CN113803642A - Compressed gas distribution method and system - Google Patents

Compressed gas distribution method and system Download PDF

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Publication number
CN113803642A
CN113803642A CN202111099025.8A CN202111099025A CN113803642A CN 113803642 A CN113803642 A CN 113803642A CN 202111099025 A CN202111099025 A CN 202111099025A CN 113803642 A CN113803642 A CN 113803642A
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gas
equipment
compressed gas
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compressed
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CN113803642B (en
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王端阳
庄春源
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Shenzhen Fox Energy Technology Co ltd
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Shenzhen Fox Energy Technology Co ltd
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    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17DPIPE-LINE SYSTEMS; PIPE-LINES
    • F17D3/00Arrangements for supervising or controlling working operations
    • F17D3/01Arrangements for supervising or controlling working operations for controlling, signalling, or supervising the conveyance of a product
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17DPIPE-LINE SYSTEMS; PIPE-LINES
    • F17D3/00Arrangements for supervising or controlling working operations
    • F17D3/18Arrangements for supervising or controlling working operations for measuring the quantity of conveyed product

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  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Filling Or Discharging Of Gas Storage Vessels (AREA)
  • Feeding, Discharge, Calcimining, Fusing, And Gas-Generation Devices (AREA)

Abstract

The application discloses a compressed gas distribution method and a system thereof. The distribution method is applied to a compressed gas distribution system, the compressed gas distribution system comprises a plurality of gas utilization devices and an air compression device, the air compression device is used for generating compressed gas, the distribution method comprises the steps of obtaining the total flow of the compressed gas transmitted to the plurality of gas utilization devices by the air compression device, selecting representative gas utilization devices from the plurality of gas utilization devices, obtaining the average flow of the compressed gas required by the representative gas utilization devices, obtaining the gas utilization time of the plurality of gas utilization devices, obtaining the accumulated flow of each gas utilization device based on the gas utilization time and the average flow, and distributing the total flow to each gas utilization device based on the accumulated flow. Therefore, the accumulated flow of a plurality of gas utilization equipment can be obtained only by metering the gas utilization of the representative gas utilization equipment, the metering cost is reduced, the energy consumption management is convenient to strengthen, and the energy-saving control measures are taken in time to reduce the waste of the compressed gas.

Description

Compressed gas distribution method and system
Technical Field
The application relates to the field of compressed air energy-saving management, in particular to a compressed gas distribution method and a compressed gas distribution system.
Background
Compressed gas is the second largest power source next to electricity, and is widely applied to the industrial field. In most enterprises, the energy consumption of the air compressor accounts for 10% -35% of the total energy consumption of the enterprise. The compressed gas is prepared by an air compressor of an air compression station, is sent into a workshop through a compressed gas pipe network after being pretreated, and is supplied to each gas end device.
The quantity of gas appliances is many usually, if measure respectively to all gas appliances, can increase more measurement cost to, gas appliances's connecting tube pipe diameter is less, mostly pulse gas, and the compressed gas flowmeter of installation of not being convenient for, and metering error is great.
Disclosure of Invention
In order to solve the technical problems that in the prior art, the flow of compressed gas distributed by each gas-using device is not beneficial to calculation, and the energy consumption, cost and the like of each gas-using device are not beneficial to distribution and calculation, the application provides a compressed gas distribution method and a system thereof.
In order to solve the above problem, an embodiment of the present application provides a compressed gas distribution method, which is applied to a compressed gas distribution system including a plurality of gas-using devices and an air compression device for generating compressed gas, and the distribution method includes: acquiring the total flow of the compressed gas transmitted to the plurality of gas-using equipment by the air compression device; selecting representative gas-using equipment from the plurality of gas-using equipment, and acquiring the average flow of compressed gas required by the representative gas-using equipment; the method comprises the steps of obtaining gas using time of the plurality of gas using equipment, obtaining accumulated flow of each gas using equipment based on the gas using time and the average flow, and distributing the total flow to each gas using equipment based on the accumulated flow.
In order to solve the technical problem, the application further provides a compressed gas distribution system, which comprises a plurality of gas utilization devices, an air compression device and a control device, wherein the air compression device is used for generating compressed gas, and the control device is used for controlling the compressed gas distribution system to realize the compressed gas distribution method.
Compared with the prior art, the compressed gas distribution method is applied to the compressed gas distribution system, the compressed gas distribution system comprises a plurality of gas utilization devices and the air compression device, the air compression device is used for generating the compressed gas, and the distribution method comprises the following steps: the method comprises the steps of obtaining total flow of compressed gas transmitted to a plurality of gas using equipment by an air compression device, selecting representative gas using equipment from the plurality of gas using equipment, obtaining average flow of the compressed gas required by the representative gas using equipment, obtaining gas using time of the plurality of gas using equipment, obtaining accumulated flow of each gas using equipment based on the gas using time and the average flow, and distributing the total flow to each gas using equipment based on the accumulated flow. Therefore, by the mode, the accumulated flow of a plurality of gas utilization equipment can be obtained only by metering the gas utilization of representative gas utilization equipment, the metering cost is reduced, and meanwhile, the compressed gas can be distributed based on the accumulated flow, so that the energy consumption index of the compressed gas can be decomposed to production teams, machines and individuals according to the distribution result of the compressed gas, the energy consumption management is facilitated, and the energy-saving control measures are taken in time to reduce the waste of the compressed gas.
It is to be understood that both the foregoing general description and the following detailed description are exemplary and explanatory only and are not restrictive of the application.
Drawings
In order to more clearly illustrate the embodiments of the present application or the technical solutions in the prior art, the drawings needed to be used in the embodiments will be briefly described below, and it is obvious that the drawings in the following description are only some embodiments of the present application, and it is obvious for those skilled in the art to obtain other drawings without creative efforts.
FIG. 1 is a schematic flow diagram of one embodiment of a compressed gas distribution method provided herein;
FIG. 2 is a schematic flowchart of an embodiment of step S103 shown in FIG. 1 provided herein;
FIG. 3 is a flowchart illustrating an embodiment of step S102 shown in FIG. 1 provided herein;
FIG. 4 is a schematic block diagram illustrating one embodiment of a compressed gas distribution system provided herein;
fig. 5 is a schematic structural diagram of an embodiment of the control device provided in the present application.
Detailed Description
The present application will be described in further detail with reference to the following drawings and examples. It is to be noted that the following examples are only illustrative of the present application, and do not limit the scope of the present application. Likewise, the following examples are only some examples and not all examples of the present application, and all other examples obtained by a person of ordinary skill in the art without any inventive step are within the scope of the present application.
Reference herein to "an embodiment" means that a particular feature, structure, or characteristic described in connection with the embodiment can be included in at least one embodiment of the application. The appearances of the phrase in various places in the specification are not necessarily all referring to the same embodiment, nor are separate or alternative embodiments mutually exclusive of other embodiments. It is explicitly and implicitly understood by one skilled in the art that the embodiments described herein can be combined with other embodiments.
Throughout the description of the present application, it is intended that the terms "mounted," "disposed," "connected," and "connected" be construed broadly and encompass, for example, fixed connections, removable connections, or integral connections unless expressly stated or limited otherwise; can be mechanically connected or electrically connected; they may be directly connected or may be connected via an intermediate medium. To one of ordinary skill in the art, the foregoing may be combined in any suitable manner with the specific meaning ascribed to the present application.
The compressed gas distribution method provided by the application is applied to a compressed gas distribution system, and the compressed gas distribution system comprises a plurality of gas utilization devices and an air compression device, wherein the air compression device is used for generating compressed gas.
The air compressing device is connected with the plurality of gas utilization equipment through pipelines, and after the air compressing device generates compressed gas, the compressed gas is transmitted to the gas utilization equipment needing to use the compressed gas through the pipelines. The air compressor device can be an air compressor in an air compression station, and the air compressor absorbs gas and forms compressed gas meeting the use condition after processing. The gas may include air or other gas that meets the actual use conditions. The gas-using equipment comprises an electromagnetic valve, a fluid control valve, a cylinder, a quick connector, a pneumatic screwdriver and the like, and the equipment can be the gas-using equipment as long as the equipment needs to use compressed gas in operation.
In practical application, even in the same production line of a certain working space, the number of gas-using equipment is also very large, and is few, then several hundred, and is many, then several thousand, and if calculate the gas-using volume of every gas-using equipment, can increase more cost undoubtedly to gas-using equipment is mostly pulse gas-using, and its pipe diameter of connecting is usually less, and the flow detection device of compressed gas is not convenient for install, even if install flow detection device at the gas-using equipment department that the pipe diameter is less, it has great error equally. In addition, if the gas consumption of the gas utilization equipment is not clear, the energy consumption and the cost of each gas utilization equipment are not favorably distributed and calculated, and the energy consumption index of the compressed gas is not favorably decomposed to a team and an energy consumption benchmarking and the like.
In order to solve at least one technical problem in the prior art, the present application provides a compressed gas distribution method, and referring to fig. 1, fig. 1 is a schematic flow chart of an embodiment of the compressed gas distribution method provided in the present application. As shown in fig. 1, the compressed gas distribution method provided by the present application may include the following steps S101 to S103, specifically:
step S101: and acquiring the total flow of the compressed gas transmitted to a plurality of gas-using equipment by the air compressing device.
After the air compressing device generates the compressed gas, the compressed gas needs to be transmitted to each gas consuming device which needs to use the compressed gas. In an application scene, can be through a house steward and a plurality of branch connection between air compression device and a plurality of gas appliances, house steward connection air compression device, gas appliances are connected to branch pipe one end, and house steward is connected to the other end, and the compressed gas that produces from air compression device passes through the house steward earlier, then gets into gas appliances from the branch pipe process that corresponds respectively. Therefore, the total flow of the compressed gas transmitted to the plurality of gas utilization equipment by the air compression device can be obtained through the acquisition module arranged at the gas outlet of the main pipe or the air compression device. Specifically, the total flow rate of the compressed gas delivered by the air compressing device in a certain period of time may be obtained, for example, a certain period of time may include 10 minutes, 15 minutes, or 30 minutes, etc.
Further, the step of obtaining a total flow rate of the compressed gas transmitted from the air compressing device to the plurality of gas consuming apparatuses (step S101) includes: the total compressed flow, pressure, temperature and instantaneous flow of the compressed gas are obtained. And calculating the total flow rate of the compressed gas under the standard condition based on an ideal gas state equation.
In this embodiment, the total flow rate of the compressed gas transmitted from the air compressing device to the gas consuming equipment can be converted into the total flow rate under the standard condition, so as to facilitate the reasonable distribution of the total flow rate of the subsequent compressed gas. The ideal gas state equation is: (P1 × Q1)/t1 ═ P × Q)/t. Wherein P1 is the air pressure under standard conditions, equal to about 101.325 kpa; q1 is the total flow rate of compressed gas at standard conditions; t1 is the air temperature at standard conditions, approximately equal to 273.15K; p is the measured pressure, Q is the measured total flow, and t is the measured temperature.
In a practical application, taking the total flow time of the compressed gas delivered by the air compressor within 10 minutes as an example, when the measured total flow is equal to about 19.35m3The measured pressure is equal to about 658kpa and the measured temperature is 298.15k, whereby the total flow of compressed gas under standard conditions is calculated to be equal to about 115.12Nm based on the ideal gas equation of state3
Step S102: and selecting representative gas-using equipment from the plurality of gas-using equipment, and acquiring the average flow of the compressed gas required by the representative gas-using equipment.
In the embodiment, only the meter gas appliances need to be replaced by a plurality of gas appliances, and the average flow of the representative gas appliances is obtained to serve as the average flow of all the gas appliances, which is equivalent to calculating the gas consumption of each gas appliance in the prior art, so that the metering cost can be reduced, the calculation rate can be increased, and the working efficiency can be improved.
The representative gas-using equipment can be one or more than one gas-using equipment. For example, one or more of a plurality of gas consuming apparatuses with a large number of types may be selected as the representative gas consuming apparatus, or one or more of the plurality of gas consuming apparatuses with a power level in a median may be selected as the representative gas consuming apparatus.
The average flow rate may be an average flow rate representing an average flow rate of the compressed gas required by the gas consuming apparatus over a certain period of time, and the average flow rate may be an average flow rate under a standard condition so as to facilitate a reasonable distribution of the total flow rate of the subsequent compressed gas.
Step S103: the method includes the steps of obtaining gas using time of a plurality of gas using equipment, obtaining accumulated flow of each gas using equipment based on the gas using time and average flow, and distributing total flow to each gas using equipment based on the accumulated flow.
The timing module can be independently arranged at each gas-using device, the gas-using time of each gas-using device in a certain time period is detected through the timing module, and then the gas-using time is multiplied by the average flow of each representative gas-using device, so that the accumulated flow of each gas-using device in a certain time period can be obtained.
After each cumulative flow is obtained, the total flow can be reasonably distributed to each gas-using device. Specifically, step S103 may include: and calculating the sum of the accumulated flow of each gas utilization device, respectively calculating the ratio of the accumulated flow of each gas utilization device to the sum of the accumulated flow, and distributing the total flow to each gas utilization device based on the ratio.
After the cumulative flow rate of each gas-using device is obtained, the cumulative flow rates of all the gas-using devices in a certain time period are added to obtain the sum of the flow rates of each gas-using device. And the sum of the accumulated flow rates corresponding to the accumulated flow rates of all the gas utilization equipment in a certain time period is divided by the sum of the corresponding accumulated flow rates, so that the ratio of the accumulated flow rates of each gas utilization equipment to the sum of the accumulated flow rates can be obtained, the sum of each ratio is equal to an integer 1, the ratio of the gas utilization of each gas utilization equipment is multiplied by the total flow rate of the compressed gas, and the total flow rate can be reasonably distributed to each gas utilization equipment based on the ratio.
Therefore, in this embodiment, the accumulated flow of a plurality of gas utilization devices can be obtained only by metering the gas utilization of a representative gas utilization device, so that the metering cost is reduced, and meanwhile, the compressed gas can be distributed based on the accumulated flow, so that the energy consumption index of the compressed gas can be decomposed to production teams, machines and individuals according to the distribution result of the compressed gas, the energy consumption management can be enhanced, and the energy-saving control measures can be taken in time to reduce the waste of the compressed gas.
Referring to fig. 2, fig. 2 is a schematic flowchart of an embodiment of step S103 shown in fig. 1 provided in the present application. As shown in fig. 2, the step of obtaining the average flow rate representing the compressed gas required by the gas-using equipment in step S103 may include the following steps S201 to S203, specifically:
step S201: the ventilation time is obtained from a first preset time period representative of the gas-using equipment.
A timing module may be provided at the representative gas consumer, by which a ventilation time of the representative gas consumer within a first preset time period is detected. In an application scenario, the first predetermined time period may be 10 minutes, and a detection within 10 minutes represents a ventilation time of 120 seconds for the gas-using apparatus.
Step S202: a representative total flow rate representative of the compressed gas taken by the gas-using device over the first predetermined time period is taken.
An acquisition module can be arranged on each pipeline for connecting the representative gas-using equipment, and the representative total flow of the compressed gas acquired in the representative gas-using equipment within the first preset time period is acquired through the acquisition module. Wherein, the representative total flow rate may be a representative total flow rate under a standard condition, specifically, step S202 may include: and acquiring representative total compressed flow, pressure, temperature and instantaneous flow representing the compressed gas required by the gas consumption equipment, and calculating to obtain a representative total flow representing the gas consumption equipment under standard conditions based on an ideal gas state equation.
The ideal gas state equation is: (P1 × Q1)/t1 ═ P × Q)/t. Wherein P1 is the air pressure under standard conditions, equal to about 101.325 kpa; q1 is the total flow rate of compressed gas at standard conditions; t1 is the air temperature at standard conditions, approximately equal to 273.15K; p is the measured pressure, Q is the measured cumulative flow, and t is the measured temperature. A representative total flow rate representative of the gas-using equipment under standard conditions may be obtained based on the actually detected parameters.
Step S203: the representative total flow was divided by the aeration time to obtain the average flow.
In an application scenario, the first predetermined time period may be 10 minutes, a detection within 10 minutes may represent an aeration time of the gas consumer of about 120 seconds, and a representative total flow rate of compressed gas obtained by the gas consumer within the first predetermined time period may represent about 4.5Nm3At this point, it may represent a total flow of 4.5Nm3The average flow rate was about 0.038Nm divided by the aeration time of 120 seconds3/S。
Referring to fig. 3, fig. 3 is a schematic flowchart of an embodiment of step S102 shown in fig. 1 provided in the present application, and as shown in fig. 3, the step of selecting a representative gas-using device from a plurality of gas-using devices in step S102 may include the following steps S301 to S302, specifically:
step S301: the method includes dividing a plurality of gas using equipment into a plurality of gas using categories based on preset conditions.
The preset conditions include the function or power of the gas-using equipment. For example, the gas-using devices can be classified into three major categories, namely, pneumatic control elements, pneumatic actuators and pneumatic auxiliary elements, according to their functions. The power consumption can be classified into high power consumption equipment and low power consumption equipment.
Step S302: and selecting a gas using device from each gas using type as a representative gas using device.
The meter gas-consuming equipment can be replaced from each gas-consuming equipment according to actual conditions, and the representative gas-consuming equipment in each category can be one or more. For example, when the plurality of gas-consuming apparatuses are classified into three types, namely, a pneumatic control element, a pneumatic actuator element, and a pneumatic auxiliary element according to functions, one or more representative gas-consuming apparatuses may be selected from the three types, respectively, and may be used as representative gas-consuming apparatuses of the three types of gas-consuming apparatuses, respectively. Therefore, all the gas consuming equipment are classified, and then the gas consuming equipment is selected from each class of gas consuming equipment to replace the meter gas consuming equipment, so that the obtained average flow rate of the compressed gas required by the representative gas consuming equipment is closer to the average flow rate of the same class of gas consuming equipment, and the result of distributing the total flow rate of the compressed gas to each gas consuming equipment is more accurate.
Further, the step of obtaining the cumulative flow rate of each gas-using device based on the gas-using time and the average flow rate may include: the gas usage time of the same kind of gas-using equipment is multiplied by the average flow rate of the representative gas-using equipment to obtain the cumulative flow rate of each gas-using equipment.
In an application scenario, the gas-using equipment comprises a plurality of gas guns, a plurality of gas cylinders and a plurality of cooling molds, and the total flow of the compressed gas transmitted to the gas-using equipment by the air pressure device is about equal to 115.12Nm3
Selecting one or more representative air guns from the plurality of air guns, detecting that the representative air gun aeration time is about 120 seconds in 10 minutes, and that the representative total flow rate of compressed gas obtained by the representative air gun in 10 minutes is about 4.5Nm3At this point, it may represent a total flow of 4.5Nm3The average flow rate was about 0.038Nm by dividing the gas usage time by 120 seconds3and/S. Wherein, the number of the air guns is 5, and the air using time of the first air gun in 10 minutes is about 150 seconds; the gas using time of the second air gun in 10 minutes is about 130 seconds; the gas using time of the third air gun in 10 minutes is about 125 seconds; the gas using time of the fourth air gun in 10 minutes is about 133 seconds; the gas usage time for the fifth air gun over 10 minutes was about 59 seconds. Thus, the cumulative flow rates of the 5 air guns can be obtained by multiplying the air usage time of each air gun by the average flow rate of the representative air gun, respectively, to obtain a cumulative flow rate of about 5.63Nm3、4.88Nm3、4.69Nm3、4.99Nm3And 2.21Nm3
Selecting one or more representative cylinders from the plurality of cylinders, detecting a representative cylinder ventilation time of about 58 seconds in 10 minutes, and a representative total flow rate of compressed gas taken by the representative cylinders in 10 minutes of about 10.9Nm3At this point, it may represent 10.9Nm of total flow3The average flow rate was about 0.188Nm by dividing the gas usage time by 58 seconds3and/S. Wherein, the number of the plurality of cylinders is 5, and the gas using time of the first cylinder in 10 minutes is about 57 seconds; the gas consumption time of the second cylinder in 10 minutes is about 59 seconds; the gas using time of the third cylinder in 10 minutes is about 57 seconds; fourth oneThe gas using time of the cylinder in 10 minutes is about 57 seconds; the gas usage time for the fifth cylinder in 10 minutes is about 58 seconds. Thus, the cumulative flow rates of 5 cylinders can be obtained by multiplying the gas usage time of each cylinder by the average flow rate of the representative cylinder, respectively, and are about 10.71Nm3、11.09Nm3、10.71Nm3、10.71Nm3And 10.90Nm3
One or more representative cooling molds are selected from the plurality of cooling molds, and it is detected that the representative cooling mold vent time is about 178 seconds in 10 minutes, and that the representative total flow rate of the compressed gas taken in 10 minutes for the representative cooling molds is about 6.3Nm3At this point, it may represent a total flow of 6.3Nm3The average flow rate was about 0.035Nm by dividing by the gas usage time of 178 seconds3and/S. Wherein, the number of the cooling moulds is 5, and the air using time of the first cooling mould in 10 minutes is about 177 seconds; the second cooling mold was used for about 179 seconds in 10 minutes; the air time for the third cooling mold within 10 minutes is about 178 seconds; the air time for the fourth cooling mold within 10 minutes was about 177 seconds; the air time for the fifth cooling mold within 10 minutes was about 179 seconds. Thus, the cumulative flow rates of 5 cooling molds each having a cumulative flow rate of about 6.26Nm can be obtained by multiplying the air usage time per cooling mold by the average flow rate representing the cooling mold3、6.34Nm3、6.30Nm3、6.26Nm3And 6.34Nm3
Wherein, the sum of the cumulative flow rates of 5 cooling dies and 5 air guns and 5 air cylinders can be obtained by adding the cumulative flow rates of 5 air guns, and the sum of the cumulative flow rates of each air appliance is about 108.1Nm3. The cumulative flow rate per gas-using equipment is divided by 108.1Nm3Obtaining the ratio of each gas utilization device, and multiplying the ratio of each gas utilization device by the total flow 115.12Nm transmitted by the air compression device3To obtain respectively 5 air guns distributing about 6.00Nm of flow3、5.20Nm3、5.00Nm3、5.32Nm3And 2.36Nm3(ii) a The flow rates distributed by the 5 cylinders are about 11.42Nm respectively3、11.82Nm3、11.42Nm3、11.42Nm3And 11.62Nm3(ii) a The flow rates allocated to the 5 cooling dies were about 6.68Nm each3、5.75Nm3、6.71Nm3、6.68Nm3And 6.75Nm3
Therefore, in this embodiment, the gas-using equipment can be classified first, then representative gas-using equipment is selected from different classes, and only by detecting the gas metering of the representative gas-using equipment, the accumulated flow rates of a plurality of gas-using equipment are obtained, so that the accuracy of the obtained accumulated flow rates of the plurality of gas-using equipment is improved. Meanwhile, the compressed gas can be distributed based on the accumulated flow, so that the energy consumption index of the compressed gas can be decomposed to production teams, machines and individuals according to the distribution result of the compressed gas, the energy consumption management can be enhanced, and the energy-saving control measures can be taken in time to reduce the waste of the compressed gas.
Referring to fig. 4, fig. 4 is a schematic structural view of an embodiment of the compressed gas distribution system provided herein.
The application also provides a compressed gas distribution system 10, which comprises a plurality of gas-using apparatuses 200, an air compressing device 100 and a control device 300, wherein the air compressing device 100 is used for generating compressed gas, and the control device 300 is used for controlling the compressed gas distribution system to realize the compressed gas distribution method of any of the above embodiments.
The air compressing device 100 is connected with the plurality of gas-using devices 200 through a pipeline, and after the air compressing device 100 generates compressed gas, the compressed gas is transmitted to the gas-using devices 200 which need to use the compressed gas through the pipeline. The air compressing device 100 may be an air compressor in an air compressing station, and the air compressor absorbs air and forms compressed air meeting the use condition after being processed. The gas may include air or other gas that meets the actual use conditions. The gas-using device 200 includes a solenoid valve, a fluid control valve, a gas cylinder, a quick coupling, a pneumatic screw driver, etc., and any device that uses compressed gas during operation may be referred to as the gas-using device 200.
The control device 300 is used for collecting and processing data related to the air compressing device 100 and the gas using equipment 200, and can control the air compressing device 100 to distribute compressed gas to the gas using equipment 200.
Referring to fig. 5, fig. 5 is a schematic structural diagram of an embodiment of a control device 300 provided in the present application. The control device 300 may include a first acquisition module 310, a second acquisition module 320, a third acquisition module 330, and a data processing device 340.
The first collecting module 310 is used for acquiring a total flow rate of the compressed gas transmitted from the air compressing device 100 to the plurality of gas consuming apparatuses 200. Specifically, the first collecting module 310 may include a first digital flow meter and a first communication module, the first communication module is configured to establish a communication connection with the data processing device 340, the first digital flow meter may be disposed at a main pipe of the air compressing device 100 or an air outlet of the air compressing device 100, and the measured total flow, the measured pressure, and the measured temperature of the compressed gas transmitted from the air compressing device 100 to the gas using equipment 200 are obtained through the first digital flow meter, and are transmitted to the data processing device 340 through the first communication module.
The second collecting module 320 is used for obtaining an average flow rate representing the compressed gas required by the gas-using equipment. Specifically, the second collection module may include a second digital flow meter and a second communication module, the second communication module is configured to establish a communication connection with the data processing device 340, the second digital flow meter may be disposed at a pipeline or a gas inlet of a representative gas appliance, the second digital flow meter obtains a measured total flow, a measured pressure, and a measured temperature of compressed gas transmitted from the air compressing device 100 to the representative gas appliance, and transmits the measured total flow, the measured pressure, and the measured temperature to the data processing device 340 through the wireless communication module.
The third collecting module 330 is used for acquiring the gas usage times of a plurality of gas-using apparatuses 200. The third collecting module 330 includes a timing module and a third communication module, the third communication module is used for establishing communication connection with the data processing device 340, the timing module may be disposed at a pipeline or a gas inlet of each gas appliance 200, acquires gas usage time of the gas appliance through the timing module, and transmits the gas usage time to the data processing device 340 through the wireless communication module.
The data processing device 340 is used for receiving and processing the data acquired by the first acquisition module 310, the second acquisition module 320 and the third acquisition module 330.
The data processing device 340 may include a server or a mobile terminal, and may further include a system in which the server and the mobile terminal cooperate with each other, and further, the server may be hardware or software. When the server is hardware, it may be implemented as a distributed server cluster formed by multiple servers, or may be implemented as a single server. When the server is software, it may be implemented as a plurality of software or software modules, for example, software or software modules for providing distributed servers, or as a single software or software module, and is not limited herein.
Specifically, the data processing device 340 is configured to receive the measured total flow, the measured pressure, and the measured temperature of the compressed gas obtained by the first acquisition module 310, and convert the measured total flow, the measured pressure, and the measured temperature into a total flow under a standard condition; the data processing device 340 is further configured to receive the measured total flow, the measured pressure, and the measured temperature of the compressed gas transmitted by the air compressing device 100 to the representative gas-using equipment, acquired by the second acquisition module 320, convert the measured total flow, the measured pressure, and the measured temperature into a representative total flow under a standard condition, and calculate an average flow of the representative gas-using equipment; the data processing device 340 is further configured to receive the gas using time of the gas using equipment 200 acquired by the third acquisition module 330, calculate an accumulated flow rate of each gas using equipment 200, and distribute the total flow rate transmitted by the air compressing device 100 to each gas using equipment 200 based on the accumulated flow rate.
Therefore, in the present embodiment, by selecting the representative gas-using equipment, the cumulative flow rates of the plurality of gas-using equipment 200 can be obtained only by detecting the gas metering of the representative gas-using equipment, and the production cost can be reduced. Meanwhile, the compressed gas can be distributed based on the accumulated flow, so that the energy consumption index of the compressed gas can be decomposed to production teams, machines and individuals, the energy consumption index of the compressed gas of a unit product can be conveniently aligned, the energy consumption management can be enhanced, and the energy-saving control measures can be taken in time to reduce the waste of the compressed gas.
In addition, if the above functions are implemented in the form of software functions and sold or used as a standalone product, the functions may be stored in a storage medium readable by a mobile terminal, that is, the present application also provides a storage device storing program data, which can be executed to implement the method of the above embodiments, the storage device may be, for example, a usb disk, an optical disk, a server, etc. That is, the present application may be embodied as a software product, which includes several instructions for causing an intelligent terminal to perform all or part of the steps of the methods described in the embodiments.
In the description of the present application, reference to the description of the terms "one embodiment," "some embodiments," "an example," "a specific example," or "some examples," etc., means that a particular feature, structure, material, or characteristic described in connection with the embodiment or example is included in at least one embodiment or example of the present application. In this specification, the schematic representations of the terms used above are not necessarily intended to refer to the same embodiment or example. Furthermore, the particular features, structures, materials, or characteristics described may be combined in any suitable manner in any one or more embodiments or examples. Furthermore, various embodiments or examples and features of different embodiments or examples described in this specification can be combined and combined by one skilled in the art without contradiction.
Furthermore, the terms "first", "second" and "first" are used for descriptive purposes only and are not to be construed as indicating or implying relative importance or implicitly indicating the number of technical features indicated. Thus, a feature defined as "first" or "second" may explicitly or implicitly include at least one such feature. In the description of the present application, "plurality" means at least two, e.g., two, three, etc., unless specifically limited otherwise.
Any process or method descriptions in flow charts or otherwise described herein may be understood as representing modules, segments, or portions of code which include one or more executable instructions for implementing specific logical functions or steps of the process, and the scope of the preferred embodiments of the present application includes other implementations in which functions may be executed out of order from that shown or discussed, including substantially concurrently or in reverse order, depending on the functionality involved, as would be understood by those reasonably skilled in the art of the present application.
The logic and/or steps represented in the flowcharts or otherwise described herein, such as an ordered listing of executable instructions that can be viewed as implementing logical functions, can be embodied in any computer-readable medium for use by or in connection with an instruction execution system, apparatus, or device (e.g., a personal computer, server, network device, or other system that can fetch the instructions from the instruction execution system, apparatus, or device and execute the instructions). For the purposes of this description, a "computer-readable medium" can be any means that can contain, store, communicate, propagate, or transport the program for use by or in connection with the instruction execution system, apparatus, or device. More specific examples (a non-exhaustive list) of the computer-readable medium would include the following: an electrical connection (electronic device) having one or more wires, a portable computer diskette (magnetic device), a Random Access Memory (RAM), a read-only memory (ROM), an erasable programmable read-only memory (EPROM or flash memory), an optical fiber device, and a portable compact disc read-only memory (CDROM). Additionally, the computer-readable medium could even be paper or another suitable medium upon which the program is printed, as the program can be electronically captured, via for instance optical scanning of the paper or other medium, then compiled, interpreted or otherwise processed in a suitable manner if necessary, and then stored in a computer memory.
The above description is only for the purpose of illustrating embodiments of the present application and is not intended to limit the scope of the present application, and all modifications of equivalent structures and equivalent processes, which are made by the contents of the specification and the drawings of the present application or are directly or indirectly applied to other related technical fields, are also included in the scope of the present application.

Claims (10)

1. A compressed gas distribution method for use in a compressed gas distribution system including a plurality of gas-using devices and an air compressor for generating a compressed gas, the distribution method comprising:
acquiring the total flow of the compressed gas transmitted to the plurality of gas-using equipment by the air compression device;
selecting representative gas-using equipment from the plurality of gas-using equipment, and acquiring the average flow of compressed gas required by the representative gas-using equipment;
the method comprises the steps of obtaining gas using time of the plurality of gas using equipment, obtaining accumulated flow of each gas using equipment based on the gas using time and the average flow, and distributing the total flow to each gas using equipment based on the accumulated flow.
2. The compressed gas distribution method of claim 1, wherein the step of selecting a representative gas consumer from the plurality of gas consumers comprises:
dividing the plurality of gas-using equipment into a plurality of gas-using types based on preset conditions;
and selecting the gas-using equipment from each gas-using type as the representative gas-using equipment.
3. The compressed gas distribution method according to claim 1 or 2, wherein said step of obtaining said average flow rate representative of the compressed gas required by the gas-using equipment comprises:
acquiring a ventilation time from the first preset time period representing the gas-using equipment;
obtaining a representative total flow rate of compressed gas obtained by the representative gas-using equipment in the first preset time period;
dividing said representative total flow by said aeration time to obtain said average flow.
4. The compressed gas distribution method of claim 1 or 2, wherein the step of distributing the total flow rate to each of the gas-using devices based on the accumulated flow rate comprises:
calculating the sum of the accumulated flow of each gas-using device;
respectively calculating the ratio of the accumulated flow of each gas-using device to the sum of the accumulated flows;
distributing the total flow to each of the gas-using devices based on the fraction.
5. The compressed gas distribution method of claim 2, wherein the step of deriving the cumulative flow rate for each of the gas-using devices based on the gas-using time and the average flow rate comprises:
multiplying the gas usage time of the gas-using devices of the same kind by the average flow rate of the representative gas-using device to obtain a cumulative flow rate of each of the gas-using devices.
6. The compressed gas distribution method of claim 1, wherein the step of obtaining a total flow rate of compressed gas delivered by the air compressor to the plurality of gas consuming devices comprises:
acquiring the total compression flow, pressure and temperature of the compressed gas;
calculating the total flow rate of the compressed gas under the standard condition based on an ideal gas state equation.
7. The compressed gas distribution method of claim 3, wherein said step of obtaining a representative total flow rate of compressed gas obtained by said representative gas-using device during said first predetermined time period comprises:
acquiring representative total compressed flow, pressure and temperature of the compressed gas required by the representative gas-using equipment;
and calculating the representative total flow of the representative gas-using equipment under the standard condition based on an ideal gas state equation.
8. The compressed gas distribution method according to claim 2, wherein the preset condition comprises a function or power of the gas-using equipment.
9. A compressed gas distribution system comprising a plurality of gas consuming appliances, a pneumatic device for generating compressed gas, and a control device for controlling the compressed gas distribution system to carry out the compressed gas distribution method of any one of claims 1 to 8.
10. The compressed gas distribution system of claim 9, wherein the control device comprises:
the first acquisition module is used for acquiring the total flow of the compressed gas transmitted to the plurality of gas-using equipment by the air compression device;
the second acquisition module is used for acquiring the average flow of the compressed gas required by the representative gas using equipment;
the third acquisition module is used for acquiring the gas using time of the plurality of gas using equipment;
and the data processing device is used for receiving and processing the data acquired by the first acquisition module, the second acquisition module and the third acquisition module.
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