Analysis of the relationship between compressed air flow and pressure (Enterprise Edition)

1. Overview of core relationships

compressed airflow(Volume per unit time) andpressure(Pressure) are the two core parameters of system design, and the two pass throughPrinciples of gas dynamicsInterrelated, but not simply linear. The following is explained from three aspects: principle, influence factors and practical application:

2. Theoretical relationships and influencing factors

1. Basic principles of physics

• Energy Conservation Perspective：
  When compressed air flows in pipes, pressure energy is converted into kinetic energy. Simplified model according to Bernoulli equation:

P+21​ρv2=constant

Among them,P For pressure,ρ For the air density,v is the flow rate.
conclusion: In an ideal frictionless pipe, increasing flow rate causes pressure to decrease, and vice versa.

• Actual system corrections：
  There is frictional resistance in actual pipes (Darcy’s formula):

ΔP=f⋅DL​⋅2ρv2​

Among them,f is the coefficient of friction,L is the length of the pipe,D is the diameter.
conclusion: The longer and smaller the diameter of the pipe, the greater the pressure loss, and the initial pressure needs to be increased to maintain flow.

2. Key influencing factors

3. Practical application and optimization strategies

1. system design principles

• Traffic needs prioritize：
  Determine the total air demand (m³/min) of end equipment (such as cylinders, nozzles) as the basis for selecting compressor displacement.
  example: Each of 10 equipment requires 0.2m³/min, and the total air demand is =2.0m³/min (select a 3.0m³/min model after considering the margin).

• Pressure matching logic：
  Calculate the initial pressure based on the pressure loss of the longest pipe:

Pinitial​=Pend​+ΔPpipeline​+ΔPlocal​

example: End needs 0.6MPa, pipe loss 0.1MPa, valve loss 0.05MPa → initial pressure needs ≥0.75MPa.

2. Operation optimization recommendations

• Pressure and flow balance adjustment：

  • If the flow is insufficient: Priority should be given to checking whether the pipe is blocked and whether the valve is fully open, rather than blindly increasing the pressure.
  • If the pressure is too high: Use a pressure regulating valve to reduce the end pressure and reduce the compressor energy consumption (for every 0.1MPa decrease in pressure, the energy is saved by about 7%).

• Gas storage tank configuration：
  The volume of the air storage tank (m³) must meet the pulse gas demand:

Vstorage​≥ΔPallow​Qpulse​×tpulse​​

example: The pulse flow rate of the sandblasting machine is 5m³/min, the duration is 10 seconds, and the pressure fluctuation is allowed to be 0.1MPa → the volume of the air tank is ≥0.83m³.

3. Energy saving design direction

• frequency conversion control：
  Use a variable frequency compressor to adjust the speed according to real-time flow requirements to avoid no-load operation (no-load energy consumption accounts for 15%-30%).

• pipe network optimization：

  • Shorten the length of the pipe and reduce the number of elbows.
  • The diameter of the main pipe is designed according to the maximum flow rate, and the branch pipes are gradually reduced according to the end demand.

IV. Summary

The flow and pressure of compressed air need to pass throughsystem designwithdynamic adjustmentAchieve balance. Enterprises can optimize pipeline layout and equipment selection through theoretical calculations (such as Bernoulli equations and Darcy equations) combined with actual measurement and verification (flowmeter monitoring), and ultimately reduce energy consumption while meeting production needs.