Study on Flow Characteristics and Mass Transfer Mechanism of Kettle Taylor Flow Reactor

Ye, Li; Wan, Tengfei; Xie, Xiaohui; H, Lin

doi:10.3390/en15062028

Cited by 4 publications

(2 citation statements)

References 22 publications

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“…There are many types of kettle reactors in the chemical industry, and their structure and appearance are not uniform. Based on the phase differences of the reaction materials, they can be divided into homogeneous reactors and heterogeneous reactors [24]. The more common ones are solid-liquid, liquid-liquid, gas-liquid reactors, and gas-liquid-solid three-phase reactors.…”

Section: Introductionmentioning

confidence: 99%

The Law of Gas–Liquid Shear Mixing under the Synergistic Effect of Jet Stirring

Zhou,

Wang,

Wang

et al. 2023

Processes

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At present, there is a common problem that the mixing mode is single and it is difficult to overcome the inherent bottleneck of multiphase mixing. A mixing device combining the advantages of jet entrainment and mixing dispersion was designed and built. In an effort to determine the mixing degree of two phases, the mixing coefficient of gas–liquid charging was measured using the cylinder method with the optimal working parameters. To explore the optimization of the mixing conditions and control mechanism of multiphase materials, the law of gas–liquid shear mixing in the process of multi-force field synergistic change was revealed. Based on the testing of the gas injection capacity under different working conditions and the calculation of the gas–liquid two-phase mixing coefficient, it was concluded that the flow rate was the direct key factor affecting the gas injection capacity. The working speed also had a certain impact on the gas injection capacity. When working at a high speed and high flow rate, the jet beam broke through the cutting barrier and presented a superposition effect. The jet impact assisted the rotation, and the suction performance of the device was significantly improved, which was conducive to the mixing of the gas and liquid phases. According to the test results of the measuring cylinder method, the calculated average inflation volume is 0.01 m3/(m2·min), the inflation uniformity coefficient is 77.51, and the mixing coefficient of the gas and liquid phases is 0.12.

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Section: Introductionmentioning

confidence: 99%

The Law of Gas–Liquid Shear Mixing under the Synergistic Effect of Jet Stirring

Zhou,

Wang,

Wang

et al. 2023

Processes

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“…Two-phase flow exists in many important industrial and engineering systems such as two-phase flow reactors, centrifugal extractor etc., e.g. [15,16], and heat-mass transfer and power generating systems of all scale, e.g. [17].…”

Section: Introductionmentioning

confidence: 99%

Multiwave Ultrasonic Doppler Method for Bubbly Two-Phase Taylor Couette Flow Measurement

Thắng¹

2022

IJHT

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Ultrasonic methods, such as the Ultrasonic Velocity Profile - UVP method, have a number of advantages over other conventional measurement methods. They are non-intrusive, applicable to opaque wall or fluid, and capable of obtaining instantaneous velocity profiles along a measurement line in real time. This paper reports on the development of a multiwave Doppler UVP method for the measurement of bubbly two-phase flow in a Taylor-Couette flow configuration. Due to its highly complex nature, two-phase flow still attracts considerable interest in both experimental measurement as well as numerical simulation. In this study the new multiwave Doppler UVP method exploits two basic ultrasonic frequencies 2 MHz and 8 MHz. The 2 MHz frequency is for the measurement of the bubble phase. The 8 MHz frequency is for that of the liquid phase. The signal processing technique is based on the pulse repetition Doppler method. A new phase discrimination method is proposed to eliminate bubble velocity included in the data of the liquid phase measured by the 8 MHz frequency. Measurements of bubbly two-phase Taylor-Couette flow have been demonstrated and discussed.

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