2020
DOI: 10.1017/jfm.2020.808
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Vertically distributed wall sources of buoyancy. Part 1. Unconfined

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Cited by 8 publications
(26 citation statements)
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“…For the updated wall‐bounded melt plume parameterization (panel (b)), we also use a smaller entrainment coefficient α = 0.068 (based on Parker et al. (2021)) and much larger Cdp=0.15 ${C}_{d}^{\mathrm{p}}=0.15$ consistent with wall‐bounded melt plumes, commonly‐used turbulent heat and salinity transfer constants of Γ T = 0.022 and Γ S = 6.2 × 10 −4 (based on Jenkins et al. (2010)), and the horizontal velocity using a value of 0.2 m/s from Jackson et al.…”
Section: Application Of Theory To Observations At Leconte Glacier Alaskamentioning
confidence: 99%
“…For the updated wall‐bounded melt plume parameterization (panel (b)), we also use a smaller entrainment coefficient α = 0.068 (based on Parker et al. (2021)) and much larger Cdp=0.15 ${C}_{d}^{\mathrm{p}}=0.15$ consistent with wall‐bounded melt plumes, commonly‐used turbulent heat and salinity transfer constants of Γ T = 0.022 and Γ S = 6.2 × 10 −4 (based on Jenkins et al. (2010)), and the horizontal velocity using a value of 0.2 m/s from Jackson et al.…”
Section: Application Of Theory To Observations At Leconte Glacier Alaskamentioning
confidence: 99%
“…While both and the vertical plume velocity are assumed to adopt ‘top-hat’ cross-stream profiles so that either quantity is uniform within a lateral boundary and zero outside, the interfaces at which they become zero are defined as and , respectively, where is a constant. Due to the wall-shear resistance, the value of is significantly below unity, see § 1 and the supporting data in Parker et al (2021).
Figure 1.Schematic of a simultaneously entraining and detraining wall plume with top-hat cross-stream profiles in a stably stratified quiescent environment with natural, or buoyancy, frequency .
…”
Section: Plume Model With Simultaneous Entrainment and Detrainmentmentioning
confidence: 54%
“… for line plumes (Paillat & Kaminski 2014). However, this ratio substantially drops to , as evaluated from figure 7 of Parker et al (2021), for a wall plume generated by a plane vertically distributed buoyancy source. Clearly, this reduced ratio of thicknesses is due to the wall-shear resistance which results in significantly flatter vertical velocity profiles relative to those of free plumes.…”
Section: Introductionmentioning
confidence: 84%
“…In Part 1 (Parker et al. 2021) of this work we considered a distributed wall-source plume in an unconfined environment by creating a uniform vertical wall source of buoyancy by forcing relatively dense salt water through a porous wall. Here we enclose the apparatus used in Part 1 and perform density measurements to investigate the resulting ambient buoyancy stratification that develops as a result of a distributed wall-source plume in both a confined unventilated environment and a confined ventilated environment.…”
Section: Introductionmentioning
confidence: 99%
“…The rate of descent of the first front must balance the plume volume flux entering the stratified region and the additional source volume flux within the stratified region, i.e. dh/dt = −(Q p + q(H − h))L −1 , where we assume that the plume width is much smaller than L. (Parker et al 2021) of this work we considered a distributed wall-source plume in an unconfined environment by creating a uniform vertical wall source of buoyancy by forcing relatively dense salt water through a porous wall. Here we enclose the apparatus used in Part 1 and perform density measurements to investigate the resulting ambient buoyancy stratification that develops as a result of a distributed wall-source plume in both a confined unventilated environment and a confined ventilated environment.…”
Section: Introductionmentioning
confidence: 99%