Haobai Xue

Dr. Haobai Xue

Tsinghua University
orcid

Research Focus & Metrics

Academic Career Length

13Years (2014-Present)

(Calculated once Scilit publication data is synced: current year − year of first publication + 1)

Representative Publications

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1 September 2014 in Energy Conversion and Management
Verified
Journal Article
Closed access
XZXinjing Zhang
Xinjing Zhang
HXHaobai Xue
Haobai Xue
YXYujie Xu
Yujie Xu
HCHaisheng Chen
Haisheng Chen
CTChunqing Tan
Chunqing Tan

12 April 2021 in Sensors
Verified
Journal Article
Open access
PDF file
HXHaobai Xue
Haobai Xue
MZMaomao Zhang
Maomao Zhang
PYPeining Yu
Peining Yu
HZHaifeng Zhang
Haifeng Zhang
GWGuozhu Wu
Guozhu Wu
XZXiang Yuan Zheng
Xiang Yuan Zheng
During the research and development of multiphase flowmeters, errors are often used to evaluate the advantages and disadvantages of different devices and algorithms, whilst an in-depth uncertainty analysis is seldom carried out. However, limited information is sometimes revealed from the errors, especially when the test data are scant, and this makes an in-depth comparison of different algorithms impossible. In response to this problem, three combinations of sensing methods are implemented, which are the “capacitance and cross-correlation”, the “cross-correlation and differential pressure” and the “differential pressure and capacitance” respectively. The analytical expressions of the gas/liquid flowrate and the associated standard uncertainty have been derived, and Monte Carlo simulations are carried out to determine the desired probability density function. The results obtained through these two approaches are basically the same. Thereafter, the sources of uncertainty for each combination are traced and their respective variations with flowrates are analyzed. Further, the relationship between errors and uncertainty is studied, which demonstrates that the two uncertainty analysis approaches can be a powerful tool for error prediction. Finally, a novel multi-sensor fusion algorithm based on the uncertainty analysis is proposed. This algorithm can minimize the standard uncertainty over the whole flowrate range and thus reduces the measurement error.

17 March 2021 in Sensors
Verified
Journal Article
Open access
PDF file
HXHaobai Xue
Haobai Xue
PYPeining Yu
Peining Yu
MZMaomao Zhang
Maomao Zhang
HZHaifeng Zhang
Haifeng Zhang
EWEncheng Wang
Encheng Wang
XZXiang Yuan Zheng
Xiang Yuan Zheng
Although the use of a classical Venturi tube for wet gas metering has been extensively studied in the literature, the use of an extended-throat Venturi (ETV) tube has rarely been reported since its first proposal by J. R. Fincke in 1999. The structure of an ETV is very simple, but due to the complexity of multiphase flow, its theoretical model has not been fully established yet. Therefore, in this paper theoretical models have been developed for the convergent and throat sections of an ETV, and the gradients of front and rear differential pressures are derived analytically. Several flowrate algorithms have been proposed and compared with the existing ones. Among them, the iteration algorithm is found to be the best. A reasonable explanation is provided for its performance. The relationship between the differential pressure gradient and the flowrate relative error is also studied, such that the relative error distributions varying with ETV measured flowrates can be derived. The gas flowrate error of ETV increases with the liquid content whilst the liquid flowrate error of ETV decreases with the liquid content, and the relative errors of liquid flowrate are generally 2 to 3 times larger than that of the gas flowrate. Finally, the ETV tends to be more accurate than the classical Venturi tube. The ETV can be designed more compact under the same signal intensity due to its significantly higher velocity in the throat section.