1973
DOI: 10.1152/jappl.1973.34.6.866
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Influence of diffusion on dispersion of indicators in blood flow.

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Cited by 30 publications
(21 citation statements)
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“…5 do not fall on the line ut/x = 1 0, is also at variance with accepted indicator dilution theory. This discrepancy, of the indicator dilution theory in laminar flow, was noted by Bate & Sirs (1971) and Bate et al (1973) and has recently been given a theoretical basis by Lane & Sirs (1974). This investigation is supported by a grant from the Wellcome Trust.…”
Section: Discussionmentioning
confidence: 68%
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“…5 do not fall on the line ut/x = 1 0, is also at variance with accepted indicator dilution theory. This discrepancy, of the indicator dilution theory in laminar flow, was noted by Bate & Sirs (1971) and Bate et al (1973) and has recently been given a theoretical basis by Lane & Sirs (1974). This investigation is supported by a grant from the Wellcome Trust.…”
Section: Discussionmentioning
confidence: 68%
“…The simplest situation is to consider solute dispersion to be due to the combined effects of solute diffusion and laminar convection by a parabolic velocity profile. Bate, Rowlands & Sirs (1973), extending the analysis first proposed by Taylor (1953), showed that the dispersion during flow through a tube was determined by a parameter a2iftDx, where D is the diffusion coefficient, a the tube radius, t2 the mean velocity and x the distance 690 D. A. LANE AND J.…”
Section: Introductionmentioning
confidence: 59%
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“…7 Some other authors have also discussed problematic aspects, mostly by use of flow pipe models. [8][9][10][11][12][13][14] The IDT has also been formulated by use of concepts borrowed from the theory of linear ͑stable͒ systems. 2,3,7,15 The use of such a formulation does not, however, demonstrate the validity of the IDT, especially not for all kinds of detectors and labeling processes.…”
Section: Discussionmentioning
confidence: 99%
“…[30e33] and Bate et al [36,37] to obtain solutions related to other regions. Equation 3.4, expressed in terms of Peclet number ðPe ¼ aF=D m Þ, reduced distance ðe ¼ D m x=a 2 F 0 Þ and reduced time (s ¼ D m t/a 2 ), was numerically integrated for all values of s < 0.8 that corresponded to the region of interest for unsegmented flow analysis.…”
Section: Sample Dispersionmentioning
confidence: 99%