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Gas-liquid bubbly flow structure in a vertical large-diameter square duct

鉛直大口径正方形管における気液二相気泡流の流動構造

Shen, X.*; 孫 昊旻; Deng, B.*; 日引 俊*; 中村 秀夫

Shen, X.*; Sun, Haomin; Deng, B.*; Hibiki, Takashi*; Nakamura, Hideo

4センサープローブを用いて、鉛直大口径正方形管内の上昇気液二相流の局所構造を計測した。球形と非球形気泡を区別する4センサープローブの計測手法を適用し、局所3次元気泡速度ベクトル、気泡径と界面積濃度を計測した。液相流量が低い時と高い時、局所ボイド率と界面積濃度はそれぞれ中心ピークと壁ピークの分布を示した。断面内における横方向気泡速度は、断面の対称的な8分の1三角領域内を循環する2次流れの存在を示し、その大きさは液相速度の上昇とともに増加した。本データに対して、既存ドリフトフラックスモデルや界面積濃度の相関式の比較を行い、適応性を検証した。

An experimental study was performed on the local structure of upward air-water two-phase flow in a vertical large diameter square duct by using a four-sensor probe. The four-sensor probe method classifying spherical and non-spherical bubbles was applied as a key measurement way to obtain local parameters such as 3-D bubble velocity vector, bubble diameter and interfacial area concentration. Both the local void fraction and interfacial area concentration indicated radial core-peak and wall-peak distributions at low and high liquid flow rates respectively. The 2 components of the bubble velocity vector in the cross-section revealed that there exists a rotating secondary flow in the octant symmetric triangular area and the magnitude of the rotating secondary flow increases with the liquid flow rate. Some of constitutive correlations of drift-flux model and interfacial area concentration are reviewed to study their predictabilities against the present data.

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パーセンタイル:17.95

分野:Nuclear Science & Technology

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