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气道中黏液通过气液两相流机制的输送:连续流模型

Mucus transport in the airways by two-phase gas-liquid flow mechanism: continuous flow model.

作者信息

Kim C S, Greene M A, Sankaran S, Sackner M A

出版信息

J Appl Physiol (1985). 1986 Mar;60(3):908-17. doi: 10.1152/jappl.1986.60.3.908.

Abstract

Mucus transport speed induced by two-phase gas-liquid interaction was measured in the continuous two-phase annular flow tube models, and factors influencing the transport speed were assessed in conjunction with rheological properties of mucus. The flow model was made with 1.0-cm-ID glass tubes and positioned either vertically or horizontally. During a continuous passage of airflow through the model tube, mucus stimulants were supplied into the tube at a rate of 0.5-2.0 ml/min. The advancing speed of the leading edge of the mucous layer and mean mucous layer thickness were then measured. The transport speed in the vertical tube model ranged from 1.1 to 3.1 cm/min with a mucus feed rate of 0.5 ml/min at airflow rates of 0.33-1.17 l/s and increased with increasing airflow rates but decreased rapidly with increasing viscosity of mucus. The transport speed increased almost proportionally with increasing mucus feed rate. Elasticity of mucus did not affect the transport speed itself. However, more elastic mucus caused lower flow resistance and thereby could be transported with a much reduced work load. The transport speed in the horizontal tube model was 5-60% faster than that in the vertical tube model. The mean mucous layer thickness in the vertical tube model was found to be in the range of 0.5-1.5 mm in the experimental conditions used, and decreased rapidly with increasing airflow rate and decreasing viscosity of mucus. From these data the transport speed could be functionally related to airway diameter, mucous layer thickness, and mucus production rate.

摘要

在连续两相环形流管模型中测量了气液两相相互作用引起的黏液传输速度,并结合黏液的流变学特性评估了影响传输速度的因素。流动模型由内径为1.0厘米的玻璃管制成,垂直或水平放置。在气流连续通过模型管的过程中,以0.5 - 2.0毫升/分钟的速率向管内供应黏液刺激物。然后测量黏液层前缘的推进速度和平均黏液层厚度。在垂直管模型中,当气流速率为0.33 - 1.17升/秒且黏液进料速率为0.5毫升/分钟时,传输速度范围为1.1至3.1厘米/分钟,且随着气流速率的增加而增加,但随着黏液黏度的增加而迅速降低。传输速度几乎与黏液进料速率的增加成比例增加。黏液的弹性本身并不影响传输速度。然而,弹性更大的黏液导致更低的流动阻力,从而可以在工作量大幅减少的情况下进行传输。水平管模型中的传输速度比垂直管模型中的快5 - 60%。在所使用的实验条件下,垂直管模型中的平均黏液层厚度在0.5 - 1.5毫米范围内,并且随着气流速率的增加和黏液黏度的降低而迅速减小。根据这些数据,传输速度可能与气道直径、黏液层厚度和黏液产生速率在功能上相关。

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