2020-11-10 | 2021-01-22 | 瑞星久宇燃气设备（成都）有限公司 | Low-pressure pipe network temperature-pressure self-adaptive protection system and method |
| CN112254007B (en) * | 2020-11-10 | 2024-06-04 | 瑞星久宇燃气设备（成都）有限公司 | Low-pressure pipe network temperature-pressure self-adaptive protection system and method |
| CN113236971A (en) * | 2021-05-31 | 2021-08-10 | 威海盛泰智能仪器仪表有限公司 | Method for realizing liquefied petroleum gas safety management by monitoring change of medium pressure |
| CN113339701A (en) * | 2021-05-31 | 2021-09-03 | 威海盛泰智能仪器仪表有限公司 | Method for realizing bottled liquefied gas safety management through temperature monitoring |
| CN113339701B (en) * | 2021-05-31 | 2022-07-01 | 威海盛泰智能仪器仪表有限公司 | Method for realizing bottled liquefied gas safety management through temperature monitoring |
| CN113654899A (en) * | 2021-07-30 | 2021-11-16 | 深圳市中金岭南有色金属股份有限公司凡口铅锌矿 | Pressure analysis method, device and equipment for conveying pipeline and storage medium |
| CN113654899B (en) * | 2021-07-30 | 2023-12-22 | 深圳市中金岭南有色金属股份有限公司凡口铅锌矿 | Pressure analysis method, device, equipment and storage medium for conveying pipeline |
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| Publication number | Publication date |
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| CN113154258B (en) | 2022-12-13 |
| CN113154258A (en) | 2021-07-23 |
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Application publication date: 20200904 |