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Analysis of the factors causing pressure difference instability at the pressure tapping ports of annular chamber orifice flowmeters and corresponding countermeasures

2018-04-11View Original

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Abstract: Annular orifice plate flowmeters play a significant role in industrial applications, especially for accurate measurement of gas flow. It is common for there to be no pressure difference at the pressure tapping ports during use. In light of these issues, Shanghai Automation Instrument Co., Ltd. shares some of its views and suggestions. As orifice plates are used for extended periods of time, factors such as the presence of solid particles in the fluid being measured or chemical corrosion can cause changes in the geometric shape and dimensions of the orifice plate. If the sharpness of the inlet edge of the orifice plate is reduced due to impact from the fluid or corrosion, the pressure difference generated when an equal volume of fluid passes through decreases, resulting in lower measurement values. In severe cases, the orifice plate needs to be replaced. In practical use, a layer of dirt may accumulate on the surface of the orifice plate; over time, impurities can deposit in the corners ahead of and behind the orifice plate, and severe corrosion can also cause a gradual change in the flow cross-sectional area of the pipeline. Additionally, leaks and blockages in the pressure tapping lines can all lead to measurement errors. Since some manufacturers use gas that is relatively dirty (containing tar), this caused the pressure-taking chambers before and after the orifice plate to become blocked, resulting in no pressure difference at the pressure-taking ports and no flow reading on the flow meter. After removing the components, cleaning the two chambers and replacing the pressure conduits, the flow meter began to display normal readings. Due to the passage of time, the zero point of the transmitter may drift. If there is a negative drift, the output current of the transmitter will be less than the standard 4 mA, resulting in a lower flow rate reading; if there is a positive drift, the output current of the transmitter will be greater than the standard 4 mA, leading to a higher flow rate reading. If the range setting is high, the flow rate will be displayed as low; if the range setting is low, the flow rate will be displayed as high. During the initial commissioning and testing, the gas flow meter showed a low reading; upon inspection, it was found that the orifice plate was installed in the wrong direction. In fact, the sharp side of the orifice plate should face the flow direction and serve as the inlet, while the flared side should be the outlet – pay attention to the direction. In addition, during installation, orifice plate flow meters… Therefore, in practical use, there are many factors that affect the accuracy of ring chamber orifice plate flow meters, with the main influencing factors coming from the following four aspects. It can be seen that if density uncertainty and differential pressure are equally important, the accuracy is not high; in the case of high differential pressure measurements, for example, the accuracy of the measurement results is a fact that is often overlooked. More specifically, for a gas flow measured by an orifice flow meter and based on gas density, the flow density is a constant that is inversely proportional to the square root of other parameters; the greater these parameters, the smaller the flow density. Yes. In practice, for orifice flow meters, the density of the gas is involved; hence a fixed value of ρ0 is required. However, whether it is a large-orifice or a small-orifice flow meter, the flow rate is related to the actual density of the natural gas, but only through ρ0. For coal whose flow rate is determined by a single gas source, as long as there is even a slight effect, it integrates into larger changes; rather than eliminating the stability within a basically constant temperature range, the gas composition and density of the system pressure remain unchanged. However, due to changes over time, such as variations in composition, and mixing with the gas components of other sources such as water gas, producer gas, and liquefied petroleum gas, the actual figures will change. Using an annular orifice flow meter for the gas density, however, significant measurement errors will occur in the value ρ0. Recognize the severity of the error. During the purification of artificial gas, the gas becomes saturated through ordinary water washing. The flow rate of the process gas, pressure, changes in the steam condensation temperature at the inlet and outlet areas before and after the straight sections of pipe, as well as the water film thickness – these are the exact requirements for using orifice plate flow meters. It is not allowed; this is a serious mistake, and measurements will be affected as a result. In addition, saturated water vapor and gases are measured, along with the gas flow rate via a flow meter. The difference caused by a decrease in gas volume affects the transfer and distribution of intermediate temperatures, as well as gas tanks, pipelines, and boosters; however, this aspect is not included in natural gas sales, nor is it related to water vapor condensation at any time. Deposition gradually adsorbs impurities such as Hall; the holes upstream of the pipeline become clogged with tar. Orifice flow meters use fly ash, naphthalene, gas, natural gas, and adhesives at the inlet of the flow measurement device, and the surface finish leads to a reduction in the inner diameter. As a result, the roughness value measured upstream of the pipeline is also higher. Automatic drainage, as well as manual drainage methods, actually yield very good results. During winter, water supply and drainage should be carried out at scheduled times for each category; the drainage must comply with the requirements of other seasons on a daily basis. Please check the sealed drainage system. Vortex flowmeters with spiral inlet were installed at the first natural gas processing plant to meet relevant quality standards; gas purification was enhanced, pollution was reduced, the flowmeters were cleaned, and impurities in the orifices and straight sections were removed on a regular basis. The top line of (1); you can change the mouth shape to be used for:. Parallel to tube (2). Stopping the convenience of natural gas makes it difficult to clean, cut, or reduce gas exchange; these functions do not cease, and it is possible to perform cleaning on the system’s orifice plate flow meters. To implement a supplementary measure, it is necessary to regularly check the accuracy of the checksums and secondary instruments; the specific procedures are as follows. (1) Leaks in pipes, fittings, valves, welding areas, as well as water leakage – potential leak points in these areas need to be addressed carefully. Special attention should be paid to issues related to soap usage, pressure differences, and pipe blockages. It is necessary to check the pressure differential transmitters, which are used to maintain balance between high and low pressures. Additionally, leak detection is related to other applications as well as pressure differential measurements; therefore, it is important to take measures to prevent errors in the valves and to minimize the impact on measurement accuracy. Zero differential pressure transmitter calibration (2) can reduce the impact of zero drift. Within this range, aside from the differential pressure transmitter (3), other auxiliary tools, including simulations of the entire production line, make use of high-precision differential pressure gauges to ensure compliance with this range. Conclusion: As a precision instrument, it is inevitable to encounter some minor issues during use; however, such problems can be prevented by carrying out regular maintenance and cleaning of the orifice plate flow meter. Any abnormalities should be addressed promptly through thorough investigation.

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