Abstract

Transient flow in pipe is a much debated topic in the field of hydrodynamics. The water hammer effect caused by instantaneous valve closing is an important branch of transient flow. At present, the fluid density is regarded as a constant in the study of the water hammer effect in pipe. When there is gas in the pipe, the variation range of density is large, and the pressure-wave velocity should also change continuously along the pipe. This study considers the interaction between pipeline fluid motion and water hammer wave propagation based on the essence of water hammer, with the pressure, velocity, density and overflow area set as variables. A new set of water hammer calculation equations was deduced and solved numerically. The effects of different valve closing time, flow rate and gas content on pressure distribution and the water hammer effect were studied. It was found that with the increase in valve closing time, the maximum fluctuating pressure at the pipe end decreased, and the time of peak value also lagged behind. When the valve closing time increased from 5 s to 25 s, the difference in water hammer pressure was 0.72 MPa, and the difference in velocity fluctuation amplitude was 0.076 m/s. The findings confirm: the greater the flow, the greater the pressure change at the pipe end; the faster the speed change, the more obvious the water hammer effect. High-volume flows were greatly disturbed by instantaneous obstacles such as valve closing. With the increase of time, the pressure fluctuation gradually attenuated along the pipe length. The place with the greatest water hammer effect was near the valve. Under the coupling effect of time and tube length, the shorter the time and the shorter the tube length, the more obvious the pressure fluctuation. Findings also confirm: the larger the gas content, the smaller the fluctuation peak of pipe end pressure; the longer the water hammer cycle, the smaller the pressure-wave velocity. The actual pressure fluctuation value was obviously lower than that without gas, and the size of the pressure wave mainly depended on the gas content. When the gas content increased from 1% to 9%, the difference of water hammer pressure was 0.41 MPa.

Highlights

  • Since the mid nineteenth century, the unsteady flow of fluid has been a much discussed topic for scholars

  • Based on the essence of water hammer, the interaction between pipeline fluid motion and water hammer wave propagation is considered in this paper, and the pressure, velocity, density and overflow area 4 of are set as variables

  • The red is the calculation result of the literature, and the blue is the calculation result of the article is the calculation result of the literature, and the blue is the calculation result of the article model. It can be seen from the figure that there are certain deviations in the results, which model. It can be seen from the figure that there are certain deviations in the results, which may be caused by different mathematical models since the model in this paper considers may be caused by different mathematical models since the model in this paper considers the four variables of pressure, flow rate, density and flow area

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Summary

Introduction

Since the mid nineteenth century, the unsteady flow of fluid has been a much discussed topic for scholars. First used the wave characteristic cally solve the water hammer equation and studied pressure fluctuations by changing the line method to numerically simulate the transient in a[14]. Based on the essence of water hammer, the interaction between pipeline fluid motion and water hammer wave propagation is considered in this paper, and the pressure, velocity, density and overflow area 4 of are set as variables. The effects of different valve closing time, flow rate and gas content on pressure distribution and water hammer effect are studied. Such calculations of the water hammer, the interaction between pipeline fluid motion and water hammer wave propagation process of the water hammer wave are more reasonable and reliable. At the beginning of dt, the momentum of the liquid in the 1-2 flow section is:

A v v
Fluid Continuity Equation
Complete Equations of Water Hammer
Difference Equation
Boundary Conditions
Sample Pipeline Foundation Parameters
Discussion
Result andvalue
Difference
12. Influence fluctuation at at thethe end of aofpipeline
Findings
Conclusions
Full Text
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