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    Measurements of Airway Dimensions and Calculation of Mass Transfer Characteristics of the Human Oral Passage

    Source: Journal of Biomechanical Engineering:;1997:;volume( 119 ):;issue: 004::page 476
    Author:
    K.-H. Cheng
    ,
    Y.-S. Cheng
    ,
    D. L. Swift
    ,
    H.-C. Yeh
    DOI: 10.1115/1.2798296
    Publisher: The American Society of Mechanical Engineers (ASME)
    Abstract: This paper presents measurements of the geometric shape, perimeter, and cross-sectional area of the human oral passage (from oral entrance to midtrachea) and relates them through dimensionless parameters to the depositional mass transfer of ultrafine particles. Studies were performed in two identical replicate oral passage models, one of which was cut orthogonal to the airflow direction into 3 mm elements for measurement, the other used intact for experimental measurements of ultrafine aerosol deposition. Dimensional data were combined with deposition measurements in two sections of the oral passage (the horizontal oral cavity and the vertical laryngeal–tracheal airway) to calculate the dimensionless mass transfer Sherwood number (Sh). Mass transfer theory suggests that Sh should be expressible as a function of the Reynolds numper (Re) and the Schmidt number (Sc). For inhalation and exhalation through the oral cavity (O-C), an empirical relationship was obtained for flow rates from 7.5–30.0 1 min−1 : Sh = 15.3 Re0.812 Sc−0.986 An empirical relationship was likewise obtained for the laryngeal–tracheal (L-T) region over the same range of flow rates: Sh = 25.9 Re0.861 Sc−1.37 These relationships were compared to heat transfer in the human upper airways through the well-known analogy between heat and mass transfer. The Reynolds number dependence for both the O-C and L-T relationships was in good agreement with that for heat transfer. The mass transfer coefficients were compared to extrathoracic uptake of gases and vapors and showed similar flow rate dependence. For gases and vapors that conform to the zero concentration boundary condition, the empirical relationships are applicable when diffusion coefficients are taken into consideration.
    keyword(s): Mass transfer , Measurement , Dimensions , Flow (Dynamics) , Heat transfer , Gases , Vapors , Cavities , Trachea , Shapes , Air flow , Reynolds number , Boundary-value problems , Heat , Diffusion (Physics) , Particulate matter AND Aerosols ,
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      Measurements of Airway Dimensions and Calculation of Mass Transfer Characteristics of the Human Oral Passage

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    http://yetl.yabesh.ir/yetl1/handle/yetl/118285
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    • Journal of Biomechanical Engineering

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    contributor authorK.-H. Cheng
    contributor authorY.-S. Cheng
    contributor authorD. L. Swift
    contributor authorH.-C. Yeh
    date accessioned2017-05-08T23:52:45Z
    date available2017-05-08T23:52:45Z
    date copyrightNovember, 1997
    date issued1997
    identifier issn0148-0731
    identifier otherJBENDY-25981#476_1.pdf
    identifier urihttp://yetl.yabesh.ir/yetl/handle/yetl/118285
    description abstractThis paper presents measurements of the geometric shape, perimeter, and cross-sectional area of the human oral passage (from oral entrance to midtrachea) and relates them through dimensionless parameters to the depositional mass transfer of ultrafine particles. Studies were performed in two identical replicate oral passage models, one of which was cut orthogonal to the airflow direction into 3 mm elements for measurement, the other used intact for experimental measurements of ultrafine aerosol deposition. Dimensional data were combined with deposition measurements in two sections of the oral passage (the horizontal oral cavity and the vertical laryngeal–tracheal airway) to calculate the dimensionless mass transfer Sherwood number (Sh). Mass transfer theory suggests that Sh should be expressible as a function of the Reynolds numper (Re) and the Schmidt number (Sc). For inhalation and exhalation through the oral cavity (O-C), an empirical relationship was obtained for flow rates from 7.5–30.0 1 min−1 : Sh = 15.3 Re0.812 Sc−0.986 An empirical relationship was likewise obtained for the laryngeal–tracheal (L-T) region over the same range of flow rates: Sh = 25.9 Re0.861 Sc−1.37 These relationships were compared to heat transfer in the human upper airways through the well-known analogy between heat and mass transfer. The Reynolds number dependence for both the O-C and L-T relationships was in good agreement with that for heat transfer. The mass transfer coefficients were compared to extrathoracic uptake of gases and vapors and showed similar flow rate dependence. For gases and vapors that conform to the zero concentration boundary condition, the empirical relationships are applicable when diffusion coefficients are taken into consideration.
    publisherThe American Society of Mechanical Engineers (ASME)
    titleMeasurements of Airway Dimensions and Calculation of Mass Transfer Characteristics of the Human Oral Passage
    typeJournal Paper
    journal volume119
    journal issue4
    journal titleJournal of Biomechanical Engineering
    identifier doi10.1115/1.2798296
    journal fristpage476
    journal lastpage482
    identifier eissn1528-8951
    keywordsMass transfer
    keywordsMeasurement
    keywordsDimensions
    keywordsFlow (Dynamics)
    keywordsHeat transfer
    keywordsGases
    keywordsVapors
    keywordsCavities
    keywordsTrachea
    keywordsShapes
    keywordsAir flow
    keywordsReynolds number
    keywordsBoundary-value problems
    keywordsHeat
    keywordsDiffusion (Physics)
    keywordsParticulate matter AND Aerosols
    treeJournal of Biomechanical Engineering:;1997:;volume( 119 ):;issue: 004
    contenttypeFulltext
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